30-m-b02-sp-011 tech spec for lp lng & drain pumps_0(all)

CONTENTS

1. GENERAL ..........................................................................................................................................................4

1.1 General..............................................................................................................................................4

1.2 Definitions .........................................................................................................................................4

1.3 Language and units ..........................................................................................................................4

1.4 Design, Standardization and Interchange ability ..............................................................................5

2. SCOPE OF SUPPLY & WORK .............................................................................................................................6

2.1 Items to be purchased ......................................................................................................................6

2.2 Scope of supply.................................................................................................................................6

2.3 Scope of work ...................................................................................................................................7

2.4 Out of scope......................................................................................................................................8

3. PROJECT DESIGN DATA ...................................................................................................................................9

3.1 Site data............................................................................................................................................9

3.2 Utility data.......................................................................................................................................10

4. APPLICABLE CODES AND STANDARDS ..........................................................................................................11

5. INSPECTION AND TESTS ...............................................................................................................................14

5.1 General............................................................................................................................................14

5.2 Shop inspection...............................................................................................................................15

5.3 Site tests .........................................................................................................................................18

6. COORDINATION MEETING .............................................................................................................................19

7. PROTECTION FOR SHIPMENT AND HANDLING .............................................................................................19

7.1 General............................................................................................................................................19

7.2 Quarantine requirements for wood packaging materials ................................................................20

8. SUPERVISION SERVICES AND TRAINING AND FIRST OVERHAUL INSPECTION ..........................................21

8.1 Supervision for installation and site acceptance test ......................................................................21

8.2 Training ...........................................................................................................................................22

8.3 First overhaul inspection .................................................................................................................22

9. GUARANTEE ...................................................................................................................................................22

9.1 Guarantee item list..........................................................................................................................22

9.2 Guaranteed lifetime of major parts based on operation hours .......................................................23

10. SPARE PARTS AND SPECIAL TOOLS ..............................................................................................................23

10.1 Spare parts......................................................................................................................................23

10.2 Special tools ....................................................................................................................................24

11. VENDOR DATA REQUIREMENTS ....................................................................................................................24

11.1 General............................................................................................................................................24

11.2 List of Vendor document and schedule...........................................................................................25

11.3 Vendor document distribution flow schematic ................................................................................28

11.4 Mechanical data book .....................................................................................................................29

12. TECHNICAL BID REQUIREMENT ....................................................................................................................30

12.1 Technical bid summary ...................................................................................................................30

13. DESIGN SPECIFICATION ................................................................................................................................44

13.1 General............................................................................................................................................44

13.2 Casings............................................................................................................................................45

13.3 Nozzle and pressure casing connection ..........................................................................................45

13.4 Impellers & shaft.............................................................................................................................46

13.5 Vibration & balancing ......................................................................................................................46

13.6 Drivers.............................................................................................................................................47

13.7 Bearing ............................................................................................................................................47

13.8 Piping connection ............................................................................................................................48

13.9 Junction box size.............................................................................................................................48

13.10 Miscellaneous requirements ............................................................................................................48

13.11 Name plate......................................................................................................................................49

13.12 Noise ...............................................................................................................................................49

13.13 Material ...........................................................................................................................................50

13.14 Welding requirements .....................................................................................................................50

14. ATTACHMENTS ...............................................................................................................................................52

ATTACHMENT #1. DATA SHEETS

ATTACHMENT #2. P & ID AND RELATED DRAWINGS

ATTACHMENT #3. RELATED SPECIFICATIONS

ATTACHMENT #4. PURCHASER’S STANDARD FORMS

1. GENERAL

1.1 General

Korea Gas Corporation (KOGAS) is constructing new LNG terminal – SAMCHEOK LNG Receiving

Terminal (hereinafter called as SAMCHEOK LNG Terminal). The terminal which is located about

200km the south-east of Seoul on the eastern coast of Korea, will be constructed step by step depending on gas demand.

This specification, the associated data sheets and attachments, is issued to cover outline the minimum requirements for the design, fabrication, construction, testing, inspection and supply of LP

LNG Pumps (P-201A/B/C ~ P-207A/B/C) & LNG Drain Pumps (P-102, P-305) and auxiliary equipment for Phase I – 2nd Project & Phase II -1st Project of SAMCHEOK LNG Terminal.

1.2 Definitions

Purchaser or

Owner or

KOGAS

Korea Gas Corporation

Head office:

171 Dolmaro(215,Jeongja-dong), Bundang-gu, Seongnam, Gyeonggi-do, 463-754,

Korea

TEL : 82-31-7100-114

FAX : 82-31-7100-117/118

Samcheok office:

18 Hosan beach, Wondeok-Eub , Samcheok City, Gangwon-do,245-803, Korea

TEL : Later

FAX : Later

Engineer or

PEN

POSCO Engineering Co., Ltd. which is the engineering company engaged by

KOGAS for terminal detail engineering and supervision services.

246 Hwangsaeul-ro, Bundang-Gu, Seongnam City, Korea, 463-825

TEL : 82-31-738-0481

FAX : 82-31-738-0465

Vendor or

Contractor or

Supplier

The person or firm of company whose tender has been accepted by the Purchaser

and includes the supplier‟s duly appointed representatives, successors and

permitted assigns.

1.3 Language and units

1.3.1 Language

All documents and drawings to be submitted shall be lettered in English or Korean.

1.3.2 Units

Following international SI units shall be applied throughout for all documentation, drawings, manuals, etc. and for charts and scales on instruments. Other units not specified herein shall

not be used unless approved by Purchaser.

Glossary Units Glossary Units

Acceleration m/s2 Heat transfer coefficient W/(m2.K), W/(m2.oC)

Area m2 Luminance (light) lx (Lux) (lx = lm/m2)

Density kg/m3 Length mm (piping size – inch), cm, m

Electric conductance mho Mass kg, t (Ton)

Glossary Units Glossary Units

Electric conductivity mho/cm Moment, torque N.m, kN.m

Electric conductor (wire) size mm2 Power W, kW

Electric current intensity A (ampere) Pressure, fluid Pa, kPa, Mpa

Electric resistance Ω (ohm) Pressure, barometric Pa, kPa

Energy, electrical kW.h Sound level dB(A)

Energy, mechanical J, kJ, MJ Stress N/mm2, N/cm2

Energy, thermal J, kJ, MJ Temperature oC (Celsius), K (Kelvin)

Flow, mass kg/h Thermal conductivity W/(m.K), W/(m.oC)

Flow, volumetric m3/h Time h (hour), min (minute),

s (second), d (day)

Force N, kN Velocity m/s

Fouling factor m2.K/W, m2.oC/W Viscosity, absolute, dynamic cP (centipoises)

Frequency Hz Voltage V (Volt)

Heat capacity, specific J/(kg.K), J/(kg.oC) Volume m3

Heat content or enthalpy J/kg

1.4 Design, Standardization and Interchange ability

1.4.1 All parts of the equipment to be designed and manufactured in accordance with the latest

acceptable degree of workmanship and modern engineering practice.

1.4.2 The equipment shall be designed to operate satisfactorily under all variations of load, pressure and temperature as may be met in normal usage and under local climatic conditions.

1.4.3 The works shall be designed to facilitate inspection, cleaning, maintenance and repair. The design shall incorporate every reasonable precaution and provision for the safety of all those

concerned in the operation and maintenance of the works.

1.4.4 Unless otherwise specified all parts of the equipment must be suitable in every respect for continuous operation at maximum output under the climatic and operation conditions peculiar

to the erection site.

1.4.5 For the equipment, only those design and machine types that comply with below requirements

shall be offered.

- It has been supplied and/or manufactured for LNG service with flow rate & diff. head equal

to or more than 220m3/hr and 200m.

Vendor shall include all supporting evidence for above eligibility in his proposal.

1.4.6 Parts subject to wear shall be easily accessible and removable whenever possible adjustment

shall be provided for taking up wear.

1.4.7 All equipment performing similar duties shall be of the same type and manufacture, in order to

limit the stock of spare parts required and to maintain uniformity of equipment to be installed.

1.4.8 In case Bidder opposes to the Purchaser‟s Technical Bid Evaluation, Bidder may solicit perusal of its own Technical Bid Evaluation Sheet only before opening of commercial bid.

1.4.9 Purchaser reserves the right to ask for coordination of standardization to the extent reasonably possible and no price variation will be allowed for this procedure.

1.4.10 Symbol and Legend

Standard symbol and legend including line and equipment identification shall be applied to this

project for unification in Purchaser. Unless specified in the attachment of this specification,

Vendor's standard symbol and legend may be applied with the Purchaser‟s approval.

2. SCOPE OF SUPPLY & WORK

2.1 Items to be purchased

The following item shall be furnished in accordance with the requirements specified in this

specification and other related documents.

ITEM No. Q’TY SERVICE REMARKS

LP LNG Pumps

P-201A/B/C 3 sets LP LNG Pumps for TK-201 330m3/hr x 270m







LNG Drain Pump

P-102 1 set Unloading Line Drain Drum Pump 40m3/hr x 310m

P-305 1 set Process Area Drain Drum Pump 40m3/hr x 310m

Total 23 sets

All the related costs to be incurred by designing, documentation and tests & inspections at the vendor's factory shall be included in the cost of the materials.

The Vendor shall supply of all materials, equipment and services for the complete installation within the specified terminal points and battery limits with the exception only of those details specifically

stated herein as being supplied by others.

The equipment shall be completely assembled and fabricated to obtain maximum shop assembly of all component parts and auxiliary equipment within the maximum permissible transportation.

2.2 Scope of supply

Vendor‟s scope of supply shall include, but not be limited to:

[ Common for both LP LNG Pumps and LNG Drain Pumps ]

1) Each pump unit, complete with integral electrical motor

2) Head plate with connecting bolts/nuts/gaskets

3) Foot valve with connecting bolts/nuts/gaskets

4) Electric power & instrument cables including earthing cables with the length proper for pump to junction box on the top of tank (But, the instrument cable for LNG Drain Drum Pump to be

excluded.)

5) Junction boxes for electric and instrument cables with N2 purge connection (But, the junction box for instrument of LNG Drain Drum Pump to be excluded.)

6) Complete removable system including:

Lifting cable with reels, the reels shall be fixed on head plate

Support cable with all accessories clamps, turnbuckles rings

Guide and roller-guide

Grounding straps

Cryogenic electrical supply with the connections on the motor

7) Anti-spin fixture to prevent cables from twisting

8) Basket protection screen on top of pumps to catch falling debris and tools

9) Nitrogen purge system for double penetration seals with valves, regulators, pressure

indicators, pressure transmitters, piping and other as indicated in attached P &ID (The instrument and valves shall be pre-assembled and mounted on skid with setting bolts/nuts)

10) All supports and foundation bolting, shims and accessories necessary for the setting,

adjustment and anchorage of the equipment supplied

11) Lifting eyes, screw jacks, and special tools required for installation, operation and

maintenance (in new and first-class condition)

12) Spare parts for installation and commissioning

13) Nameplates

14) All documents required by this specification (Vendor shall submit all Vendor documents by

web based KOGAS Project Management Information System. Refer to Attachment #3. “Usage

of Vendor Prints Information System”)

15) All necessary components, accessories and appurtenances, as normally provided, whether

mentioned in this specification or not

[ Scope of LP LNG Pumps only ]

16) Instrumentation for each pump with

Dual vibration sensors: all sensors shall be able to be interface with SHINKAWA infisys

RV-200 VM-7B system. (Vendor shall recommend the specification of vibration signal

cable)

Interface module installed in proper housing (junction box)

17) Dummy pump (1 set)

The vendor shall provide all materials needed for site assembly and installation of the Pump(s) and

their ancillaries (gaskets, fittings, couplings, electrical interconnecting cables etc.) together with any special tools or equipment needed for assembly and normal maintenance.

Dummy pumps & Foot valves, if any, shall be delivered to Purchaser‟s site prior to equipment delivery in accordance with site construction schedule upon Purchaser‟s written request.

2.3 Scope of work

1) Data for column vibration analysis and the static & dynamic loading data with various directions

2) KOSHA (Korean Occupational Safety & Health Agency), KTL (Korea Testing Laboratory) or KGS (Korean Gas Safety Corporation) certificates for explosion proof type electric equipment and

instruments (see Section 5.1.8)

3) KGS certificates for safety, shut-off (on-off) ball and globe valves for gas system (see Section

5.1.8)

4) Painting up to finish coating at shop and touch-up painting at site

5) Coordination meeting

6) Supervision for installation, commissioning and site acceptance test

7) Training for Purchaser‟s trainees

8) Packing for export and site storage for 6 months

9) Inspection and test required by this specification

10) Performance guarantee

11) Review of Purchaser‟s column drawings

2.4 Out of scope

1) Columns for pump installation

2) LNG Tank & Drum

3) All piping and instrument work except those specified to be provided by Vendor

4) All external power and control wiring without the battery limits

5) Field installation of equipment

6) Vibration module rack with power supply system (non-hazardous area)

7) Spare parts for 2-years operation (But, the recommended spare parts list with itemized price list shall be submitted for Purchaser‟s review.)

3. PROJECT DESIGN DATA

3.1 Site data

3.1.1 Plot plan

Ground elevation : EL. +6.0 m (relative to MSL)

Seawater intake & B-C tank area : EL. +6.0 m LNG tank area, process area, utility area : EL. +6.0 m

3.1.2 General site data

1. Nature of terrain : Prepared cut and profiled site, part reclaimed land

2. Air pollution precaution : Yes

3. Air corrosiveness : Yes

4. Vibration transmittal

precautions

: Yes Earthquake zone in accordance with NFPA

59A and see 10, Earthquake data

5. Noise precautions : Yes 85dB(A) max at 1m from equipment

125-140 dB(A) max for relief valves

50 dB(A) max at terminal battery limit

6. Water pollution precautions : Yes

7. General earthquake data :

a. Operational basis earthquake (OBE) parameters

Peak ground acceleration = 0.1 g

Peak ground velocity = Refer to UBC 1997

Peak ground displacement = Refer to UBC 1997

b. Safe shutdown earthquake (SSE) parameters

Peak ground acceleration = 0.2 g

Peak ground velocity = Refer to UBC 1997

Peak ground displacement = Refer to UBC 1997

c. For equipment items that are designed for SSE, allowable stresses are to be

determined in accordance with NFPA-59A, 4-1.3.5 as permitted by UBC 1997, sections

1634.1.2 alternative 2, or 1643.4, where I =1.0 for all items.

Item Facilities Design Seismic Remark

Mechanical LP LNG Pumps & Drain pumps SSE 0.2g

3.1.3 Wind and barometer

Prevailing direction by height : Southwest

Prevailing velocity (mean) : 3.6 m/sec

Design velocity : 45 m/sec @ 10m elevation Average monthly wind velocity [m/s]

Month 1 2 3 4 5 6 7 8 9 10 11 12

Wind Vel 4.2 4.0 2.6 2.8 2.6 2.2 2.5 2.2 1.9 1.8 2.1 2.1

Barometric pressure (Min./Avg./Max.) : 97.28 / 101.63 / 104.23 kPa.a

3.1.4 Air temperatures

Maximum summer : 37 °C Minimum winter : -14.1 °C

Winter design : -14.1 °C Mean annual : 12.5 °C

Average monthly temperatures [°C]

Month 1 2 3 4 5 6 7 8 9 10 11 12

Temperature 1.0 1.9 6.0 11.9 16.1 19.0 22.9 23.8 19.8 14.9 9.0 3.6

Black body temperature : 65 °C

Relative humidity (Min./Avg./Max.) : 6.0 / 68.7 / 90 % Design relative humidity for cold service : 82 %

3.1.5 Precipitation

Design rainfall : Precipitation shall be calculated for a

1 in 50 year return period as:

hrmmt

I /81.1

75550

Where t= period in minutes

Design snow loading : 300 kg/m2

Paved area runoff : 100% Unpaved area runoff : 10%

3.2 Utility data

In case vendor‟s equipment/system requires utilities of lower voltage or pressure than available as specified in this section, Vendor shall provide regulator(s) to adjust the voltage or pressure as

required, unless specifically exempted in this specification.

3.2.1 Electric power utilisation

Motors

a) above 149.2 kW 6.6 kV 3 ph 60 Hz

b) 0.56 kW to 149.2 kW 440 V 3 ph 60 Hz

c) below 0.56 kW for process critical service,

including lube oil pumps

440 V 3 ph 60 Hz

d) below 0.56 kW for non-process service 220 V 1 ph 60 Hz

Heaters

a) above 7 kW 440 V 3 ph 60 Hz

b) above 3.1 kW to 7 kW 440 V ph-ph 60 Hz

c) 3 kW and below 220 V 1 ph 60 Hz

d) space heaters for panels 220 V 1 ph 60 Hz

e) space heaters for 6.6 kV motors 220 V 1 ph 60 Hz

f) space heaters for LV motors (if necessary) 220 V 1 ph 60 Hz

g) trace heating 440 V 3 ph 60 Hz

Instrumentation and communications

a) Instrumentation – critical 115 V UPS 1 ph 60 Hz

b) Instrumentation – non-critical 220 V 1 ph 60 Hz

c) Communications 115 V UPS 1 ph 60 Hz

Notes:

1. Voltage variation ± 10%

2. Frequency variation ± 5%

3. Where equipment requires voltages not listed above the equipment supplier shall provide

the appropriate transformers, rectifiers etc.

3.2.2 Nitrogen

Liquid nitrogen will be imported by road tankers, and will be supplied through storage tank and

vaporizers.

Operating pressure : Low pressure N2 : Normal 0.785 MPa.g

Design 0.981 MPa.g

: for column and accessories of LP pump : 0.294Mpa.g Oxygen content : Less than 80ppm

Water content : Dry Misc. Impurities : CO2 and oil free

4. APPLICABLE CODES AND STANDARDS

Reference to standards and codes in this specification and the data sheets shall mean the latest edition thereof plus all amendments ruling at the time of tendering, unless otherwise specified. Vendor shall be

ultimately responsible for all aspects of the equipment supplied regardless of source and shall be

responsible for ensuring compliance with all applicable regulations, code and standards including followings:

LNG pumps

API 610 11th Centrifugal Pumps for Petroleum, Petrochemical and Natural Gas Industries

(where applicable)

Pressure vessels and welding

ASME Sec. II Material Specification, Part C – Welding Rods, Electrodes and Filler Metals

ASME Sec. II Material Specification, Part D – Properties

ASME Sec. V Nondestructive Examination

ASME Sec. VIII, Div.1 Pressure Vessels

ASME Sec. IX Welding and Brazing Qualification

AWS standards

Piping (cryogenic and non-cryogenic)

ASME B1.20.1 Pipe Threads

ASME B16.5 Pipe Flanges and Flanged Fittings

ASME B16.9 Factory Made Wrought Steel Butt weld Fittings

ASME B16.11 Forged Steel Fittings

ASME B16.28 Wrought Steel Butt welded, Short Radius Elbows and Returns

ASME B16.47 Large Diameter Steel Flanges

ASME B31.3 Process Piping

ASME B36.10 Welded & Seamless Wrought Steel Pipe

Electrical

IEC 60034 Rotating Electrical Machines

IEC 60079 Electrical Apparatus for Explosive Gas Atmospheres

CENELEC

NEC

NEMA MG-1 Motors and Generators

ANSI

NFPA

Korean Industrial Standard (KS)

JIS

API

IEEE

NACE

KOSHA, KTL or KGS (for enclosure of hazardous service)

Hazardous area

Korean regulation, ACT 1993-19, Ministry of Labor, May, 1993

NFPA 59A Standard for Production, Storage and Handling of Liquefied Natural Gas

NFPA 497A Classification of Class I Hazardous (Classified) Locations for Electrical

Installations in Chemical Process Areas

IEC 60079-10 Electrical apparatus for Explosive Gas Atmospheres - Classification of Hazardous Areas

IP (Institute of Petroleum) Model Code of Safe Practice, Part 15

For Zone 1:

IEC 60079-1 or EN 50018 for Flameproof (Ex d)

IEC 60079-11 or EN 50020 for Intrinsically Safe (Ex i)

IEC 60079-2 or EN 50016 for Pressurized (Ex p)

For Zone 2:

All above same

(The EN designation refers to CENELEC/ Euronorm manufacturing standards.)

Instruments

ASME B1.20.1 General purpose pipe thread

ASME B16.5 Pipe Flanges and Flanged Fittings

ASME B46.1 Surface Texture

API 550 Manual on Installation of Refinery Instruments and Control Systems

API 670 Vibration, Axial Position and Bearing Temperature Monitoring System

API 678 Accelerometer Based Vibration System

ISA RB31.1 Specification, Installation & Calibration of Turbine Flow Meters

ISA S75.01 Flow Equation for Sizing Control Valves

ISA S5.1 Instrumentation in Symbols and Identification

ISA S5.2 Primary Logic Diagrams for Process Operation

ISA S5.3 Graphic Symbols for Distributed Control/Shared Display Instrumentation, Logic and Computer Systems

ISA S18.1 Annunciator Sequences and Specifications

IEC 60034-1 Rotating Electrical Machines - Rating and Performance (Motor Operated Valves)

IEC 60073 Basic and Safety Principles for Man-Machine Interface, Marking and Identification - Coding Principles for Indication Devices and Actuators

IEC 60079 Electrical Apparatus for Explosive Gas Atmosphere

IEC 60529 Degrees of Protection Provided by Enclosures (IP Code)

IEC 60584 Thermocouples

IEC 60654 Industrial Process Measurement & Control Equipment

IEC 60751 Industrial Platinum Resistance Thermometer Sensors

IEC 60801 Electromagnetic Compatibility for Process Measurement and Control Equipment

ISO 5167-1 Measurement of Fluid Flow by means of Orifice Plates, Nozzles and Venturi Tubes

ISO 8310 Refrigerated Light Hydrocarbon Fluids

KGS (for safety valves, shut-off (on-off) ball & globe valve for LNG, NG and fuel gas system)

KOSHA, KTL or KGS (for enclosure of hazardous service)

JIS

Safety

NFPA 59A Standard for Production, Storage and Handling of Liquefied Natural Gas

Environmental Regulations

Korean local regulations

Earthquake Design

UBC, ANSI A58.1, NFPA-59A

Korean local regulations

Material

ASTM/ASME, JIS, KS

Painting & insulation

Purchaser‟s specification

Note: Korean local regulation shall be applied for all equipment, if applicable. Vendor shall be responsible for determining and complying with the requirements of all applicable local

regulations (laws, acts, regulations, etc.) current at the time of proposal.

In case of any inconsistency happens between above-mentioned codes and standards, Vendor shall ask

written resolution to Purchaser.

5. INSPECTION AND TESTS

5.1 General

5.1.1 Inspection and tests shall be performed in accordance with this specification, Vendor‟s Final

documents approved by Purchaser, the applicable codes and standards.

5.1.2 Purchaser or its representatives reserve the right to access freely to all parts of the shop where fabrication is in progress, and to witness and inspect the shop tests and inspections at any

time and place including sub-Vendor's works.

5.1.3 The manufacturer shall provide the inspectors with all the means necessary to verify the

equipment is being properly manufactured in accordance with the terms of the order.

5.1.4 Vendor shall conduct, at its own expense and responsibility, the tests and inspections required

under contract documents. In the event Purchaser‟s or its representative's witnessed inspection

is required, the costs, fees and expenses arising therefrom shall be borne by Vendor, with the exception of Purchaser's cost and expenses for dispatching inspectors.

5.1.5 All inspection and tests required by this specification shall be done by 3rd party inspector(s) for the product and major sub-assemblies irrespective of place/country of manufacturer/assembly.

The 3rd party inspector(s) shall be one of Lloyd‟s Register Verification, TÜV Rheinland Group,

DNV (Det Norske Veritas), ABS Consulting INC, BV (Bureau Veritas), HSB (The Hartford Steam Boiler Inspection & Instrance Co.) and KR (Korean Register of Shipping), subject to approval of

Purchaser‟s QA/QC department. All cost, fees and expenses for the 3rd party inspector shall be borne by Vendor.

The 3rd party inspector shall directly submit the final inspection report and certificate signed by the 3rd party inspector(s) for Purchaser‟s approval before shipment.

If the inspection and test shall be witnessed by Purchaser, Vendor shall notify to Purchaser‟s

QA/QC team before two (2) weeks for the products manufactured in foreign country, and one (1) week for the products manufactured in domestic prior to the actual date of inspection and

test.

The 3rd party inspection shall be performed in accordance with Purchaser‟s 3rd party inspection

work & flow schematic (Refer to Attachment #3).

5.1.6 The below table is shown the typical inspection and test plan by 3rd party inspection agency, and Vendor shall prepare detail inspection and test plan with each item marked with type of

activity (“Review”, “Witness” or “Hold”, etc.) and inspection party (Manufacturer, Vendor, Purchaser, 3rd party inspection agency, etc) for Purchaser‟s approval.

No. Inspection and Test Item Activity

Remarks Vendor 3rd Party KOGAS

1. Welding check V R R

2. Material inspection V R R

3. Non-destructive examination V R R

4. Visual and dimensional check V W R

5. Pressure test V W R

6. Assembly check V H SW

7. Cold hand spin test V H SW

8. Performance test at shop V H SW

9. Dismantle inspection V H SW

10. Motor test V H R

11. Electric equipment & instrument V R (or SW) R

12. Painting inspection V W R

No. Inspection and Test Item Activity

Remarks Vendor 3rd Party KOGAS

13. Packing and marking inspection V H R

14. Others

- Column foot valve V H R

- Shaft stabilization in liquid nitrogen V SW R

LEGEND

V Vendor to provide H Hold point

R Review of documentation and/or Certificates W or SW Witness or Spot Witness

5.1.7 Explosion proof type electric equipment & instruments are required to be certified by IEC Ex Certification Bodies (http://www.iecex.com/directory/bodies/bodies1.asp?id=5). Vendor should

submit the certificate, test report and QAR (Quality Assessment Report) from KOSHA, KTL or KGS for approval to KOGAS before site commissioning and acceptance test

The procedure of safety certification for approval from KOSHA, KTL or KGS shall be followed to

under article 34 of Korean industrial safety health law

5.1.8 For the safety valves, shut-off (on-off) ball and globe valves of LNG, NG and fuel gas system,

Vendor shall obtain KGS certificates, and those valves shall be stamped on the body by KGS.

5.2 Shop inspection

Vendor shall provide detailed test procedures to verify the parameters listed in this paragraph, and

the test procedures shall be reviewed & approved by Purchaser.

The test procedures shall be included the detail method & frequency of calibration of measuring

instruments.

Vendor shall specify in the test procedure the formulae for conversion calculation in detail, and shall

justify any deviation from site conditions during shop test, if possible.

5.2.1 Welding check

The edge preparation, welding materials, preheat and interpass temperature (if applied) shall

be checked during welding in accordance with applicable welding procedure specification and fabrication drawings. Visual inspection of weldments for pressure containing parts shall be

made in accordance with ASME Sec. VIII Div.1.

Test pieces (per welding process) for pressure parts containing LNG or fuel gas only shall be

sampled from production in order to carry out the following tests;

- Tensile test

- Guide bend test

- Impact test (at -196°C)

The resilience values obtained in the transition and fusion zones shall be at least equal to those required by the base metal.

5.2.2 Material inspection

The material applied shall be checked for conformity with the requirements of this specification and applied code and standards.

Material of major parts subject to pressure, cyclic loading, power transmission, and parts containing flammables shall be tested for mechanical property and the Vendor shall submit

chemical composition and certificate for Purchaser‟s review.

Pressure casting repairs shall be carried out in accordance with ASTM specification for similar material. All repairs shall be subject to inspector‟s approval.

http://www.iecex.com/directory/bodies/bodies1.asp?id=5

5.2.3 Non-destructive examination

The following non-destructive examination shall be performed in accordance with applicable

code and standards.

1) Radiographic examination shall be applied for:

- Butt weld pressure parts of LNG or fuel gas system (100% RT)

- Pump casings

The film shall be reviewed by Purchaser or 3rd party inspector. Interpretation and

acceptability of welds shall be made as per ASME Sec. VIII, Div. 1 or ASTM E155 for

aluminium castings.

2) Dye penetrant inspection shall be applied for:

- All non-radiographic tested welding joints for LNG or fuel gas system

- Pump impellers

Acceptance criteria shall be as per ASME Sec. VIII, Div. 1 or ASTM E165

3) Ultrasonic inspection shall be applied to:

- Pump shafts

5.2.4 Visual and dimensional check

Every part shall be inspected and it shall be confirmed that there are no harmful blowholes,

dusts, cracks, and cavities.

The main dimensional such as diameters, lengths, etc shall be checked according to fabrication

drawings.

5.2.5 Pressure test

All pressure containing parts including pump casing, double penetration seal and separating

conduit, etc, shall be tested at 1.5 times the maximum allowable working pressure for at least 30 minutes or over.

The hydrostatic test(s) will be performed in order to confirm that there is no deformation, damage or leakage from welded areas and flange connections. Such test(s) shall be executed

prior to painting.

The test pressure shall be continuously recorded on a chart by automatic recorder during pressure test. Vendor shall submit the test record sheet for Purchaser's approval.

In case of test using water, only clean fresh water of pH value between 6 and 8 shall be used for hydrostatic testing. Chloride content shall be less than or equal to 200 ppm for carbon steel,

below 10 ppm for austenitic stainless steel (as applicable).

The test may utilize water and/or nitrogen depending the impossibility of perfect drying after testing and the difficulty of freely replacing the water by a more volatile liquid, subject to

acceptance of purchaser and inspection authority. In addition, the double penetration seal shall be leak tested with Helium gas.

After hydrostatic testing, the equipment shall be thoroughly dried with dry air or N2 and Vendor shall be responsible for consequences due to poor drying. Complete drying of all parts

contacting with handling liquid shall be achieved with a dew point of –40oC, and the equipment

shall be sealed immediately after affixing desiccant bags.

5.2.6 Assembly check

All parts shall be assembled in the shop to confirm their proper fit within the limits prescribed in working drawings. Lifting system shall be checked for it‟s mechanical integrity and proof

tested for the lift and support cables.

Extent of shop assembly shall be described in Vendor‟s test procedure.

5.2.7 Cold hand spin test

Cold hand spin test using liquid nitrogen shall be performed for all pumps before performance

test unless they are performance tested with cryogenic liquid.

5.2.8 Performance test

The Performance test shall be witnessed jointly by the inspectors of Purchaser and 3rd party inspection agency.

It is preferred that all pumps shall be tested on LNG at the rated temperature with the rated

electrical supply at the motor terminals. Vendor may offer testing using alternative cryogenic fluids if LNG test facility is not available to Vendor, and must submit, with the proposal, a

technical justification for the alternative fluid.

Unless specific exception is taken in the proposal and agreed by the Purchaser in writing, all

running, performance and NPSH tests shall be performed with the pump in its normal

operating position (i.e. with the shaft vertical).

Performance test shall be carried out for all pumps at 5 points, such as shut-off, minimum

continuous flow, flow between minimum continuous flow and rated flow, rated flow, maximum flow, which shall be more than 120% of rated flow.

During the performance test, followings shall be checked in addition to those required by applicable code and standards:

- Flow rate, suction and discharge pressure

- Pressure pulsation

- Liquid temperature of suction and discharge, specific gravity

- Vibration (displacement and velocity)

- Noise level

- Current, voltage and frequency

- Input power

- NPSH re (at all test points for one pump of each item, remainder pumps at only rated

point)

- Liquid level, etc

Motor starting current shall be measured for each test.

Minimum pump-down level and minimum start-up level test shall be performed for all pumps.

Thrust balance mechanism shall be tested by measuring shaft axial movement for all pumps.

To gain acceptance by the Purchaser the equipment shall be guaranteed to meet the specified

rated duty with the tolerances listed in table 16 of API 610, 11th Edition.

Additionally, vibration levels shall be guaranteed not to exceed the levels specified in API 610,

11th Edition.

5.2.9 Dismantle inspection

The Dismantle inspection shall be witnessed jointly by the inspectors of Purchaser and 3rd

party inspection agency.

After the performance test, the pumps shall be dismantled, and the condition of the major

components shall be checked according to Vendor‟s standard. If mechanical deficiencies including minor scruffs and scratches occur on bearing or impeller surfaces, these parts shall

be repaired or replaced and shop running test specified herein shall be performed again if

required in the judgement of the inspectors of Purchaser and 3rd party inspection agency.

5.2.10 Motor test

The following tests shall be carried out on each motor as a minimum:

- Visual inspection

- Measurement of winding resistance at ambient temperature and at the temperature which

will exist prior to start-up (when not recently run).

- High voltage test plus insulation resistance before and after pump performance test.

- Measurement of starting current and run up time under cold conditions.

- Pump start test at minimum voltage and operating temperature

Note:

It is recognised that any running tests of the motor can only be conducted after the pump is

assembled, and submerged in the test tank.

5.2.11 Electric equipment & instrument

1) Leak tightness and electrical integrity shall be checked for all electrical and instrument

seal assemblies.

2) All cables shall be checked for their electrical integrity.

3) Cables shall be checked for flexibility by immersing in liquid nitrogen and bending to minimum radius. The cryogenic cable test may be exempted if test certificate is available

for identical test and the same cable.

5.2.12 Painting inspection

Inspection items such as surface preparation, first and final coat thickness, coating integrity

and their allowable limits shall be specified in the procedure.

Surface preparation and colour of the coat shall be checked and coat thickness and integrity of

the coat shall be examined by suitable gauge.

5.2.13 Packing and marking inspection

Packing and marking shall be checked in conformity with related specification.

5.2.14 Other tests

1) Column foot valve

All column foot valves shall be tested at operating or at liquid nitrogen temperature for function and sealing capability.

2) Shaft stabilization in liquid nitrogen

All shafts shall be immersed into liquid nitrogen several times and their straightness shall be checked.

5.3 Site tests

Testing procedures including list of instrument & accuracy shall be prepared by Vendor, and

approved by Purchaser in writing prior to execution.

Site tests shall be performed by Purchaser under the supervision of Vendor.

5.3.1 Pre-commissioning and commissioning

Pre-check and test operation shall be carried out for all system including piping, instrument, and system function, etc. Line flushing, dry-out, and purge, etc. shall be performed during pre-

check stage as required.

5.3.2 Site acceptance test

1) To verify pump performance and guaranteed design data, site acceptance test shall be

performed by Purchaser under the witness of Vendor for at least twenty four (24) hours.

2) The test shall be performed according to site test procedure, which is prepared by

Vendor and approved by Purchaser.

3) Site acceptance test shall be performed for all pumps under the condition of min.

continuous flow, rated flow and max. flow (120% of rated flow).

The below items shall be checked during site acceptance test, but not be limited to:

- Capacity [m3/hr]

- Differential pressure [MPa]

- Input power (kW) & current [Amp.]

- Vibration [mm/s RMS]

- Noise [dB(A)]

If the equipment does not meet the guarantee performance values including allowances specified in this specification or applicable codes, Vendor shall take any corrective action

under Vendor‟s sole responsibility and cost.

5.3.3 Approval on the site acceptance test

The site acceptance will be noted with written consent or approval of Purchaser. The site

acceptance test certificate will be written with Purchaser‟s standard form in Attachment #4.

To gain approval by Purchaser, the equipment shall meet the guarantee performance values for

site acceptance test items and mechanical data book package (for final) shall be submitted.

6. COORDINATION MEETING

After the bidder is awarded, Kick off meeting shall be held upon Purchaser‟s request to facilitate communication on technical matters, and the coordination meetings shall be held to check the design and

manufacturing process at least two times free of charge.

Vendor shall dispatch a sufficient number of qualified personnel to attend the coordination meetings, if the meeting held at purchaser‟s office.

7. PROTECTION FOR SHIPMENT AND HANDLING

7.1 General

All gasket surfaces, flange faces and machined or ground metal surfaces shall be thoroughly cleaned, greased & protected with suitable wood, metal, or other substantial-type covering to insure their full

protection.

All exposed threaded parts shall be greased and protected with metallic or other substantial type

protectors.

All female threaded connection shall be closed with forged steel pipe plugs or snap-in protection

plugs. Cast-iron pipe plugs will not be acceptable.

Suitable weather protection, blocking straps and skids shall be provided to protect the equipment from damage in transit and during storage.

All loose piping shall be properly protected by an appropriate corrosion inhibiting material and all ends openings shall be closed securely with substantial closures to prevent damage and entry of

foreign material. Small loose parts shall be protectively wrapped and packaged cartons and crates

and tagged or marked with permanent identification.

7.2 Quarantine requirements for wood packaging materials

All wood packaging materials for all imported consignments shall be subject to quarantine

requirements of National Plant Quarantine Service, under the sole responsibility of Vendor.

7.2.1 Regulated articles

All non-manufactured wood packaging materials (WPM) such as pallets, crating, dunnage, packing blocks, etc

7.2.2 Exempted articles

Plywood, veneer panel, particleboard, oriented strand board, wafer board, fiber board, densified wood, glued laminated wood, agglomerated cork, pulp, wood wool, wood flour,

ground cork

7.2.3 Regulated areas

All countries

7.2.4 Requirements

1) All imported wood packaging materials should be treated by one of the following

methods, and present the mark which certifies the approved treatment on two opposite sides of the wood packaging material.

2) Treatment methods

(1) Heat Treatment (HT)

WPM must be heated in accordance with a specific time-temperature schedule that a

minimum temperature of 56℃ for a minimum duration of 30 continuous minutes throughout the entire profile of the wood (including at its core)

(2) Methyl Bromide (MB) fumigation

WPM must be fumigated with methyl bromide in accordance with a schedule that

achieves the minimum concentration-time product (CT) over 24 hours at the

temperature and final residual concentration specified in table 1.

This CT must be achieved throughout the wood, including at its core, although the

concentrations would be measured in the ambient atmosphere. The minimum

temperature of the wood and its surrounding atmosphere must be not less than

10℃ and the minimum exposure time must be not less than 24 hours.

Monitoring of gas concentrations must be carried out at a minimum at 2.4 and 24

hours.(in the case of longer expose times and weaker concentrations, additional

measurement should be recorded at the end of fumigation)

Table 1. Min. CT over 24 hours for wood packaging material fumigated with methyl

bromide

Temperature CT (g.h/m3) over 24hr Min. final concentration

(g/m3) after 24hr

21 oC or above 650 24



Table 2. Example of a treatment schedule that achieves the minimum required CT for

wood packaging material treated with methyl bromide(initial loses may need to be

higher in conditions of high sorption of leakage)

Temperature Dosage rate Minimum concentration (g/m3) at

0.5 hrs. 2 hrs. 4 hrs. 16 hrs.

21 oC or above 48 36 24 17 14

16 oC or above 56 42 28 20 17

11 oC or above 64 48 32 22 19

Provided, Wood packaging material made of Pinus spp., Larix spp., Cedrus spp. from

Japan, China, Taiwan, US, Canada, Mexico, Portugal and Wood packaging material

made of Pinus spp. from Vietnam should be fumigated with methyl bromide for 24

hours. The treatment standard is as follows. The minimum temperature should not

be less than 10 oC and the minimum exposure time should be 24 hours.

3) The Mark should contain the valid symbol approved by IPPC, country code, unique

number of the producer / treatment facility designated by the National Plant Protection Organization (NPPO) of exporting countries and treatment methods (HT, MB).

7.2.5 Non-compliance measures

1) Wood packaging material without approved mark : Disposal or Return to the origin

2) Wood packaging material with approved mark but with live regulated pests : Treatment

or Disposal or Return to the origin

7.2.6 Marking for approved measures

XX-00000

HT or MB

1) Symbol

2) ISO two letter country code followed by a unique number assigned by the NPPO to the

producer of the wood producer of the wood packaging material, who is responsible for ensuring appropriate wood is used and properly marked.

3) IPPC (International Plant Protection Convention) abbreviation for the approved measure used (e.g HT, MB).

8. SUPERVISION SERVICES AND TRAINING AND FIRST OVERHAUL INSPECTION

8.1 Supervision for installation and site acceptance test

The Vendor shall take the full responsibility for proper quality and function of the goods supplied by the vendor. For this purpose, the Vendor shall dispatch to the Purchaser's site its qualified

supervisor(s) who shall provide technical direction and shall perform the duties as required to assure

proper installation and successful operation of the goods under the conditions of actual operation.

The supervisor(s) shall have a good knowledge of instrumentation and control for all equipment

supplied by Vendor and/or sub-Vendor.

The manpower requirement for the supervision services including instrument supervisor shall be Six

(6) man-months as specified below:

1) Four (4) man-months during the installation period

2) Two (2) man-months during site acceptance test

The Vendor shall include the price for above supervision service in his proposal.

8.2 Training

The Vendor shall provide a comprehensive training program free of charge for the Purchaser‟s

personnel to be familiarized with designing, operation & maintenance, etc. of the equipment supplied by the vendor.

The training shall be conducted both at the Vendor‟s factory and Purchaser‟s site as follows:

(A) At the Vendor‟s factory

(B) At the Purchaser‟s site

The training shall be conducted for trainees of Purchaser for a

period of two (2) calendar weeks, and the round-trip air fairs and

living allowances to be incurred by the trainees during the training

period shall be borne by Purchaser.

The training shall be performed during the site acceptance testing

of the pumps, and conducted during the Vendor‟s supervision

service as specified in 8.1.

The Vendor shall submit to the Purchaser the detailed content and schedule of training programs for

the Purchaser‟s approval at least sixty (60) days prior to the beginning of the training.

8.3 First overhaul inspection

After initial continuous operation, Purchaser‟s operating team will perform 1st overhaul of equipment

for inspection of major parts. The Vendor shall dispatch supervisor(s) for overhaul in accordance

with the overhaul schedule upon Purchaser‟s written request without any delay.

9. GUARANTEE

9.1 Guarantee item list

The equipment and its supporting systems shall be guaranteed to operate continuously and

satisfactorily at all the specified operating conditions (full and part-load) as shown on the data sheets.

Vendor shall guarantee following performance data at rated condition specified in Data Sheet in Attachment #1:

1) Capacity at rated condition

2) Differential pressure

3) Shut-off head

4) Pump BkW at rated condition

5) Efficiency (pump & motor)

6) NPSH re

7) Min. pump start-up level

8) Vibration (displacement and velocity)

9) Noise

10) Min. 25000 hours total running times under actual operation conditions without any

maintenance after start-up

If the equipment does not meet the guarantee performance values including allowances specified in

this specification or applicable codes, Vendor shall repair the equipment until their performance conditions are fulfilled.

9.2 Guaranteed lifetime of major parts based on operation hours

Followings are minimum required lifetime of equipment major parts based on actual operation hours.

Should any defect or fault develop in these major parts during the guaranteed lifetime after initial commercial operation following operation and maintenance manual provided by Vendor, the Vendor

agrees to make all necessary replacement of the parts, free of charge. For replaced parts during the lifetime the guaranteed lifetime counts from the moments of service of the new parts.

Parts Minimum Lifetime

Motor 20 years

Bearing 25000 hrs

Bushing 25000 hrs

Casing 20 years

Wear ring 25000 hrs

If any defects or faults are detected during recommended maintenance period within the guaranteed

lifetime after normal operation according to Vendor‟s operation and maintenance manual, Purchaser shall give the Vendor notice of any defect of nonconformity within three (3) weeks after such defect

or nonconformity has been found.

Vendor shall start necessary action in order to rectify defect within three (3) weeks of Purchaser‟s

notice and shall complete action within a mutually agreed period of time.

In case of defect by an accident, Purchaser, Vendor and/or 3rd party inspectors shall investigate the cause and verify responsible parties.

If there is any disagreement each other, the final decision shall be up to Korean commercial arbitration board.

If the Korean commercial arbitration board concludes Vendor‟s responsibility, the Vendor shall rectify or replace the faulty components free of charge to Purchaser up to the completion of the rectifying

or replacement work including all transportation cost.

The guarantee will be subject to the following additional conditions and will be valid only for the above project:

The equipment shall operate under normal operating conditions as per those specified in the equipment data sheets including part load conditions.

The equipment is to be maintained on a regular basis in accordance with Vendor‟s recommended maintenance intervals.

During warranty time the replacement parts will be supplied and delivered to Purchaser free of

charge.

10. SPARE PARTS AND SPECIAL TOOLS

10.1 Spare parts

After the initial delivery to Purchaser of spare parts, Vendor shall agree to continue to quote and sell

the spare parts to Purchaser at the same price which it is then offering to other commercial customers for similar quantities under similar conditions. In the event Purchaser discovers that

Vendor has failed to meet its obligations to Purchaser under this article, Purchaser will be entitled, within one (1) year after the date of sale of any spare parts, to demand and receive a refund in the

amount of any excess price Purchaser has paid to Vendor.

Vendor shall provide sufficient spare parts for erection and start-up considering unexpected accidents during such period to prevent reordering shortages and to maintain delivery schedule and

to avoid delaying target completion date. If any parts including consumable items supplied by Vendor for the erection and start-up purpose are required additionally due to Vendor‟s fault prior to

completion of the Project, they shall be supplied and/or replaced at Vendor‟s cost. And no delay of

the Project due to the above shall relieve Vendor‟s responsibility under Contract.

10.2 Special tools

If any, Vendor shall offer special tools with itemized price for each components of the equipment and

all auxiliaries. Special tools are those not commercially available. Special tools shall be purchased with the main equipment.

Vendor shall quote by furnishing detail list for special tools, tackles, devices required for lifting, installation, removal and/or maintenance of equipment.

11. VENDOR DATA REQUIREMENTS

11.1 General

1) All documentation and drawings including information, calculations, schedules, etc. shall be submitted within the specified due date, as indicated in Section 11.2. Vendor shall be

responsible for submitting all documentation in accordance with a program to be prepared by

the Vendor's own allowing all participants sufficient time to check, access, comment, and eventually approve the documents.

2) The quality of the submitted documents must be in accordance with acceptable international practice and allow a speedy checking procedure. Documents not fulfilling these requirements

will be returned to Vendor without comments for Vendor's improvement and resubmission. It

is solely at the discretion of Purchaser to decide whether or not documents are acceptable.

3) All Vendor documentation shall employ Korean or English language, and all units shall be as

per Section 1.3.2.

4) Vendor's subcontractor list shall be approved by Purchaser prior to order to subcontractor.

5) Technical documentation of Vendor's subcontractor shall be reviewed and crosschecked and approved by Vendor prior to submission to Purchaser for approval.

6) Vendor's drawings (for layout, outline, assembly or subassembly, arrangement) shall include

basically the followings:

- Coordinates and north direction arrow mark

- Descriptions of elevation base

- Parts list

- Revision mark and revised description

- Project title block with full descriptions

7) Vendor's drawings shall be prepared on ISO standard sized sheets of A1, A2, A3 and A4.

8) Vendor's P & I Diagrams shall use symbol and legends prepared by Purchaser.

9) The numbering system for equipment, piping, instrumentation, correspondences, drawings and documentation for this project will be informed to the Vendor after contract and shall be

followed by the vendor.

10) Purchaser‟s drawing title block (see Attachment #4) shall be used at all Vendor's documents.

11) When submitting revised vendor documents, Vendor shall clearly indicate all revised points

with cloud mark and/or revision marks. This is mandatory requirement. Vendor shall be responsible for all possible results caused by omitting revision mark. Any document omitting

the revision marks may be returned without comment.

12) Purchaser‟s acceptance, with or without comments, of Vendor‟s documents does not relieve

Vendor from complying with all terms, conditions, codes, standards, requirements of the order and this specifications. Purchaser reserves the right to review and comment on documents

that have previously accepted with or without comments, and Vendor shall incorporate those

comments without any cost and delivery impact.

13) Purchaser‟s comments on submitted documents are not to be considered as authorization to

change the scope of purchase order, unless commented as scope change. Changes of scopes shall only be effected via letter or faxes.

14) Formal clarification, exception and deviation (“deviation” hereinafter) list shall be submitted in

Vendor‟s proposal. If deviation is specified on some part of proposal, not in formal deviation

list, then the deviation shall be not be accepted at all. All requirements in this specification shall be deemed accepted by Vendor if not specified in deviation list.

Any deviation shown on Vendor document after contract award shall not be accepted by Purchaser even though Purchaser overlooks it.

11.2 List of Vendor document and schedule

Document

When bid

For Approval Final

Remark No. of copies

No. of copies

Due date

No. of copies

Due date

GENERAL DOCUMENTS

1) Vendor prints index / schedule 1OR+5C *1 4w *2 +3w Note 6

2) Engineering, fabrication, test & delivery

schedule by item

1OR+5C *1 4w *2 +3w

3) Monthly progress report monthly

4) Clarification, exception and deviation list

against this specification

1OR+5C

5) Clarification, exception and deviation list

against API 610

1OR+5C

6) Sub-vendor list 1OR+5C *1 14w *2 +3w

7) Installation list of similar machines with

required data showing conformance with Sec.

1.4.5.

1OR+5C

8) Narrative description of the system 1OR+5C *1 10w *2 +3w

9) List of guaranteed items and values 1OR+5C *1 10w *2 +3w Sec. 9.1

10) Spare parts list for installation &

commissioning

1OR+5C *1 14w *2 +3w Note 3

11) Recommended spare parts list for 2-years

operation with itemized price list

1OR+5C *1 14w *2 +3w Note 3

12) Special tool list 1OR+5C *1 14w *2 +3w Note 3

13) Technical Bid Evaluation Sheet (to be filled-up

by Bidder)

1OR+5C Sec. 12.1

14) Rust preventive schedule *1 14w *2 +3w Note 3

15) Training program and schedule *1 24w *2 +3w Sec. 8.2

16) Installation, operation and maintenance

manual

*2 -4w

17) Packing specification *2 - 4w

18) Shipping schedule & packing list *2 - 4w

19) Catalogue 1OR+5C

20) Technical data requested by Purchaser upon

request

MECHANICAL DOCUMENTS

21) P & ID (showing all instrumentations) 1OR+5C *1 10w *2 +3w

22) Specification & data sheet 1OR+5C *1 10w *2 +3w

23) Equipment noise data sheet *1 10w *2 +3w Note 3

24) Equipment performance curve including:

- Curves at lean, typical and rich LNG case

- Pump & motor torque curve at 100% &

80% terminal voltage

- Initial starting condition of discharge valve

open & full re-circulation

1OR+5C *1 10w *2 +3w

25) Dimensional outline drawing with nozzle list 1OR+5C *1 10w *2 +3w

26) Description of auxiliary piping arrangement 1OR+5C *1 10w *2 +3w

Document

When bid

For Approval Final


No. of copies

Due date

No. of copies

Due date

27) Assembly & erection drawing with clearance *1 10w *2 +3w

28) Cross-section drawing with material list *1 10w *2 +3w

29) Calculation sheet *1 10w *2 +3w

ELECTRICAL DOCUMENTS

30) Motor data sheets 1OR+5C *1 10w *2 +3w

31) Motor outline drawing *1 10w *2 +3w

32) Motor characteristic curve at ambient temp. &

cryogenic temp.

1OR+5C *1 10w *2 +3w

33) Terminal box drawing *1 10w *2 +3w

34) Cable list *1 10w *2 +3w

35) Electric load list 1OR+5C *1 10w *2 +3w Note 3

INSTRUMENTATION DOCUMENTS

36) Instrument list 1OR+5C *1 10w *2

*4

+3w

+++2w

37) Instrument data sheet *1 10w *2

*4

+3w

+++2w

38) Instrument set point list *1 12w *2

*4

+3w

+++2w

39) Instrument layout drawing *1 12w *2

*4

+3w

+++2w

40) Cable specification & schedule *1 12w *2

*4

+3w

+++2w

41) Junction box drawing with terminal

arrangement

*1 12w *2

*4

+3w

+++2w

42) Vibration sensor data & specification 1OR+5C *1 12w *2

*4

+3w

+++2w

43) Instrument catalogues *1 12w *2 +3w

Q.A DOCUMENTS

44) Quality assurance manual 1OR+5C *1 14w *2 +3w

45) Inspection and test plan including 3rd party

inspection

1OR+5C *1 14w *2 +3w

46) Inspection and test procedure *1 14w *2 +3w

47) Shop inspection & test report, certificates *2 - 4w

48) KOSHA, KTL or KGS certificate for explosion-

proof type electric equipment and instruments

*2 Sec. 5.1.7

49) KGS certificates for safety valve, shut-off (on-

off) ball and globe valves for LNG & fuel gas

system

*2 Sec. 5.1.8

50) Site acceptance test plan & procedure *1 24w *2 +3w

51) Site test report *2 after test

MECHANICAL DATA BOOK PACKAGE

52) Mechanical data book package *3 -2w *4 ++2w Sec.11.4

Legend : *1 : 2C + PDF files *2 : 2C + PDF files *3 : 3C + 2 USB *4 : 11C + 5 USB

OR : Original C : Hard Copy(by air mail) PDF:PDF file(by e-mail) USB : USB memory stick

+: after receiving comment -: before shipment ++: after shipment +++: after commissioning (Note 7)

Document

When bid

For Approval Final


No. of copies

Due date

No. of copies

Due date

1) Quotation must include cost of above data.

2) Revised drawing and documents shall be submitted within 3 weeks after Purchaser‟s comment issue unless

otherwise specified in this section.

3) Purchaser‟s standard forms in Attachment #4 shall be used.

4) Documents required for proposal as specified in “When bid” column shall be included in the proposal. Omission of

any document may cause rejection of the proposal at the discretion of Purchaser.

5) Any document submission schedule that Vendor cannot follow shall be clearly suggested in Bidder‟s deviation list

in proposal. Vendor shall have the obligation to keep the submission schedule specified in this section unless

otherwise agreed.

6) Vendor document list containing all anticipated drawings and data shall be submitted prior to first issue of Vendor

documents as soon as possible. This list shall be updated and submitted to Purchaser with each issue of Vendor

documents. The format for the list can be found in Attachment #4.

7) Specified instrumentation documents shall be updated by Vendor incorporating all field changes, if any, that may

happen during installation and commissioning.

11.3 Vendor document distribution flow schematic

11.3.1 Overall document processing procedure

Vendor document processing procedure shall be as follows:

1ST

ISSUE

REVISE AND

RE-ISSUE FOR

APPROVAL

ISSUE FINAL

(CERTIFIED)

YES YES

NO NO

NO

WORK MAY PROCEED.

WORK MAY NOT PROCEED.

APPROVED ?

(NO COMMENT) APPROVED WITH

COMMENT ?

NOT

APPROVED ?

APPROVED ?

ISSUE MECHANICAL

DATA BOOK

(FOR REVIEW)

YES

NO

REVISE AND

RE-ISSUE FINAL

ISSUE MECHANICAL

DATA BOOK

(FOR FINAL)

SHOP INSPECTION

AND TEST

11.3.2 Document submission procedures

Basically, Vendor shall submit their technical documents to Purchaser and Engineer (in the

address stated in Section 1.2) at the same time in accordance with following schematics:

When submitting to Purchaser, Vendor shall submit to purchaser all Vendor documents via web

based “KOGAS Project Management Information System.”

For Approval/Review documents Final documents

VENDOR

ENGINEER

PURCHASER Comment

1+PDF file

1 copy + PDF file

Comment

VENDOR

ENGINEER

PURCHASER Comment

1+PDF file

1 copy+ PDF file

Comment, if any

This applies to 1st submitted documents or revised document by Purchaser‟s comments.

This applies to documents approved without comment by Purchaser.

Mechanical data book package (for review) Mechanical data book package (for final)

VENDOR

ENGINEER

PURCHASER Comment

2 copies

1 copy + 2 USB

if any

VENDOR

ENGINEER

PURCHASER

(Head office)

Comment, if any

2 copies + 2 USB

1 copy + 1 USB

if any

PURCHASER

(Samcheok office)

8 copies + 2 USB

if any

Vendor can enter this process only when all the

documents are approved without comment by

Purchaser.

See section 11.4 for preparation of mechanical

data book package.

This step is applied when Mechanical Data Book

Package for Review is approved by Purchaser.

See section 11.4 for preparation of mechanical

data book package.

11.4 Mechanical data book

11.4.1 Mechanical data book package with all vendor's documents/drawings and inspection/test report shall be submitted after Purchaser‟s final approval.

11.4.2 The hard copies shall be binded in hard cover file book of good quality. Each book shall be provided with detail index, dividers, etc. All drawings bigger than A4 size shall be folded and

inserted into translucent plastic drawing holder, and compiled in the binders.

11.4.3 The cover of mechanical data book shall be in accordance with the format in Attachment #4.

11.4.4 Soft copies of electronic files contained in USB shall be submitted together with hard copies.

The contents and their order shall be strictly same with the hard copies. All documents generated by office software, such as MS Office, Auto Cad, Korean Hangul, shall be submitted

in both original source files and converted Acrobat PDF format. All other documents generated by hand-writing, photo and proprietary analysis software, etc. shall be submitted in either

Acrobat PDF or TIFF white-black compressed image format with minimum 300 DPI resolution.

12. TECHNICAL BID REQUIREMENT

In addition to technical bid documents required in Section 11.2, Bidder or Vendor shall fulfill the bid requirements in this section.

12.1 Technical bid summary

This form shall be completed by Bidder or Vendor and submitted with the proposal.

No Item Unit Required Proposed

I General

Bidder‟s Bidding Document No.

Manufacturer

Korean Agency

Type Submerged, in-tank,

retractable

Model

Delivery condition

Delivery period

Eligibility (See Section 1.4.5)

- has been supplied and/or

manufactured for LNG service with

equal to or more than 220m3/hr and

200m

II Bidding documents

II-1 General documents

Vendor prints index / schedule To be submitted with the bid

Engineering fabrication, test & delivery

schedule by item

“

Deviation list against this specification “

Deviation list against API 610 “

Sub-vendor list “

Installation list of similar machines “

Narrative description of the system “

List of guaranteed items and values “

Spare parts list for installation and

Commissioning

“

Recommended spare parts list for 2-years

operation with Itemized price

“

Special tool list “

Technical bid evaluation sheet (See sec.

12.1)

“

Catalogue “

II-2 Mechanical documents

P & ID showing all instrumentations To be submitted with the bid

Specification & data sheet “

Equipment performance curve “

- Curves at lean, typical, rich LNG case “

- Pump & motor torque curve at 100%

& 80% terminal voltage

“

- Initial starting condition of discharge

valve open & full re-circulation

“

Dimensional outline drawing with nozzle list “


Description of auxiliary piping arrangement “

II-3 Electrical documents

Motor data sheet To be submitted with the bid

Motor characteristic curve “

Electric load list “

II-4 Instrumentation documents

Instrument list To be submitted with the bid

Vibration sensor data & specification “

II-5 Q.A documents

Quality assurance manual To be submitted with the bid

Inspection and test plan including 3rd party

inspection

“

II-6 Number of Vendor documents

For approval 2 copies + PDF files

Final 2 copies + PDF files

Mechanical data book package – for review 3 copies+ 2 USB

Mechanical data book package – final 11 copies + 5 USB

Instrumentation document – as built 11 copies + 5 USB

III Code and standards

LNG Pumps API 610, 11th Ed.

Unfired pressure vessels and welding ASME Sec. VIII, Div.1

ASME Sec. II

ASME Sec. VIII

ASME Sec. IX

AWS standards

Piping (cryogenic and non-cryogenic) ASME B1.20.1, B16.5,

B16.9, B16.11, B16.28,

B16.47, B31.3, B36.10

Electrical IEC-60034, 60079

CENELEC

NEC

NEMA MG-1

ANSI

Korean Industrial Standard

(KS)

JIS

API

IEEE

KOSHA, KTL or KGS (for

enclosure of hazardous

service)

Instruments ASME B1.20.1, B16.5, B46.1

API 550, 670, 678

ISA S5.1, S5.2

IEC 60079, 60529, 60654

ISO 8310

KGS (for safety valves, ball

& globe valves for LNG,NG,

N2 fuel gas system)


KOSHA, KTL or KGS (for

enclosure of hazardous

service)

JIS

Safety NFPA 59A

Material ASTM/ASME, KS, JIS

Painting & Insulation (if applicable) Purchaser‟s spec

IV Scope of supply & work

IV-1. Scope of supply

[ Common for LP LNG pumps & LNG Drain

pumps ]

1) Each pump complete with integral

electrical motor

by Vendor

2) Head plate with connecting

bolts/ nuts/gaskets

by Vendor

3) Foot valve with connecting

bolts/nuts/gaskets

by Vendor

4) Electric power & instrument cables

including earthing cables with the

length proper for pump to junction

box on the top of tank (But, the

instrument cable for LNG Drain Drum

Pump to be excluded.)

by Vendor

5) Junction boxes for electric and

instrument cables with N2 purge

connection (But, the junction box for

instrument of LNG Drain Drum Pump

to be excluded.)

by Vendor

6) Complete removable system

including

by Vendor

- Lifting cables with reels, the reels

shall be fixed on head plate

“

- Support cable with all accessories

clamps, turnbuckles rings

“

- Guide and roller-guide “

- Grounding straps “

- Cryogenic electrical supply with

the connections on the motor

“

7) Anti-spin fixture to prevent cables

from twisting

by Vendor

8) Basket protection screen on top of

pumps to catch falling debris and

tools

by Vendor

9) Nitrogen purge system for double

penetration seals with valves,

regulators, pressure indicators,

pressure transmitters, piping and

other as indicated in attached P &ID

(The instrument and valves shall be

pre-assembled and mounted on skid

with setting bolts/nuts)

by Vendor

10) All supports and foundation bolting,

shims and accessories necessary for

the setting, adjustment and

by Vendor


anchorage of the equipment

supplied

11) Lifting eyes, screw jacks, and special

tools for installation, operation and

maintenance (in new and first-class

condition)

by Vendor

12) Spare parts for installation and

commissioning

by Vendor

13) Nameplates by Vendor

14) All documents required by this

specification (Vendor shall submit all

Vendor documents by web based

KOGAS Project Management

Information System. Refer to

Attachment #3. “Usage of Vendor

Prints Information System”)

by Vendor

15) All necessary components,

accessories and appurtenances, as

normally provided, whether

mentioned in this specification or not

by Vendor

[ Scope of LP LNG Pumps only ]

16) Instrumentation for each pump with by Vendor

- Dual vibration sensors: all

sensors shall be able to be

interface with SHINKAWA RV-200

VM-7B system. (Vendor shall

recommend the specification of

vibration signal cable)

“

- Interface module installed in

proper housing (junction box)

“

17) Dummy Pump (1 set) by Vendor

IV-2. Scope of work

1) Data for column vibration analysis

and the static & dynamic loading

data with various directions

by Vendor

2) KOSHA (Korean Occupational Safety

& Health Agency), KTL (Korea Testing

Laboratory) or KGS (Korean Gas

Safety Corporation) certificates for

explosion proof type electric

equipment and instruments (see

Section 5.1.8)

by Vendor

3) KGS certificates for safety, shut-off

(on-off) ball and globe valves for gas

system (see Section 5.1.8)

by Vendor

4) Painting up to finish coating at shop

and touch-up painting at site

5) Coordination meeting by Vendor

6) Supervision for installation,

commissioning and site acceptance

test

by Vendor

7) Training for Purchaser‟s trainees by Vendor

8) Packing for export and site storage by Vendor


for 6 months

9) Inspection and test required by this

specification

by Vendor

10) Performance guarantee by Vendor

11) Review of purchaser‟s column

drawings

by Vendor

IV-3. Spare parts list for installation and

commissioning

To be specified by Bidder

IV-4. Recommended spare parts list for 2-years

operation

To be specified by Bidder

IV-5. Special tools list To be specified by Bidder

V. Technical specification for LP LNG

Pumps

V-1. General

1) Model

2) Type Submergible

3) Q‟ty sets Twenty-one (21)

4) Stage stage

V-2. Operation conditions

1) Capacity, rated m3/h 330

2) Suction pressure

- Max. MPa.a 0.240 / 0.246 / 0.252

- Rated MPa.a 0.122

3) Discharge pressure MPa.a 1.271 / 1.316 / 1.388

4) Differential pressure MPa 1.149 / 1.194 / 1.266

5) Differential head m 270

6) Head (rated) per stage m

7) NPSH av @ tank bottom m 1.6

8) Hydraulic kW, Lean/Typ./Rich kW

V-3. Liquid

1) Liquid LNG

2) Pumping temp., min./nor./max. oC -163 / -159 / -157

3) S.G, Lean / Typ. / Rich 0.434 / 0.451 / 0.478

4) Viscosity @ -159 °C cP 0.131 / 0.146 / 0.173

5) Vap. pressure, min./max MPa.a 0.127 / 0.142

V-4. Performance

1) Capacity, Rated m3/h 330

B.E.P m3/h

Rated / B.E.P % 80 ~ 110 per API

2) Min. continuous flow, thermal/stable m3/h (%

or rated

flow)

3) Preferred operating region m3/h (%

of B.E.P)

(70% ~ 120% per API)

4) Allowable operating region m3/h (%

of B.E.P)

5) Speed / slip rpm / % /


6) Impeller dia., min. / rated / max. mm

7) Head increase by max. impeller dia. % > 5

8) Motor rating kW

9) Rated power kW

kW

@ nor SG

@ max. SG

10) Motor rating / Rated power @ max.

SG

% > 110 per API

11) Efficiency @ rated condition %

12) Max. head rated impeller m

13) Max. head / Rated head % > 110

14) Max. power rated impeller kW @ nor SG

@ max. SG

15) Motor rating / Max. power % > 100

16) NPSH required at rated capacity m @ inducer CL

m Distance between centre of

inducer and bottom of tank

m Margin = NPSHav - NPSHre

17) Suction specific speed rpm, m,

m3/min

(N x Q^0.5) / NPSHR^0.75

18) Max. sound pressure level @ 1m dB(A) Max. 85

19) Vibration within preferred operating

region

- Overall mm/sec < 5.0 RMS

- Discrete frequencies mm/sec < 3.35 RMS

20) Min. pump down level at rated flow

(from tank bottom)

m

21) Min. start-up level (from tank

bottom)

m < 1.6

22) Min. pump down level at minimum

continuous flow (from tank bottom)

m

23) Max. discharge pressure as per

definition of Section 13.1.3.

MPa.g < 1.86

Max. suction pressure +

shutoff head x (1.0 + 0.08

+ 0.05) x 478 x 9.806 /

1000000

V-5. Mechanical design condition

1) Case pressure rating

- Max. allowable working press. MPa.g

- Temperature oC

2) Hydro-test pressure Mpa.g MAWP x 1.5 times

V-6. Construction

1) Connection

- Head plate 24” 300# RF SF

- Foot valve 24” 300# FF SF

2) Pump assembly

- Mounting Vertical in-tank

- Overall length of pump assembly

only

mm

- Column inside diameter mm 584.2 (24” Sch. XS)

- Column height m About 52.6

- Lifting cables m

3) Casing


- Type Diffuser

- Split Radial

4) Impeller

- Type

- Mounting

- Individually secured Yes

5) Inducer type

6) Shaft (pump & motor) Solid or Hollow

7) Rotation (viewed from suction end)

8) Thrust balancing mechanism

9) Bearing

- Motor upper bearing model

- Motor upper bearing material

- Motor lower bearing model

- Motor lower bearing material

- Bottom (at inlet) bearing model

- Bottom (at inlet) bearing material

10) Lubrication by pumped liquid (LNG)

11) Suction region designed for MAWP Yes

12) Number of shaft piece

13) Junction box size, L x W x H m

V-7. Material

1) Case

2) Impeller

3) Inducer

4) Wear ring for case

5) Wear ring for impeller

6) Shaft (pump & motor)

7) Sleeve

8) Diffusers

9) Head plate

10) Foot valve

11) Lifting cable & Support cables

V-8. Instruments

1) Area classification Zone 1, IIB T4

2) Vibration sensors

- Q‟ty per pump ea Two (2)

- Manufacturer / model PCB or eq. /

- Location

3) Vibration interface modules by Vendor, if required

(To be interfaced with

SINKAWA infisys RV-200

VM-7B system)

- Manufacturer / model /

- Location In junction box

4) Pressure transmitters with digital out

for N2 purge system

- Type SMART type transmitter with

integral digital indicators

- Manufacturer Emerson process,

YOGOKAWA or eq.

- Display scale SI units only


5) Pressure gauges for N2 purge system

- Type Heavy duty, liquid filled,

bourdon tube

- Manufacturer


V-9. Motor

1) Code IEC-60034

2) Manufacturer

3) Model & Frame No.

4) Rating @ operating temp. kW

5) Speed rpm

6) Mounting Vertical

7) Volts/Phase/Hz 6.6kV / 3 / 60

8) Type Submerged

9) Enclosure IP 56 (J/B only)

10) Cooling

11) Service factor

12) Minimum starting volts 80% of rated voltage

13) Starting method

14) Insulation

15) Temp rise oC

16) Efficiency @ operating temp.

- at 1/2 load %

- at 3/4 load %

- at full load %

17) Power factor

- at 1/2 load

- at 3/4 load

- at full load

18) Full load amps Amps

19) Locked rotor amps Amps, %

20) Bearing type, DE/NDE

21) Bearing lubrication, DE/NDE

22) Rotor GD2 kg-m2

V-10. Weight

1) Pump & motor kg

2) Power cable & retraction system kg

3) Foot valve assembly kg

4) Head plate assembly kg

5) Total weight kg

V-11. Others

1) Rotor individually balanced Required

2) Completed rotor balanced Required

3) Demonstration of max. vibration at

min. flow

Required

4) Lateral analysis Required

5) Cavitation study Required

VI. Technical specification for LNG Drain

Drum Pumps

VI-1. General


1) Model

2) Type Submergible

3) Q’ty set Two (2)

4) Stage

V-2. Operation conditions

1) Capacity, rated m3/h 40

2) Suction pressure

- Rated MPa.a 0.130

3) Discharge pressure MPa.a 1.50

4) Differential pressure MPa 1.37

5) Differential head m 310

6) Head (rated) per stage m

7) NPSH av @ drain drum bottom m 0.5

8) Hydraulic kW, Lean/Typ./Rich kW

V-3. Liquid

1) Liquid LNG

2) Pumping temp., nor./max. oC -159 / -158

3) S.G, Lean / Typical / Rich 0.434 / 0.451 / 0.478

4) Viscosity @ -159 °C cP 0.133

5) Vapor pressure, min./max. MPa.a 0.106 / 0.13

V-4. Performance

1) Capacity, Rated m3/h 40

B.E.P m3/h

Rated / B.E.P % 80 ~ 110 per API

2) Min. continuous flow, thermal/stable m3/h (%

or rated

flow)

3) Preferred operating region m3/h (%

of B.E.P)

(70% ~ 120% per API)

4) Allowable operating region m3/h (%

of B.E.P)

5) Speed / slip rpm / % /

6) Impeller dia., min. / rated / max. mm

7) Head increase by max. impeller dia. % > 5

8) Motor rating kW

9) Rated power kW

kW

@ nor SG

@ max. SG

10) Motor rating / Rated power @ max.

SG

% > 110 per API

11) Efficiency @ rated condition %

12) Max. head rated impeller m

13) Max. head / Rated head % > 110

14) Max. power rated impeller kW @ nor SG

@ max. SG

15) Motor rating / Max. power % > 100

16) NPSH required at rated capacity m @ inducer CL

- Distance between centre of

inducer and bottom of drum

m

m Margin = NPSHav - NPSHre

17) Suction specific speed rpm, m,

m3/min

(N x Q^0.5) / NPSHR^0.75


18) Max. sound pressure level @ 1m dB(A) Max. 85

19) Vibration within preferred operating

region



20) Min. pump down level at rated flow

(from drum bottom)

m

21) Min. start-up level (from drum

bottom)

m

22) Min. pump down level at minimum

continuous flow (from drum bottom)

m

23) Max. discharge pressure as per

definition of Section 13.1.3.

MPa.g < 1.77

Max. suction pressure +

shutoff head x (1.0 + 0.05

+ 0.05) x 478 x 9.806 /

1000000

V-5. Mechanical design condition

1) Case pressure rating

- Max. allowable working press. MPa.g

- Temperature oC

2) Hydro-test pressure Mpa.g MAWP x 1.5times

V-6. Construction

1) Connection

- Head plate 16” 300# RF SF

- Foot valve 16” 300# FF SF

2) Pump assembly

- Mounting Vertical in-drum

- Overall length of pump assembly

only

mm

- Column inside diameter mm 386.4

- Column height m About 4.6

- Lifting cables m

3) Casing

- Type Diffuser

- Split Radial

4) Impeller

- Type

- Mounting

- Individually secured Yes

5) Inducer type

6) Shaft (pump & motor) Solid or Hollow

7) Rotation (viewed from suction end)

8) Thrust balancing mechanism

9) Rotor dynamic balanced

- Individual balanced Yes

- Complete rotor balanced Yes

10) Bearing

- Motor upper bearing model

- Motor upper bearing material

- Motor lower bearing model

- Motor lower bearing material

- Bottom (at inlet) bearing model


- Bottom (at inlet) bearing material

11) Lubrication by pumped liquid (LNG)

12) Suction region designed for MAWP Yes

13) Number of shaft piece

14) Junction box size, L x W x H m

V-7. Material

1) Case

2) Impeller

3) Inducer

4) Wear ring for case

5) Wear ring for impeller

6) Shaft (pump & motor)

7) Sleeve

8) Diffusers

9) Head plate

10) Foot valve

11) Lifting cable & Support cables

V-8. Instruments

1) Area classification Zone 1, IIB T4

2) Pressure transmitters with digital out

for N2 purge system

- Type SMART type transmitter with

integral digital indicators

- Manufacturer Emerson process,

YOGOKAWA or eq.


3) Pressure gauges

- Type Heavy duty, liquid filled,

bourdon tube

- Manufacturer


V-9. Motor

1) Code IEC-60034

2) Manufacturer

3) Model & Frame No.

4) Rating @ operating temp. kW

5) Speed rpm

6) Mounting Vertical

7) Volts/Phase/Hz AC440V / 3 / 60

8) Type Submerged

9) Enclosure IP 56 (J/B only)

10) Cooling

11) Service factor

12) Minimum starting volts 80% of rated voltage

13) Starting method

14) Insulation

15) Temp rise oC

16) Efficiency @ operating temp.

- at 1/2 load %

- at 3/4 load %

- at full load %


17) Power factor

- at 1/2 load

- at 3/4 load

- at full load

18) Full load amps Amps

19) Locked rotor amps Amps, %

20) Bearing type, DE/NDE

21) Bearing lubrication, DE/NDE

22) Rotor GD2 kg-m2

V-10. Weight

1) Pump & motor kg

2) Power cable & retraction system kg

3) Foot valve assembly kg

4) Head plate assembly kg

5) Total weight kg

V-11. Others

1) Rotor individually balanced Required

2) Completed rotor balanced Required

3) Demonstration of max. vibration at

min. flow

Required

4) Lateral analysis Required

5) Cavitation study Required

VII. Guarantee

VII-1. Guarantee item list

[ For LP LNG Pumps ]

1) Capacity at rated condition m3/hr 330

2) Differential head m 270 -3%, +3%

3) Shutoff head m -3%, +8%

4) Pump BkW at rated condition kW +4%

5) Efficiency

- Pump %

- Motor %

6) NPSH re m +0%

7) Noise dB(A) less than 85

8) Vibration



9) Min. pump start-up level m 1.6 from tank bottom

10) Running hours without maintenance 25,000 under actual

operating condition

[ For Drain Pumps ]

1) Capacity at rated condition m3/hr 40

2) Differential head m 310 -3%, +3%

3) Shutoff head m -3%, +5%

4) Pump BkW at rated condition kW +4%

5) Efficiency

- Pump %

- Motor %

6) NPSH re m +0%

7) Noise dB(A) less than 85


8) Vibration



9) Min. pump start-up level m From drum bottom

10) Running hours without maintenance 25,000 under actual

operating condition

VI-2. Guarantee life time

1) Motor Year 20

2) Bearing Hr 25,000

3) Bushing Hr 25,000

4) Casing Year 20

5) Wear ring Hr 25,000

VII. Inspection and tests

VII-1. Shop test

1) Welding check

- Visual inspection Yes

- Test piece Tensile, guide bend,

impact @-196°C

2) Material inspection Certificate required

3) Nondestructive inspection

- RT Butt weld parts (100%)

Pump casing

- Acceptability code for RT ASME Sec. VIII, ASTM E155

- PT Welds of non-RT

Pump impellers

- Acceptability code for dye test ASME Sec.VIII,

ASTM E165

- UT Pump shaft

4) Visual and dimensional check Yes

5) Pressure test 1.5 x MAWP

6) Assembly check Yes, for all pumps

7) Cold hand spin test Yes, for all pumps

8) Performance test Witnessed by the jointly

inspectors of Purchaser &

3rd party inspection agency

- Test fluid LNG or cryogenic liquid

- Flow, suction & discharge press. Yes, for all pumps

- Pressure pulsation Yes, for all pumps

- Liquid temperature of suction and

discharge, specific gravity

Yes, for all pumps

- Vibration Yes, for all pumps

- Noise Yes, for all pumps

- Current, voltage and frequency Yes, for all pumps

- Input power Yes, for all pumps

- NPSH re Yes, at 5 points for one

pump of each item, at rated

point for remainder

- Liquid level Yes, for all pumps

- Pump-down and start-up level Yes, for one pump of each

item

- Thrust balance mechanism Yes, for one pump of each

item


9) Pump dismantle inspection Yes, for all pumps

10) Motor test Yes, for all pumps

11) Electric & instrument test

- Double seal leak tight test Yes, for all pumps

- Cable test Yes

- Cable flexibility in LN2 Yes

12) Painting inspection Yes

13) Packing & marking inspection Yes

14) Other test

- Column foot valve test Yes, for all valves

- Shaft stabilization in LN2 Yes for all shafts

VI-2. Site test

1) Test procedure By Vendor

2) Site acceptance test By Purchaser under Vendor‟s

witness

3) Site acceptance test completion

certificate

By Purchaser

VI-3. 3rd party inspection

1) 3rd party inspection agency One of Lloyd‟s Register

Verification, TÜV Rheinland

Group, DNV, ABSG

Consulting INC, BV, HSB and

KR

2) Scope see Sec. 5.1.6

13. DESIGN SPECIFICATION

13.1 General

13.1.1 Submersible pumps for refrigerated, liquefied gas products shall be supplied in accordance

with the requirements of the American Petroleum Institute Standard 610 and special

requirements indicated in this specification.

13.1.2 The Vendor shall be responsible for ensuring that any technical conflicts between documents

comprising the purchase order shall have been resolved, and agreed by the Engineer in writing before proceeding with manufacture of the affected parts. The Vendor shall be expected to

attend a design review and co-ordination meeting with the Purchaser before proceeding with manufacture.

13.1.3 Maximum Discharge Pressure shall be the maximum possible suction pressure to be

encountered, plus the maximum differential pressure the pump is able to develop when operating at the specified condition of speed, specific gravity, and pumping temperature with

the furnished impeller.

13.1.4 “Unit Responsibility" includes expediting, and assurance that all applicable specifications

referenced on the data sheets or requisition are supplied to, and complied with, by any

sub-Vendor. It also includes guarantee of performance of the complete package furnished. Unless specified otherwise in the Purchase Order, the Prime Vendor's shall have unit

responsibility.

In the event of problems being experienced with the Complete Operating unit when installed,

it is the Prime Vendor's responsibility to identify the source of the problem and only if and when he can establish that the source is not within his control will he cease to be responsible

for the resolution of that problem.

13.1.5 “Submergence” is the vertical distance of the pump reference datum (which is defined as the entrance to the pump suction bell mouth) below the free liquid surface.

13.1.6 “Pump down” is the condition of minimum submergence, at which the pump loses prime.

Pump down is defined as the point at which the pump loses prime by a 40% or more loss in

discharge pressure.

13.1.7 “Guaranteed Minimum Flow” is the flow stated on the pump data sheet (min. cont. m3/hour) and is the minimum flow at which the pump may be run continuously, with the Vendor's

approval, and with his assurance that it will not cause accelerated deterioration of any components.

13.1.8 Installed impeller diameters as well as maximum and minimum impeller sizes compatible with the pump casing shall be shown on the data sheets.

13.1.9 Pumps shall exhibit stable performance characteristic, rising continuously to shut off, and shall

be suitable for both individual and parallel operation.

13.1.10 Pumps shall be designed for continuous low temperature operation, and the materials used

shall be suitable for all service conditions.

13.1.11 All pumps with identical duties shall have identical hydraulic characteristics and must be

capable of single and parallel operation.

13.1.12 The suction flow passages, and inducer shall be designed to ensure satisfactory suction

conditions, velocity distribution and freedom from cavitation - as determined by a 3%

reduction in head generated - and other adverse effects over the complete range of flow rates when specified NPSH (or greater) is available to the pump under all operating conditions.

13.1.13 Vendor shall advise calculated maximum heat input to LNG during all specified operating conditions.

13.1.14 Each pump design shall be checked during a performance test, for actual critical speeds

occurring below running speed. If not possible, critical speed calculation report to be submitted to verify the critical speed occurring below running speed.

13.1.15 Critical speeds shall be calculated on the basis of the pump being filled with the service fluid.

13.1.16 The magnitude of unbalanced axial thrust loads resulting from hydraulic forces at impellers and

inducers shall be determined, for all operating conditions within the pump operating range,

with pump internal clearances at design values and also at double design values. The pump thrust compensating mechanism (whether an hydraulic or rolling contact bearing or

combination of both) shall be capable of supporting all the above loads. Where the design uses a balance disc or balance piston, there shall be not thrust reversal over the full flow range.

13.1.17 Unproven, prototype or first-off equipment is not acceptable, only proven equipment may be used. Refer to paragraph 1.4.5 for acceptability criteria.

13.2 Casings

13.2.1 The pressure casing shall also include head plate assemblies, electrical seal assemblies, valves, and sections of the column within the Vendor's supply, in addition to the pump pressure

casings.

13.2.2 Inner casings within the pump motor unit itself, shall also be designed to withstand the

pressure conditions that may exist within the unit under backflow and/or backpressure

conditions generated by the circumstances.

13.3 Nozzle and pressure casing connection

13.3.1 With the exception of flanges requiring to be specially designed as an integral part of the pump and motor assembly, all connections larger than 1/2 inch nominal diameter shall be

made using pipe flanges of standard size and conforming to applicable specifications of the American National Standards Institute. Pipe sizes of 1 1/4, 2 1/2, 3 1/2, 5, 7 and 9 inch shall

not be furnished unless approved by the Purchaser.

13.3.2 Pumps shall be designed to be self venting i.e, no pocketed high points, to ensure that bearings are not „vapour locked‟ when the pump is stationary.

13.3.3 Gaskets shall be type 304 or 316 stainless steel spiral wound with graphite filler suitable for and having a proven record for cryogenic service.

Joints not open to atmosphere may be designed without gaskets.

13.4 Impellers & shaft

13.4.1 Impellers for multistage pumps shall be individually secured against axial movement in either

direction along the shaft.

13.4.2 Impellers shall have solid hubs.

13.4.3 The shaft of vertical submerged motor pump units shall preferably be of one piece.

13.4.4 Shafts shall be machined and properly finished throughout their length so that the overhung

portion of the shaft containing the impellers shall be maximum 0.001 inch (25 micrometers)

TIR, and other non-critical area shall be maximum 0.002 inch (50 micrometers).

13.4.5 One and two stage pumps shall be of stiff shaft construction. Pumps having more than two

stages may be of flexible shaft design.

13.5 Vibration & balancing

13.5.1 Instrumentation shall include vibration sensors. Vibration readings shall be taken with the

probe mounted on the pump casing and located as close as possible to bottom bearing. To eliminate low frequency “noise” from the test stand a low frequency (below 20 Hz) filter may

be used. Vibration limits are given in API paragraph 6.9.3.6 and 6.9.3.7.

13.5.2 The vendor shall demonstrate that the pump can operate at any capacity from rated flow to

quoted minimum continuous stable flow without exceeding the vibration limits given in API paragraph 6.9.3.6 and 6.9.3.7.

13.5.3 All major components such as impellers, rotors and balancing drums shall be individually

dynamically balanced. The assembled rotor shall be check, dynamically balanced. The component parts shall be designed or marked such that subsequent re-assembly does not

affect the degree of balance. The vendor‟s standard balancing procedure shall be used provided that the accuracy of the final balance is better than grade G2.5 as specified in ISO

1940.

13.5.4 The axial thrust compensating mechanism must also be designed to provide full force balance capability when the normal direction of rotation of the pump is reversed whether by

inadvertent incorrect connection of phases or by transient reverse flow of fluid in the pump column. The vendor‟s attention is drawn to the reverse flow to be anticipated as a result of the

maximum pressure conditions.

Particular attention shall be paid to the operation of the axial force balancing mechanism, and

also to the adequacy of lubrication and cooling of the bearings during this transient condition.

In case that the axial thrust compensating mechanism is not designed to provide thrust balance for reverse rotation or reverse flow, Vendor shall guarantee the reverse rotation due to

inadvertent incorrect phasing will not harm the pump for short periods of time and the pump should be protected by undercurrent relay.

Undercurrent relay settings to be advised by Vendor and verified at shop performance test.

The pump shall be able to endure transient reverse flow under normal condition such as when the pump is stopped and the column liquid level is dropping.

13.6 Drivers

13.6.1 The motor shall be designed for starting with full voltage available at the terminal box. The

torque provided by the motor with 80% of rated voltage available at the terminal box shall be capable of accelerating the machine to full speed when the worst condition existing at the

pump discharge (eg. open discharge valve; or any other condition or combination of conditions stated by the Vendor to be the most severe).

13.6.2 The motor shall be of the squirrel cage induction design capable of continuous operation at the

specified conditions when fed with the electricity supply noted on the motor data sheets for each unit.

13.6.3 The Vendor shall arrange for electrical and instrument penetrations of the column head plate to be made through two series connected electrical seal assemblies.

An enclosed chamber between the seals shall be supplied, designed for complete purging with

inert gas. Vendor shall provide suitable purge system piping connections.

This electrical seal system shall be fitted on the outside of the column, above the tank roof.

Stranded conductors shall not be used across the sealing interfaces.

These two seal assemblies, and the chamber between them, shall be capable of withstanding

either liquid or vapour at the pump casing design pressure and temperature and at ambient temperature.

13.6.4 In addition to the cables, seals and associated equipment, the Vendor shall supply two

terminal boxes, one for the main motor cable and the other for instruments certified by a recognised testing authority, as being suitable for use in the specified hazard area as defined

on the data sheets.

Nitrogen purge connections shall be provided and insulated studs shall be fitted, suitable for

accepting compression type cable lugs. The box, its terminals and gland entries shall be

suitably sized to accept the feeder cables.

13.6.5 Flanged connections to the terminal box shall not use bolting that penetrates through to the

inside of the box.

13.6.6 A heavy duty earth terminal shall be provided external to the main terminal box.

13.6.7 Vendor shall advise his recommendations for equipment protection, for example, over and under current protection characteristics, venting requirements, vibration monitoring etc. Also

congruence between supplied sensors and the vibration monitoring system shall be

demonstrated by the Vendor.

13.7 Bearing

13.7.1 The thrust and radial bearings shall be suitable for lubrication and cooling by the pumped fluid under all static and dynamic conditions, and shall be vendor‟s standard design for the

application.

13.7.2 Thrust and radial bearings shall be lubricated by the pumped fluid.

13.8 Piping connection

13.8.1 The Vendor shall supply all integral piping he considers necessary for the successful operation

of the equipment and shall furnish it fully assembled and installed if it pertains to equipment listed in the scope of supply.

13.8.2 Except where permitted under API paragraph 5.3.1, flanges of nominal diameter up to and including 24 inch shall conform to ASME/ANSI B16.5. Flanges of nominal diameter 26 inch and

above shall conform to ASME/ANSI B16.47.series A (MSS-SP-44), Pipe threads shall be taper

threads in accordance with ASME/ANSI B1.20.1

13.8.3 Threaded joints shall not be seal welded.

13.8.4 Plugs, where used, shall be of the same material as the component into which they are to be fitted, and shall be adequately secured.

13.9 Junction box size

The junction box size shall be large enough for connecting termination kit. So, space between each J/B terminal and the bottom J/B shall be not less than 550mm.

13.10 Miscellaneous requirements

13.10.1 The pump and associated equipment shall be designed to operate within the product storage

tank. The configuration of any specific item will be shown on the data sheets for that item. The Vendor shall co-ordinate with tank manufacturer on all technical aspects relating to pump

mounting and installation.

13.10.2 The Vendor shall supply a spring loaded, nitrogen purged foot valve to shut off the flow of fluid to the pump column when the pump is being removed for maintenance. The foot valve shall

include a double seal, and provision shall be made for nitrogen to be supplied to the space between the seals.

13.10.3 Vendor shall supply adequate stainless steel lifting equipment between the pump and the

outside of the head plate to enable the pump to be lifted and lowered by means of external lifting equipment supplied by others. By means of a gland in the top plate it shall be possible

to raise the pump sufficiently for the foot valve to close, without removing the top plate. A gasketed blanking plate shall be provided over the gland and lifting attachment to prevent

escape of gland leakage when the pump is in service.

13.10.4 A system requiring minimum interruption of the lifting or lowering is preferred. A secondary

cable system shall be included to enable lifting to be continued in the event of failure of the

main lifting system. This cable will not normally be in tension and may be stored with the electrical cables.

13.10.5 Earthing shall not be via the metal parts of the lifting system.

13.10.6 Instrument and electrical cables installed in the tank column between the head plate and the

pump shall be designed for disconnection in the head plate assembly, and for winding on to a

storage drum whilst the pump is being lifted. They must also be suitable for continuous operation when immersed in LNG and shall maintain their flexibility under LNG temperatures.

Furthermore the cables shall be abrasion resistant and waterproof. The electrical power cables feeding the motor shall be rated for the full load current of the motor and shall be suitable for

the specified operating voltage, frequency and method of system neutral earthing. Any voltage drop in the "in-tank" cables is the responsibility of the Vendor.

The main power cables shall be supported at regular intervals inside the column from the head

plate to the motor so as to prevent excessive cable movement under fault conditions and to

minimise cable damage due to abrasion against the walls of the column.

13.10.7 Service is considered to be continuous since one pump per tank will be in continuous operation,

recirculation tank contents. This operation mode will be transferred between pumps to ensure similar overall running times.

13.10.8 The pumps will be constructed to avoid entrainment of liquefied gas products when the pump

is withdrawn from the tank for maintenance.

13.10.9 The pump set and its support shall incorporate features designed to minimise the possibility of

misalignment during installation and removal of the pump in the column.

13.10.10 Vendor shall supply complete details, including static and dynamic loadings, for the connection

between the pump support and the tank.

13.10.11 The design of the lower column section shall, after welding or flanging to the upper section, permit hydrostatic testing of the column at 1.5 times maximum allowable casing pressure.

13.10.12 Vendor shall supply a 'dummy pump' of agreed diameter for which when lowered in a warm column will simulate a warm pump in a cold column. The 'dummy pump' should be of the

similar shape as the real pump to permit its use for training operators in removal procedures.

13.11 Name plate

13.11.1 Nameplate shall be provided in accordance with the requirements specified in API 610

paragraph 6.13.

13.11.2 The nameplate and rotation arrows (if attached) on external equipment shall be furnished of

18Cr-8Ni stainless steel or monel, securely attached by stainless steel pins at an easily accessible point and allowing for insulation thickness. Welding is not permitted.

13.11.3 The information required in API 610 paragraph 6.13.2 plus Manufacturer‟s name and the

casing hydrostatic test pressure, etc shall also be provided on the suction vessel.

13.12 Noise

The noise level shall be lower than the allowable limit.

Where standard equipment exceeds the required noise levels, Vendor shall take measures to reduce

the noise levels to meet the specified limits at his own cost. Typical measures may be:

- Selection of alternative designs

- Uni-directional, aerofoil section electric motor cooling fans

- Low noise trim on control valves

- Sound insulation on noisy piping systems, and direct lagging of certain equipment.

- Inlet and discharge silencers

- Acoustic enclosures

The design and integration of any acoustic device shall not impair the operation of the equipment

and will remain within the responsibility of the vendor.

The noise level shall be verified by noise test.

Noise test procedure shall be approved by Purchaser prior to test. Test procedure shall be based on international standard specified in Section 4.

13.13 Material

All material shall be specified by reference to the ASTM code. Alternative equivalent international

material code may be used upon Purchaser‟s written approval. In case non-ASTM materials are used, the equivalent ASTM code shall be shown on all relevant documents and drawings. Unless otherwise

specified, material of construction for all equipment shall be established on the basis of minimum operating temperatures and shall be, as minimum:

Minimum operating

temperature Material Corrosion Allowance

above –28.9°C carbon steel 3mm

-45.6 ~ -28.9°C impact tested carbon steel 3mm

-198 ~ -45.6°C 300 series stainless steel zero

9% nickel steel 1.2 mm (zero if prime coated)

aluminium or aluminium alloy zero

Material and specification for piping shall conform to the attached Purchaser‟s Piping Material Specification.

Acceptable grades of austenitic stainless steel are 304, 304L, 316, 316L, 317, 317L, 321, 347 and

348.

Austenitic stainless steel castings used for pressure components of valves, pumps and compressors

in cryogenic service (below minus 101°C) shall be impact tested at the minimum design temperature or lower.

Each batch/lot and heat of austenitic stainless steel welding (filler) material for services below minus

101°C shall be prequalified at the minimum design temperature or lower.

All stainless steel surfaces shall be pickled and passivated.

Aluminium alloys such as 5083-0, 8454-0, 5456-0 and 6061-T6 that are approved by the ASME Pressure Vessel Code are acceptable for LNG service.

Clad or lined materials shall not be used for cryogenic service.

13.14 Welding requirements

Weld requirements in this section are applicable to pressure containing parts on the outside,

exposed to atmosphere.

13.14.1 WPS and PQR requirement

Welding procedures for gas system piping and pressure parts shall be submitted for Purchaser‟s approval prior to welding work. They shall accompany by weld maps correlating

welds to the appropriate WPS and PQR.

The joint design, including root opening, shall be clearly shown in the WPS and PQR. Tolerances for all dimensions shall be included.

A separate WPS is required for each group of base metals which require a different AWS classification.

Weld repair procedure for major repairs (those affecting more than 50% of the casing wall thickness) shall be subject to Purchaser‟s approval prior to repair work. All pressure parts weld

repair shall be checked by radiograph. Weld repair record shall be submitted to Purchaser‟s or

3rd party inspector for acceptance.

13.14.2 Filler metals

Filler metals and fluxes shall be completely specified in the WPS and PQR by the use of applicable ASME/AWS specification

Use of non AWS filler metals and fluxes shall be subject to Purchaser‟s advanced written

approval. The product‟s relevant physical and mechanical properties and chemical analysis shall be submitted to Purchaser.

13.14.3 Preheat & heat treatment

The preheat recommendations of Appendix R of ASME Section VIII, Division 1 shall be

mandatory for all carbon and alloy steels. When preheat is a requirement for welding, it is also a requirement for back gouging, electric arc cutting, and flame cutting.

If required, post weld heat treatment cycles, method of heat treatment, heating rate, holding temperature (maximum and minimum), holding time, and cooling rate shall be defined in WPS

and PQR.

13.14.4 Welding process

Welding method not listed in this section shall be subject to the Purchaser‟s approval.

Submerged arc welding

Welding procedure shall be re-qualified whenever the welding flux or wire is changed from one

manufacturer to another, or from one manufacturer‟s grade to another grade from the same

manufacturer.

Alloy, semi-active, active flux or reground fused flux shall not be used.

Manual submerged arc welding is not permitted on pressure containing parts.

Lincoln 860 flux shall not be used for impact tested weldments with the design temperature

below minus 29°C

Gas tungsten arc (GTAW) and plasma arc (PAW) welding

Inert backing gas is required for all materials except carbon steel, carbon-molybdenum, x%

nickel steel and 1-1/4% and lower Cr steel.

For GTAW, SFA 5.18, ER70S-2 is the preferred welding wire for carbon steel.

Shield metal arc welding (SMAW)

Electrodes used for the SMAW process shall be of the low hydrogen type.

The SMAW shall not be used for root passes unless the backside of the root is ground or back

gouged to sound metal and back welded.

E6010 or E6011 electrodes may be used for welding the root pass and the subsequent pass in all carbon steel buttwelds, except (1) buttwelds in pipe 2” and smaller and (2) for welding

galvanized structural attachment to carbon steel pressure containing components.

The SMAW process shall not be used for root pass application in single welded joints of

stainless steel or nickel alloys.

Gas metal arc welding (GMAW)

Inert backing gas is required for all materials except carbon steel, carbon-molybdenum, x%

nickel steel, 1-1/4% and lower Cr steel, and similar materials unless the joint is ground or back

gouged to sound metal and back welded.

13.14.5 Welding material

Stainless steel

When “H grade” materials are specified, high carbon electrode, with 0.040% minimum carbon

shall be used.

The interpass temperature for austenitic stainless steel shall not be greater than 177°C.

Low temperature service

To ensure impact properties of austenitic stainless steel welds with design temperature of minus 101 oC or lower, each heat, lot, or batch of filler material and filler material/flux

combination shall be “pre-use” impact tested, except following filler materials:

- ENiCrFe-2 and E16-8-2-15 or 16 for SMAW

- ERNiCr-3 and ER16-8-2 for SAW, GTAW, GMAW, or PAW

- ER308, ER308L, ER316, or ER316L for GTAW

The report of “pre-use” impact test shall be attached to the applicable PQR.

14. ATTACHMENTS




ATTACHMENT #4. PURCHASER‟S STANDARD FORMS

Att #1


LP LNG Pump Data Sheets (7 sheets)

LNG Drain Pump Data Sheet (6 sheets)

Owner KOGAS Page No. 1 of 7

Project No. 080228 Item No. P-201A/B/C ~ P-207A/B/C

Project Name Service LP LNG Pumps

Location SAMCHEOK, Korea No. Required Twenty-one (21)

1 Applicable to: (X) Proposal ( ) Purchase ( ) As-built

2 Pump Size Type Vertical, In-Tank Retractible No. Stages

3 Manufacturer Model Serial No.

4 Remarks:

5

6 GENERAL

7 Pumps to operate in parallel with No. motor driven Twenty-one (21) No. turbine driven N.A

8 Pump item No. See above Pump item No. N.A

9 Gear item No. N.A Motor item No. Turbine item No. N.A

10 Gear Provided by N.A Motor provided by Pump Vendor Turbine provided by N.A

11 Gear Mounted by N.A Motor mounted by Pump Vendor Turbine mounted by N.A

12 Gear data sheet No. N.A Motor data sheet No. Sheet 6 Turbine data sheet No. N.A

13 OPERATING CONDITIONS *1)

14 (X) Capacity, nor / rated 330 / 330 m3/h LIQUID

15 Other (X) Type/name of liquid LNG

16 (X) Suct. press. max/rated MPa.a (X) Pumping temp. min/nor/max -163 / -159 / -157 oC 0

17 (X) Discharge press. MPa.a ( ) Vapor pressure, max. *5) MPa.a oC 0

18 (X) Differential press. MPa (X) Specific gravity, min/nor/max 0.434 / 0.451 / 0.478 *3)

19 (X) Differential head m NPSHav*1) m ( ) Specific heat, Cp MJ/kgoC 0

20 ( ) Process variations (6.1.3) (X) Viscosity 0.131 cP at PT oC Max. 0.173 cP

21 (X) Starting conditions (6.1.3) Disch. v/v open & full recirc. ( ) Corrosive / Erosive agent (6.12.1.9) None

22 Service: (X) Continuous ( ) Intermittent (Start/day) ( ) Chloride concentration None ppm

23 (X) Parallel operation required (6.1.11) ( ) H2S concentration (6.12.1.12) None ppm

24 Others Liquid (x) Hazardous (x) Flammable ( ) Other

25 Others

26 SITE AND UTILITY DATA

27 Location: PERFORMANCE *6)

28 ( ) Indoor ( ) Heated ( ) Under roof Proposal curve No. RPM rpm

29 ( ) Outdoor ( X) Unheated ( ) Partial sides ( ) Impeller dia. min/rated/max / / mm

30 ( ) Grade ( ) Mezzanine ( X) In-Tank ( ) Rated power kW Efficiency %

31 (X) Electrical area classification (6.1.22 / 7.1.5) ( ) Min. continous flow, thermal/stable / m3/h

32 Zone Gas Gr. T. class ( ) Preferred operating region to m3/h

33 ( ) Winterization required ( ) Tropicalization required ( ) Allow. operating region to m3/h

34 Site Data (6.1.28) ( ) Max. head @ rated impeller m

35 (X) Altitude m Barometer kPa.a ( ) Max. power @ rated impeller kW

36 (X) Range of ambient temp: min/max oC ( ) NPSH required at rated cap. (6.1.8) *4) m 0

37 (X) Relative humidity: min/max % ( ) Suction specific speed (6.1.9)

38 Unusual conditions: (6.1.28) ( ) Dust ( ) Fumes ( ) Min. pump startup level (above tank bottom) *8) m

39 ( ) Other ( ) Est. max. sound press. Level (6.1.14) dB(A)

40 ( ) Utility conditions ( ) Max. disch. press.*7) MPa.g

41 Steam: N.A Driver Heating Others

42 Press, min/max MPa.g

43 Temp. min/max oC General notes:

44 Electricity: Drivers Heating Control Shutdown 1. Vendor to advise if the heat input to the line exceed 2kJ/kg of LNG

45 Voltage pumped under the specified operating conditions.

46 Hertz 2. All blanks shall be filled out by Bidder/Vendor.

47 Phase

48 Cooling water: (6.1.17) Source N.A

49 Temp. inlet/max return N.A oC

50 Press. nor/design N.A MPa.g Specific notes:

51 Min. return/max dp N.A MPa.g *1) Suction condition, NPSH values are referenced to tank bottom.

52 Chloride concentration N.A ppm *2) Suction pressure, max. : 0.240 / 0.246 / 0.252 MPa.a

53 Instrument air: Type N.A *3) Lean (SG=0.434) / Rich (SG=0.478)

54 Press. min/max N.A MPa.g *4) NPSHr to be minimized to enable tank to be emptied to lowest

55 Others possible level.

56 *5) Vapour pressure, Min / Max : 0.127 / 0.142 MPa.a

57 *6) Vendor to specify performance values for each Lean / Rich LNG case.

58 *7) Max. discharge pressure at shut off condition shall not be greater than 1.86 MPa.g.

59 *8) Min. pump startup level to be less than 1.6 m from tank bottom. 0

60

N.A N.A

N.A

N.A

3

N.A

N.A

N.A

-14.1 / +37.0

6 / 90

6600

60

N.A

N.A

1 II B T4

Sea level 101.63

270 1.6

1.149 / 1.194 / 1.266 *3)

*2) / 0.122

LP LNG PUMP DATA SHEET

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LP LNG Pumps

PT

SAMCHEOK LNG Terminal

1.271 / 1.316 / 1.388 *3)



Project Name SAMCHEOK LNG Terminal Service LP LNG Pumps


1 CONSTRUCTION CONSTRUCTION (CONT)

2 Applicable standard: Couplings: (7.2.2) N.A

3 (X) API 610 11th edition ( ) Make

4 ( ) Other (See Remark) ( ) Model

5 ( ) Coupling rating (kW/100rpm)

6 Pump type: (4.2.1) ( ) Lubrication

7 ( ) OH2 ( ) BB1 ( ) VS1 ( ) VS6 ( ) Limited end float required

8 ( ) OH3 ( ) BB2 ( ) VS2 ( ) VS7 ( ) Spacer length

9 ( ) OH6 ( ) BB3 ( ) VS3 ( ) Other ( ) Service factor

10 ( ) BB4 ( ) VS4 Driver half coupling mounted by:

11 ( ) BB5 ( ) VS5 ( ) Pump mfr ( ) Driver mfr ( ) Purchaser

12 ( ) Coupling per API 671 (7.2.4)

13 Nozzle connections: (6.4.2)

14 Size Rating Facing Position Baseplates: N.A

15 Suction 24" 300# FF SF Bottom ( ) API baseplate number (Appendix M)

16 Discharge 6" 300# RF SF Column ( ) Non-grout construction: (7.3.13)

17 Balance drum

18 Pressure casing connections: (6.4.3) Remarks:

19 No. Size Rating Facing

20 ( ) Drain

21 ( ) Vent

22 ( ) Press. gauge MATERIAL

23 ( ) Temp. gauge ( ) Appendix H class (6.12.1.2) Vendor standard

24 ( ) Warm-up ( ) Min. design metal temp (6.12.4.1) oC

25 ( ) LT ( ) Barrel/case

26 ( ) Cylindrical threads required (6.4.3.8) ( ) Impeller

27 ( ) Case/impeller wear rings

28 Casing mounting: ( ) Shaft

29 ( ) Centerline ( ) Near centerline ( ) Diffusers

30 ( ) Foot ( ) Separate mounting plate ( ) Coupling spacer/hubs

31 ( ) In-line (X) Vertical In-Tank ( ) Coupling diaphragms (disks)

32 Casing split: ( )

33 ( ) Axial (X) Radial ( )

34 Casing type: ( )

35 ( ) Single volute ( ) Multiple volute (X) Diffuser ( )

36 ( ) Overhung ( ) Between bearings ( ) Barrel ( )

37 Case pressure rating: ( )

38 Max.allow. working press. MPa.g

39 at oC Remarks:

40 Hydrotest press. MPa.g

41 (X) Suction press. regions must be designed for MAWP (6.3.6)

42 Rotation: (Viewed from coupling end) ( ) CW ( ) CCW

43 (X) Impeller individually secured (9.2.1.2) BEARING AND LUBRICATION

44 Bearing (Type/Number)

45 Remarks: ( ) Radial /

46 ( ) Thrust /

47 ( ) Review and approve thrust bearing size (6.10.1.2)

48

49 ( ) Bolt OH3 pump to pad/foundation (9.1.2.2) Lubrication: (6.11) by pumped liquid (LNG)

50 ( ) Grease ( ) Flood ( ) Ring oil

51 Shaft: ( ) Flinger ( ) Purge oil mist ( ) Pure oil mist

52 ( ) Shaft diameter at coupling mm ( ) Constant level oiler preference (6.10.2.2)

53 ( ) Shaft diameter between bearings mm ( ) Pressure lube sys (9.2.6) ( ) API-610 ( ) API-614

54 ( ) Span between bearing centers mm ( ) Oil visc. ISO grade N.A

55 ( ) Span between bearing & impeller mm ( ) Oil heater req'd ( ) Electric ( ) Steam

56 Remarks: ( ) Oil press to be greater than coolant press

57 Remarks:

58

59

60

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1 INSTRUMENTATION VERTICAL PUMPS

2 Vibration: Vertical type ( ) VS1 ( ) VS2 ( ) VS3

3 ( ) Noncontacting (API 670) (x) Transducer *1) ( ) VS4 ( ) VS5 ( ) VS6 ( ) VS7 ( ) Other

4 ( ) Provision for mounting only (6.10.2.10)

5 ( ) Flat surface req'd (6.10.2.11) ( ) Pump thrust: (+) up (-) down

6 ( ) See attached API-670 data sheet at min. flow kg kg

7 ( ) Monitors and cables (7.4.2.4) at rated flow kg kg

8 at max. flow kg kg

9 Remarks: *1) mounted on pump casing as close as possible max. thrust kg kg

10 to bottom bearing. ( ) Soleplate: mm x mm

11 Amplifier & junction box to be supplied by Vendor. ( ) Soleplate thickness mm

12

13 Temperature and pressure: Column pipe: (X ) Flanged ( ) Threaded

14 ( ) Radial BRD metal temp. ( ) Thrust BRD metal temp. Diameter ID 584.2 mm mm 0

15 ( ) Provision for instruments only

16 ( ) See attached API-670 data sheet Guide bushing:

17 ( ) Temp. gauges (with thermowells) (7.4.1) ( ) Number

18 ( ) Other ( ) Line shaft bearing spacing mm

19 ( ) Pressure gauge type (7.4.1) Guide bushing lube: ( ) Water ( ) Oil

20 Location ( ) Grease ( ) Pumpage

21 Line shaft: ( ) Open ( ) Enclosed

22 Remarks: Line shaft dia: mm Tube dia: mm

23 Line shaft coupling:

24 ( ) Sleeve & key ( ) Threaded

25 ( ) Suction can thickness: mm

26 ( ) Length m

27 SPARE PARTS (TABLE 20) ( ) Diameter m

28 (x) Start-up (x) Normal maintenance

29 (x) Specify Vendor to recommend, subject to Purchaser's Suctions strainer type:

30 review. ( ) Float & rod ( ) Float switch

31 ( ) Impeller collets acceptable (6.6.3)

32 ( ) Hardened sleeves under bearings (9.3.10.5)

33 MOTOR DRIVE (7.1.5) *1) ( ) Resonance test (8.3.4.7)

34 ( ) Manufacturer ( ) Structural analysis (9.3.5)

35 ( ) Rating *2) kW rpm ( ) Drain piped to surface (9.3.13.5)

36 ( ) Horizontal (X) Vertical

37 ( ) Frame ( ) Sump depth m

38 ( ) Service factor ( ) Pump length m

39 (x) Volts/Ph/Hz 6600 / 3 / 60 (x) Min. pump start-up level *3) m

40 (x) Type Squirrel cage (x) Min. pump down level *3) m

41 (x) Enclosure IP 56 (J/B only) 0

42 (x) Min. starting voltage (6.1.5) 80% Remarks: *3) Referenced to Tank bottom. 0

43 ( ) Temperature rise

44 ( ) Full load amps

45 ( ) Locked rotor amps

46 ( ) Insulation

47 ( ) Starting method

48 ( ) Lube

49 ( ) Vertical thrust capacity

50 Up kg Down kg

51

52 Bearings (Type/number)

53 ( ) Radial /

54 ( ) Thrust /

55

56 Remarks: *1) See separate Electrical Motor Data Sheeet.

57 *2) Motor rating to be larger than BkW required throughout

58 the whole operating range at all operating conditions

59 specified in data sheet. Margin required by API 610

60 shall be applied at rated condition.

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1 SURFACE PREPARATION, PAINT & SHIPMENT QA INSPECTION AND TEST

2 ( ) Manufacturer's standard (X) Review vendors QA program ( 8.1.6)

3 (X) Other : Purchaser's painting spec. (X) Performance curve approval

4 Pumps: (X) Shop inspection ( 8.1.1)

5 ( ) Surface prep. ( ) Primer ( ) Test with substitute seal ( 8.3.3.2 b)

6 ( ) Finish coat

7 Baseplate: (7.3.12) Test Non-wit Wit Observe

8 ( ) Surface prep. ( ) Primer (X) Hydrostatic ( 8.3.2) ( ) (X) ( )

9 ( ) Finish coat (X) Performance ( 8.3.3) ( ) (X) ( )

10 Shipment: (8.4.1) (X) NPSH ( 8.3.4.3) ( ) (X) ( )

11 ( ) Domestic ( ) Export (X) Export boxing required (X) Complete unit test ( 8.3.4.4) ( ) (X) ( )

12 (X) Outdoor storage more than 6 months (X) Sound level test ( 8.3.4.5) ( ) (X) ( )

13 Spare rotor assembly packaged for: (X) Cleanliness prior to ( ) (X) ( )

14 ( ) Horiz. storage ( ) Vert. storage final assembly ( 8.2.2.6)

15 Type of shipping preparation ( ) Nozzle load test ( 7.3.21) ( ) ( ) ( )

16 Remarks: ( ) BRG hsg resonance ( ) ( ) ( )

17 test ( 8.3.4.7)

18 ( ) Remove/inspect

19 WEIGHT hydrodynamic bearings after test ( 9.2.7.5)

20 Motor driven ( ) Auxiliary equipment ( ) ( ) ( )

21 Pump & Motor kg test ( 8.3.4.6) ( )

22 Power cable & retraction system kg (X) Dismantle inspection ( ) (X) ( )

23 Headplate assembly kg (X) Cold hand spin test ( ) (X) ( )

24 Foot valve assembly kg ( ) ( ) ( ) ( )

25 kg ( ) ( ) ( ) ( )

26 kg (X) Material certification req'd ( 6.12.1.8)

27 Total weight kg (X) Casing (X) Impeller (X) Shaft

28 Turbine driven (X) Other All pressure retaining parts

29 Baseplate N.A kg (X) Casing repair procedure approval req'd ( 6.12.2.5)

30 Turbine N.A kg (X) Inspection required for connection welds ( 6.12.3.4 e)

31 Gear N.A kg ( ) mag. particle (X) Liquid penetrant

32 N.A kg (X) Radiographic ( ) Ultrasonic

33 N.A kg (X) Inspection required for casting ( 6.12.2.3 a)

34 Total weight N.A kg ( ) mag. particle (X) Liquid penetrant *2)

35 Remarks: (X) Radiographic *1) ( ) Ultrasonic

36 (X) Additional inspection required for: ( 8.2.1.3)

37 Shaft

38 OTHER PURCHASE REQUIREMENT ( ) mag. particle ( ) Liquid penetrant

39 (X) Coordination meeting required (10.1.3) ( ) Radiographic (X) Ultrasonic

40 (X) Review Owner's drawings related with pump installation (X) Additional inspection required for: ( 8.2.1.3)

41 ( ) Review piping draiwing Austenitic stainless steel castings

42 ( ) Observe piping check ( ) mag. particle ( ) Liquid penetrant

43 ( ) Observe initial alignment check ( ) Radiographic (X) Sharpy test

44 ( ) Check alignment at operating temperature ( ) Alternative acceptance criteria (See remark) ( 8.2.2.5)

45 (X) Connection design appoval ( 6.12.3.4) ( ) Hardness test required for: ( 8.2.2.7)

46 ( ) Rigging device req'd for type OH3 pump ( 9.1.2.6)

47 ( ) Hydrodynamic thrust BRG size review req'd ( 9.2.5.2.4) ( ) Wetting agent hydrotest ( 8.3.2.7)

48 (X) Lateral analysis required ( 9.1.3.4/9.2.4.1) (X) Vendor submit test procedure ( 8.3.1.1 / 10.2.5)

49 (X) Rotor dynamic balance ( 9.2.4.2) (X) Record final assembly running clearance

50 ( ) Mount seal reservoir off baseplate ( 7.5.1.4) ( ) Inspection check-list (Appendix N) ( 8.1.5)

51 (X) Installation list in proposal ( 10.2.3L) Remarks: *1) RT for pump casings

52 ( ) Spare rotor vertical storage ( 9.2.8.2) *2) PT for pump impellers

53 ( ) Torsional analysis / report ( 6.9.2.10)

54 (X) Progress reports required ( 10.3.3)

55 (X) Vendor to demonstrate max allowable vibration at min. flow.

56 ( )

57 ( )

58 Remarks:

59

60

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1

2

3

4

5

6

7

8

9

10

11

12

13

14

15

16

17

18

19

20

21

22

23

24

25

26

27

28

29

30 0

31 0

32

33

34

35

36

37

38

39

40

41

42

43

44

45

46

47

48

49 *1) Column size : 24" (ID = 584.2mm) * = Vendor to advise

50

51 *2) Those dimensions may change depending on suction valve design decided upon after order.

52

53 *3) Lifting cables will be used to withdraw primary pump from column and transport the pump to ground

54 level. Vendor shall supply cables of suitable length for the work.

55

56 *4) Those dimensions may change depending on suction valve design decided upon after order.Column height will be fixed by Tank designer during detail engineering.

57

58 Note

59 1. Vendor shall coordinate with tank manufacturer on all technical aspects for pump mounting & installation.

60

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InstrumentTerminalBox

MotorTerminalBox

Tank Bottom

Min Start-up Level(less than 1.6m fromtank bottom)Min

Pump downLevel

Tank Roof

Lifting Cables

Motor Cables

Earthing Cable

SupportCable

InstrumentCable

Discharge

N 2

VentVent

Vent

PI

Double ElectricalPenetration Seals

Pu

mp

Colu

mn

heig

ht,

appro

xim

ate

ly5

2.6

mete

rsto

be

con

firm

ed

aft

er

con

tract.

No

cost

&deliv

ery

impact

sh

all

be

allo

wed

inth

ism

att

er.

Spring loadedfoot valve

Flange Details

24" ASME B16.5 300# R.F

Main Lifting Point

InducerCentre Line

Size 6”

Rating 300# R.F

N 2

N 2

N 2N 2

*1)

*2)

*2)

*2)

Gland inHeadplate

*2)

*2)

Flange Details24" ASME B16.5 300# FF

*3)

*4)





1 DESIGN DATA MANUFACTURER'S DATA

2 Applicable specification IEC-60034 Frame No.

3 Motor type and arrangement Certifying authority

4 (X) Squirrel cage (X) Wound rotor

5 ( ) Horizontal (X) Vertical submerged

6 ( ) Foot ( ) Shaft up Load kW

7 ( ) Flange (x) Shaft down Efficiency %

8 Site data Current A

9 (X) Max. temp 37.0oC (X) Min. temp. -14.1

oC P.factor

10 (X) Direct sun temp. 65oC (X) Altitude Sea level Rated load torque kg-m (N-m)

11 (X) Humidity 90 / 6 % ( ) Fumes Locked rotor torque % FLT

12 (X) Salty atm. ( ) Other Locked rotor current A

13 Hazardous classification (for terminal boxes) Locked rotor power factor

14 Zone 1 Code IEC Pull up torque % FLT

15 Gas group II B T class T4 Breakdown torque % FLT

16 Type of protection IP 56 (only instrument & J/B) Protection ( ) Exe ( ) Exd ( ) Exn ( )

17 Driven equipment Equivalent diagram Start Stop

18 Type Cent. Pump Inertia (GD2) kg-m2 Rotor resistance PU *

19 Cooling method Rotor reactance PU *

20 ( ) TEFC ( ) CACA ( ) CACW Stator resistance/reactance / PU *

21 ( ) Pipe ventilated (X) Pumped liquid Magnetising resistance/reactance / PU *

22 Basic data Sub transient reactance x'd % *

23 Nameplate rating kW Open circuit time constant T'oo Sec *

24 Volts/Ph/Hz 6600 / 3 / 60 Rated load speed rpm

25 Syn. Speed rpm Service factor ( ) Fan ( ) Uni-directional ( ) By-directional

26 Rotation viewed on coupling end ( ) CW ( ) CCW Unit run-up time Sec

27 System ( ) 3 wire ( ) 4 wire Te time Sec

28 Insulation class Allow. temp. riseoC Safe stall time (cold) Sec

29 Starting conditions Safe stall time (hot) Sec

30 (X) Full volge (X) Red. Volts 80 % No. of starts allowed (cold) 0

31 (X) Unloaded (X) Loaded No. of starts allowed (hot)

32 Starter ( ) Vacuum ( ) Oil ( ) Air Winding ( ) Star ( ) Delta

33 Control (X) DOL ( ) Star/Delta Fault rating MVA

34 Re-acceleration ( ) Yes ( ) No Main terminal box

35 Auto-transformer ( ) Yes ( ) No Maximum entry size mm

36 Main terminal box Temp. detector terminal box

37 Type Maximum entry size mm

38 Location viewed on NDE ( ) LHS ( ) RHS ( ) Top Anti-condensation heater N.A

39 Entry ( ) Threaded size ( ) Wiping cone Rating kW

40 Conductors mat'l No. Size Maximum entry size mm

41 * Cable dia. O/L O/A O/ALL Mechanical data

42 Anti-condensation heater Motor net weight kg

43 ( ) Yes (X) No Volt Ph Motor inertia (GD2) kg-m2

44 Entry type threaded Size Rotor end float mm

45 Resistance temperature detectors N.A Limit end float to ± mm

46 Number Resistance Utilities

47 ( ) Selector switch ( ) Relay ( ) Indicator Lube oil m3/h Heat load MJ

48 By ( ) Purchaser ( ) Manufacturer Other data to be furnished

49 Other protection ( ) Differential ( ) Stress cones (X) Speed vs. torque curve @ 100%, 80% volts

50 Bearings (X) Speed vs. current curve

51 Type Lubrication (X) Time vs. current curve

52 Temp. device ( ) Yes (X) No Type

53 Cooling water N.A

54 Temp. In.oC Out

oC Notes: * maked data not required for low tension motors

55 Design pressure MPa.g below 37 kW.

56 Noise limitation 85 dB(A) @ 1m

57 Painting

58 Notes:

59

60

3/4 1/2

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ELECTRICAL MOTOR DATA SHEET

rating Normal

AbsorbedN'plate





1 Manufacturer

2 Type

3 Model

4

5 EQUIPMENT DESIGN DATA

6 Calculated DL = SWL (Note 1)

7 Efficiency %

8 Equipment size (L x W x H) m Driver type

9 Power kW Driver speed rpm

10 Capacity m3/hr Equipment speed rpm

11 Pressure discharge MPa.a Gear tooth contact rate Hz

12 Pressure suction MPa.a Blades / vanes pass frequency

13 Equipment weight kg Number of stator / number of rotor blade ratio

14

15 PURCHASER SPECIFIED DATA

16 Noise level limit dB(A) Octave band center frequency

17 SPL (Note 1) 31.5 63 125 250 500 1000 2000 4000 8000

18 85

19

20

21

22 Special requirement:

23

24

25 Noise test required: Vibration test required:

26 (X) Yes ( ) No ( ) Optional (X) Yes ( ) No ( ) Optional

27 SUPPLIER'S DATA

28 Guaranteed SWL dB(A) Octave band center frequency

29 (Note 1) 31.5 63 125 250 500 1000 2000 4000 8000

30

31

32

33

34

35 Guaranted SPL

36 Narrow band component, Yes / No Frequency / octave band Hz

37 Method / standard for noise level test:

38

39

40

41 Description of implemented noise control measure / other information:

42

43

44

45 AS-BUILT NOISE DATA

46 Measured noise dB(A) Octave band center frequency

47 level (Note 1) 31.5 63 125 250 500 1000 2000 4000 8000

48

49

50

51

52 Special information:

53

54

55 Note 1 SPL Sound pressure level, in dB (re. 20 mPa) at 1m distance free field conditions.

56 SWL Sound power level, in dB (re. 1pW).

57 Note 2 VVL Vibration velocity level, in dB (re. 5 x 10^4 m/s) RMS on skid adjacent to support points.

58 Remarks:

59

60

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EQUIPMENT NOISE DATA SHEET


Project No. 080228 Item No. P-102 / P-305

Project Name SAMCHEOK LNG Terminal Service LNG Drain Pumps

Location SAMCHEOK, Korea No. Required Two (2)

1 Applicable to: (X) Proposal ( ) Purchase ( ) As-built

2 Pump Size Type No. Stages

3 Manufacturer Model Serial No.

4 Remarks:

5

6 Note: ( ) Indicates information completed by Purchaser ( ) By manufacturer ( ) By manufacturer or purchaser

7

8 Pumps to operate in (parallel) No. motor driven No. turbine driven

9 (serial) with Pump item No. Pump item No.

10 Gear item No. Motor item No. Turbine item No.

11 Gear Provided by Motor provided by Turbine provided by

12 Gear Mounted by Motor mounted by Turbine mounted by

13 Gear data sheet No. Motor data sheet No. Turbine data sheet No.

14

15 (X) Capacity, Normal (m3/h) Rated (m3/h) Water source

16 Other Chloride concentration (ppm)

17 (X) Suction pressure, Max/Rated (MPa.a) Instrument air: Max/Min press. (MPa.g)

18 (X) Discharge pressure (MPa.a)

19 (X) Differential pressure (MPa) ( ) Type/Name of liquid

20 (X) Differential head (m) NPSHav (m) (X) Pumping temp.

21 ( ) Process variations (6.1.3) Min/Nor/Max / / (oC)

22 ( ) Starting conditions (6.1.3) ( ) Vapor pressure (MPa.a) at (oC)

23 Service: ( ) Continuous (X) Intermittent (Start/day) (X) Relative density (SG)

24 ( ) Parallel operation required (6.1.11) Min/Nor/Max / /

25 ( ) Specific heat, Cp (kJ/kgoC)

26 Location: (X) Viscosity (cP) at (oC) 0

27 ( ) Indoor ( ) Heated ( ) Under roof (X) Max viscosity (cP)

28 ( ) Outdoor (X) Unheated ( ) Partial sides ( ) Corrosive / Erosive agent (6.12.1.9)

29 ( ) Grade ( ) Mezzanine (X) ( ) Chloride concentration (ppm)

30 (X) Electrical area classification (6.1.22/7.1.5) ( ) H2S concentration (6.12.1.12) (ppm)

31 Zone Gas group Class Liquid (X) Hazardous (X) Flammable ( ) Other

32 ( ) Winterization required ( ) Tropicalization required

33 Site Data (6.1.28)

34 ( ) Altitude (m) Barometer (kPa.a) Proposal curve No. ( ) RPM

35 ( ) Range of ambient temp: Min/Max / (oC) ( ) Impeller dia. Min/Rated/Max (mm)

36 ( ) Relative humidity: Min/Max / (%) ( ) Rated power (kW) Efficiency (%)

37 Unusual conditions: (6.1.28) ( ) Dust ( ) Fumes ( ) Min. continous flow:

38 ( ) Other Thermal (m3/h) Stable (m3/h)

39 ( ) Utility conditions ( ) Preferred operating region to (m3/h)

40 Steam: Drivers Heating ( ) Allow. operating region to (m3/h)

41 Min. (MPa.g) (oC) (MPa.g) (oC) ( ) Max. head @ rated impeller (m)

42 Max. (MPa.g) (oC) (MPa.g) (oC) ( ) Max. power @ rated impeller (kW)

43 Electricity: Drivers Heating Control Shutdown ( ) NPSH required at rated cap. (6.1.8) (m)

44 Voltage ( ) Suction specific speed (6.1.9)

45 Hertz ( ) Min. pump startup level (above drum bottom) (m)

46 Phase ( ) Est. max. sound press. Level (6.1.14) (dBA)

47 Cooling water: (6.1.17) Source Remarks

48 Temp. Inlet/Max return / (oC) *1)

49 Press. Nor/Dsn / (MPa.g) *2)

50 Min. return/Max dp / (MPa.g) *3) 0

51 *4)

52

53

54 General notes:

55

56

57

58

59

60

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LNG DRAIN PUMP DATA SHEET

P-305 : Process Area Drain Drum Pump

N.A

LNG

0.133

0.180

NPSH value is referenced to drain drum bottom level.

For Typical LNG

N.A

N.A

N.A

440

60

3 N.A

N.A

N.A

P-102 : Unloading Line Drain Drum Pump

*5)

Vapour press. min./max.:0.106/0.13 MPa.a

N.A

*5) Max. discharge pressure at shut off condition shall not be greater than 1.77 Mpa.g.

N.A

LIQUID

N.A

N.A

PERFORMANCE

0.434

-159

None

None

None

310

6 90

37.4

IIB T4

-14.1

0.5 *2)

N.A

Pump Vendor

GENERAL

-158

N.AN.A

OPERATING CONDITIONS

/ 0.13

1.50 *1)

1.37 *1)

4040

Lean (SG=0.434) / Typical (SG=0.451) / Rich (SG=0.478)

Sheet 6

0.478

*3)

*4)

N.A

SITE AND UTILITY DATA (CONT.)

-159

0.451

Vertical, Submersible

Two (2)

P-102 / 305

101.63

SITE AND UTILITY DATA

N.A

N.A

In-Tank

Sea level

1

N.A

N.A N.A

N.A

Pump Vendor





1












13 ( ) Nozzle connections: (6.4.2)

14 Baseplates: N.A

15 Suction ( ) API baseplate number (Appendix M)

16 Discharge ( ) Non-grout construction: (7.3.13)

17 Balance drum


19

20 ( ) Drain

21 ( ) Vent (Column)

22 ( ) Press. gauge

23 ( ) Temp. gauge ( ) Appendix H class (6.12.1.2)

24 ( ) Warm-up ( ) Min. design metal temp (6.12.4.1) (oC)

25 ( ) ( ) Casing

26 ( ) Cylindrical threads required (6.4.3.8) ( ) Impeller/Inducer 0








34 Casing type: ( )




38 ( ) Max.allowable working press. (MPa.g)

39 ( ) at (oC) Remarks:

40 ( ) Hydrotest press. (MPa.g)

41 (X) Suction press. Regions must be designed for MAWP (6.3.6)

42 Rotation: (Viewed from suction end)

43 ( ) CW ( ) CCW

44 (X) Impeller individually secured (9.2.1.2) Bearing (Type/Number)


46 ( ) Thrust /


48 ( ) Bolt OH3 pump to pad/foundation (9.1.2.2)

49 Lubrication: (6.11) by pumped liquid (LNG)

50 Shaft: ( ) Grease ( ) Flood ( ) Ring oil

51 ( ) Shaft diameter at coupling (mm) ( ) Flinger ( ) Purge oil mist ( ) Pure oil mist

52 ( ) Shaft diameter between bearings (mm) ( ) Constant level oiler preference (6.10.2.2)

53 ( ) Span between bearing centers (mm) ( ) Pressure lube sys (9.2.6) ( ) API-610 ( ) API-614

54 ( ) Span between bearing & impeller (mm) ( ) Oil visc. ISO grade

55 Remarks: ( ) Oil heater req'd ( ) Electric ( ) Steam

56 ( ) Oil press to be greater than coolant press

57 Remarks:

58

59

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BEARING AND LUBRICATION

1 1" 300# RF

Column

Bottom

TypeSize(NPS)

300# RF

No.

CONSTRUCTION

Size Rating Facing Position

16" 300# FF

*1)

MATERIAL

Vendor standard

*1) 4" for D-102, 3" for D-305

N.A





1

2 Vibration: Vertical type (Fig.1.1) ( ) VS1 ( ) VS2 ( ) VS3

3 ( ) Noncontacting (API 670) ( ) Transducer ( ) VS4 ( ) VS5 ( ) VS6 ( ) VS7 ( ) Other



6 ( ) See attached API-670 data sheet at min. flow (kg) (kg)

7 ( ) Monitors and cables (7.4.2.4) at rated flow (kg) (kg)

8 at max. flow (kg) (kg)

9 Remarks: max. thrust (kg) (kg)

10 ( ) Soleplate (mm) x (mm)

11 ( ) Soleplate thickness (mm)

12

13 Temperature and pressure: Column pipe: (X) Flanged ( ) Threaded

14 ( ) Radial BRD metal temp. ( ) Thrust BRD metal temp. Diameter (mm) (m) 0




18 Other ( ) Line shaft bearing spacing (mm)

19 ( ) Pressure guage type (7.4.1) Guide bushing lube: ( ) Water ( ) Oil

20 Location ( ) Grease (X) Pumpage


22 Remarks: ( ) Line shaft dia: (mm) ( ) Tube dia: (mm)



25 ( ) Suction can thickness (mm)

26 ( ) Length (m)

27 ( ) Diameter (m)

28 (X) Start-up (X) Normal maintenance

29 (X) Specify ( ) Suctions strainer type

30 ( ) Float & rod ( ) Float switch



33 ( ) Resonance test (8.3.4.7)


35 ( ) (kW) (rpm) ( ) Drain piped to surface (9.3.13.5)


37 ( ) Frame ( ) Sump depth (m)

38 ( ) Service factor ( ) Pump length (m)

39 (X) Volts/Ph/Hz / / (X) Min. pump startup level *3) (m)

40 (X) Type (X) Min. pump down level at rated flow *3) (m)

41 (X) Enclosure

42 (X) Min. starting voltage (3.1.6) Remarks: 0




46 ( ) Insulation


48 ( ) Lube


50 ( ) Up (kg) Down (kg)

51


53 ( ) Radial /

54 ( ) Thrust /

55

56 Remarks:

57

58

59

60

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ID 386.4

MOTOR DRIVE (7.1.5) *1)

SPARE PARTS (TABLE 20)

Vendor to recommend

80%

*1) See separate Electrical Motor Data Sheet.

*2) Motor rating to be larger than BHP required throughout

the whole operaing range at all operating conditions

specified in data sheet.

IP 56 (only J/B)

440 3 60

Submerged

INSTRUMENTATION VERTICAL PUMPS

*3) to be referenced to drum bottom.





1

2 ( ) Manufacturer's standard (X) Review vendors QA program (8.1.6)

3 (X) Other Purchaser's painting spec. (X) Performance curve approval

4 Pumps: (X) Shop inspection (8.1.1)

5 ( ) Surface prep. ( ) Primer ( ) Test with substitute seal (8.3.3.2.b)

6 ( ) Finish coat


8 ( ) Surface prep. ( ) Primer (X) Hydrostatic (8.3.2) ( ) (X) ( )

9 ( ) Finish coat (X) Performance (8.3.3) ( ) (X) ( )

10 Shipment: (8.4.1) (X) NPSH (8.3.4.3) ( ) (X) ( )

11 ( ) Domestic ( ) Export (X) Export boxing required (X) Complete unit test (8.3.4.4) ( ) (X) ( )

12 (X) Outdoor storage more than 6 months (X) Sound level test (8.3.4.5) ( ) (X) ( )


14 ( ) Horiz. storage ( ) Vert. storage final assembly (8.2.2.6)

15 ( ) Type of shipping preparation ( ) Nozzle load test (7.3.21) ( ) ( ) ( )


17 test (8.3.4.6)


19 hydrodynamic bearings after test (9.2.7.5)


21 Pump / Motor (kg) test (8.3.4.7)

22 Elec. system (kg) (X) Dismatle inspection ( ) (X) ( )

23 Headplate assembly (kg) (X) Cold hand spin test ( ) (X) ( )

24 Foot valve assembly (kg) ( ) ( ) ( ) ( )

25 (kg) ( ) ( ) ( ) ( )

26 (kg) (X) Material certification req'd (6.12.1.8)

27 Total weight of pump & system (kg) (X) Casing (X) Impeller (X) Shaft

28 Turbine driven (X) Other

29 Baseplate (kg) (X) Casing repair procedure approval req'd (6.12.2.5)

30 Turbine (kg) (X) Inspection required for connection welds (6.12.3.4.e)

31 Gear (kg) ( ) mag. particle (X) Liquid penetrant

32 (kg) (X) Radiographic ( ) Ultrasonic

33 (kg) (X) Inspection required for casting (6.2.2.3.a)

34 Total weight (kg) ( ) mag. particle (X) Liquid penetrant

35 Remarks: (X) Radiographic ( ) Ultrasonic 0

36 (X) Additional inspection required for: (8.2.1.3)

37

38 ( ) mag. particle ( ) Liquid penetrant


40 (X) Review Owner's drawings related with pump installation (X) Additional inspection required for: (8.2.1.3)

41 ( ) Review piping draiwing



44 ( ) Check alignment at operating temperature ( ) Alternative acceptance criteria (See remark) (8.2.2.5)

45 (X) Connection design appoval (6.12.3.4) ( ) Hardness test required for: (8.2.2.7)

46 ( ) Rigging device req'd for type OH3 pump (9.1.2.6)

47 ( ) Hydrodynamic thrust BRG size review req'd (9.2.5.2.4) ( ) Wetting agent hydrotest (8.3.2.7)

48 (X) Lateral analysis required (9.1.3.4 / 9.2.4.1) (X) Vendor submit test procedure (8.3.1.1/10.2.5)

49 (X) Rotor dynamic balance (9.2.4.2) (X) Record final assembly running clearance

50 ( ) Mount seal reservoir off baseplate (7.5.1.4) ( ) Inspection check-list (Appendix N) (8.1.5)

51 (X) Installation list in proposal (10.2.3L) Remarks:

52 ( ) Spare rotor vertical storage (9.2.8.2)

53 ( ) Torsional analysis / report (6.9.2.10)

54 (X) Progress reports required (10.3.3)

55 (X) Review drum column drawing for interface check

56 (X) Vendor demonstration of max. allowable vibration at min. flow.

57 ( )

58 Remarks:

59

60

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QA INSPECTION AND TEST

Shaft

All pressure retaining parts

OTHER PURCHASE REQUIREMENT

N.A

N.A

N.A

N.A

N.A

N.A

WEIGHT

Austenitic stainless steel castings

SURFACE PREPARATION, PAINT & SHIPMENT





1

2 Applicable specification Frame No.





7 ( ) Flange (X) Shaft down Effc'y %

8 Site data Current Amps

9 (X) Max. temp oC (X) Min. temp. oC P.factor %

10 (X) Direct sun temp. oC (X) Altitude Rated load torque kgm

11 (X) Humidity % ( ) Fumes Locked rotor torque % FLT

12 (X) Salty atm. ( ) Other Locked rotor current Amps

13 Hazardous classification (for Junction Boxes) Locked rotor power factor

14 Zone Code Pull up torque % FLT

15 Gas group T class Breakdown torque % FLT

16 Type of protection Protection ( ) Exe ( ) Exd ( ) Exn ( )


18 Type Inertia (GD2) kgm2 Rotor resistance PU *


20 ( ) TEFC ( ) CACA ( ) CACW Stator resistance/reactance / PU*

21 ( ) Pipe ventilated (X) Pumped liquid Magnetising resistance/reactance / PU*

22 Basic data Sub transient reactance x'd %*

23 Nameplate rating kW Open circuit time constant T'oo Secs*

24 Volts/Ph/Hz / / Rated load speed rpm


26 Rotation viewed on coupling end ( ) CW ( ) CCW Unit run-up time Secs

27 System ( ) 3 wire ( ) 4 wire Te time Secs

28 Insulation class Allow. temp. rise oC Safe stall time (cold) Secs

29 Starting conditions Safe stall time (hot) Secs

30 (X) Full volge (X) Red. Volts % No. of starts allowed (cold) 0



33 Control ( ) DOL ( ) Star/Delta Fault rating MVA










43 ( ) Yes (X) No Volt Ph Motor inertia (GD2) kgm2




47 ( ) Selector switch ( ) Relay ( ) Indicator Lube oil m3/h Heat load kcal

48 By ( ) Purchaser ( ) Manufacturer Cool'g water m3/h Heat load kcal

49 Other protection ( ) Differential ( ) Stress cones Other data to be furnished

50 Bearings (X) Speed vs. torque curve @ 100%, 80% volts

51 Type Lubrication (X) Speed vs. current curve

52 Temp. device ( ) Yes (X) No Type (X) Time vs. current curve

53 Cooling water N.A ( )

54 Temp. In. ℃ Out oC Notes: * maked data not required for low tension motors

55 Design pressure kPa.g below 37 kW.

56 Noise limitation

57 Painting

58 Notes:

59

60

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80

440

F

IP 56 ( J / B only )

3 60

DESIGN DATA

IEC-60034

Purchaser's painting spec.

MANUFACTURER'S DATA

Absorbed

Normal

3/4

65

90/6

Sea level

85 dB(A) @ 1m

-14.1

1

IIB

IEC

T4

37

1/2N'plate

rating





1 Manufacturer

2 Type

3 Model

4



7 Efficiency %



10 Capacity Equipment speed rpm




14



17 SPL (Note 1) 31.5 63 125 250 500 1000 2000 4000 8000

18 85

19

20

21


23

24



27 SUPPLIER'S DATA


29 (Note 1) 31.5 63 125 250 500 1000 2000 4000 8000

30

31

32

33

34

35 Guaranted SPL



38

39

40


42

43

44



47 level (Note 1) 31.5 63 125 250 500 1000 2000 4000 8000

48

49

50

51


53

54




58 Remarks:

59

60

R

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V






1












13 ( ) Nozzle connections: (6.4.2)

14 Baseplates: N.A

15 Suction ( ) API baseplate number (Appendix M)

16 Discharge ( ) Non-grout construction: (7.3.13)

17 Balance drum


19

20 ( ) Drain

21 ( ) Vent (Column)

22 ( ) Press. gauge

23 ( ) Temp. gauge ( ) Appendix H class (6.12.1.2)

24 ( ) Warm-up ( ) Min. design metal temp (6.12.4.1) (oC)

25 ( ) ( ) Casing

26 ( ) Cylindrical threads required (6.4.3.8) ( ) Impeller/Inducer 0








34 Casing type: ( )




38 ( ) Max.allowable working press. (MPa.g)

39 ( ) at (oC) Remarks:

40 ( ) Hydrotest press. (MPa.g)

41 (X) Suction press. Regions must be designed for MAWP (6.3.6)

42 Rotation: (Viewed from suction end)

43 ( ) CW ( ) CCW

44 (X) Impeller individually secured (9.2.1.2) Bearing (Type/Number)


46 ( ) Thrust /


48 ( ) Bolt OH3 pump to pad/foundation (9.1.2.2)

49 Lubrication: (6.11) by pumped liquid (LNG)

50 Shaft: ( ) Grease ( ) Flood ( ) Ring oil

51 ( ) Shaft diameter at coupling (mm) ( ) Flinger ( ) Purge oil mist ( ) Pure oil mist

52 ( ) Shaft diameter between bearings (mm) ( ) Constant level oiler preference (6.10.2.2)

53 ( ) Span between bearing centers (mm) ( ) Pressure lube sys (9.2.6) ( ) API-610 ( ) API-614

54 ( ) Span between bearing & impeller (mm) ( ) Oil visc. ISO grade

55 Remarks: ( ) Oil heater req'd ( ) Electric ( ) Steam

56 ( ) Oil press to be greater than coolant press

57 Remarks:

58

59

60

R

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V


BEARING AND LUBRICATION

1 1" 300# RF

Column

Bottom

TypeSize(NPS)

300# RF

No.

CONSTRUCTION

Size Rating Facing Position

16" 300# FF

*1)

MATERIAL

Vendor standard

*1) 4" for D-102, 3" for D-305

N.A





1

2 Vibration: Vertical type (Fig.1.1) ( ) VS1 ( ) VS2 ( ) VS3

3 ( ) Noncontacting (API 670) ( ) Transducer ( ) VS4 ( ) VS5 ( ) VS6 ( ) VS7 ( ) Other



6 ( ) See attached API-670 data sheet at min. flow (kg) (kg)

7 ( ) Monitors and cables (7.4.2.4) at rated flow (kg) (kg)

8 at max. flow (kg) (kg)

9 Remarks: max. thrust (kg) (kg)

10 ( ) Soleplate (mm) x (mm)

11 ( ) Soleplate thickness (mm)

12

13 Temperature and pressure: Column pipe: (X) Flanged ( ) Threaded

14 ( ) Radial BRD metal temp. ( ) Thrust BRD metal temp. Diameter (mm) (m) 0




18 Other ( ) Line shaft bearing spacing (mm)

19 ( ) Pressure guage type (7.4.1) Guide bushing lube: ( ) Water ( ) Oil

20 Location ( ) Grease (X) Pumpage


22 Remarks: ( ) Line shaft dia: (mm) ( ) Tube dia: (mm)



25 ( ) Suction can thickness (mm)

26 ( ) Length (m)

27 ( ) Diameter (m)

28 (X) Start-up (X) Normal maintenance

29 (X) Specify ( ) Suctions strainer type

30 ( ) Float & rod ( ) Float switch



33 ( ) Resonance test (8.3.4.7)


35 ( ) (kW) (rpm) ( ) Drain piped to surface (9.3.13.5)


37 ( ) Frame ( ) Sump depth (m)

38 ( ) Service factor ( ) Pump length (m)

39 (X) Volts/Ph/Hz / / (X) Min. pump startup level *3) (m)

40 (X) Type (X) Min. pump down level at rated flow *3) (m)

41 (X) Enclosure

42 (X) Min. starting voltage (3.1.6) Remarks: 0




46 ( ) Insulation


48 ( ) Lube


50 ( ) Up (kg) Down (kg)

51


53 ( ) Radial /

54 ( ) Thrust /

55

56 Remarks:

57

58

59

60

R

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V


ID 386.4

MOTOR DRIVE (7.1.5) *1)

SPARE PARTS (TABLE 20)

Vendor to recommend

80%

*1) See separate Electrical Motor Data Sheet.

*2) Motor rating to be larger than BHP required throughout

the whole operaing range at all operating conditions

specified in data sheet.

IP 56 (only J/B)

440 3 60

Submerged

INSTRUMENTATION VERTICAL PUMPS

*3) to be referenced to drum bottom.





1

2 ( ) Manufacturer's standard (X) Review vendors QA program (8.1.6)

3 (X) Other Purchaser's painting spec. (X) Performance curve approval

4 Pumps: (X) Shop inspection (8.1.1)

5 ( ) Surface prep. ( ) Primer ( ) Test with substitute seal (8.3.3.2.b)

6 ( ) Finish coat


8 ( ) Surface prep. ( ) Primer (X) Hydrostatic (8.3.2) ( ) (X) ( )

9 ( ) Finish coat (X) Performance (8.3.3) ( ) (X) ( )

10 Shipment: (8.4.1) (X) NPSH (8.3.4.3) ( ) (X) ( )

11 ( ) Domestic ( ) Export (X) Export boxing required (X) Complete unit test (8.3.4.4) ( ) (X) ( )

12 (X) Outdoor storage more than 6 months (X) Sound level test (8.3.4.5) ( ) (X) ( )


14 ( ) Horiz. storage ( ) Vert. storage final assembly (8.2.2.6)

15 ( ) Type of shipping preparation ( ) Nozzle load test (7.3.21) ( ) ( ) ( )


17 test (8.3.4.6)


19 hydrodynamic bearings after test (9.2.7.5)


21 Pump / Motor (kg) test (8.3.4.7)

22 Elec. system (kg) (X) Dismatle inspection ( ) (X) ( )

23 Headplate assembly (kg) (X) Cold hand spin test ( ) (X) ( )

24 Foot valve assembly (kg) ( ) ( ) ( ) ( )

25 (kg) ( ) ( ) ( ) ( )

26 (kg) (X) Material certification req'd (6.12.1.8)

27 Total weight of pump & system (kg) (X) Casing (X) Impeller (X) Shaft

28 Turbine driven (X) Other

29 Baseplate (kg) (X) Casing repair procedure approval req'd (6.12.2.5)

30 Turbine (kg) (X) Inspection required for connection welds (6.12.3.4.e)

31 Gear (kg) ( ) mag. particle (X) Liquid penetrant

32 (kg) (X) Radiographic ( ) Ultrasonic

33 (kg) (X) Inspection required for casting (6.2.2.3.a)

34 Total weight (kg) ( ) mag. particle (X) Liquid penetrant

35 Remarks: (X) Radiographic ( ) Ultrasonic 0

36 (X) Additional inspection required for: (8.2.1.3)

37

38 ( ) mag. particle ( ) Liquid penetrant


40 (X) Review Owner's drawings related with pump installation (X) Additional inspection required for: (8.2.1.3)

41 ( ) Review piping draiwing



44 ( ) Check alignment at operating temperature ( ) Alternative acceptance criteria (See remark) (8.2.2.5)

45 (X) Connection design appoval (6.12.3.4) ( ) Hardness test required for: (8.2.2.7)

46 ( ) Rigging device req'd for type OH3 pump (9.1.2.6)

47 ( ) Hydrodynamic thrust BRG size review req'd (9.2.5.2.4) ( ) Wetting agent hydrotest (8.3.2.7)

48 (X) Lateral analysis required (9.1.3.4 / 9.2.4.1) (X) Vendor submit test procedure (8.3.1.1/10.2.5)

49 (X) Rotor dynamic balance (9.2.4.2) (X) Record final assembly running clearance

50 ( ) Mount seal reservoir off baseplate (7.5.1.4) ( ) Inspection check-list (Appendix N) (8.1.5)

51 (X) Installation list in proposal (10.2.3L) Remarks:

52 ( ) Spare rotor vertical storage (9.2.8.2)

53 ( ) Torsional analysis / report (6.9.2.10)

54 (X) Progress reports required (10.3.3)

55 (X) Review drum column drawing for interface check

56 (X) Vendor demonstration of max. allowable vibration at min. flow.

57 ( )

58 Remarks:

59

60

R

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QA INSPECTION AND TEST

Shaft

All pressure retaining parts

OTHER PURCHASE REQUIREMENT

N.A

N.A

N.A

N.A

N.A

N.A

WEIGHT

Austenitic stainless steel castings

SURFACE PREPARATION, PAINT & SHIPMENT





1

2 Applicable specification Frame No.





7 ( ) Flange (X) Shaft down Effc'y %

8 Site data Current Amps

9 (X) Max. temp oC (X) Min. temp. oC P.factor %

10 (X) Direct sun temp. oC (X) Altitude Rated load torque kgm

11 (X) Humidity % ( ) Fumes Locked rotor torque % FLT

12 (X) Salty atm. ( ) Other Locked rotor current Amps

13 Hazardous classification (for Junction Boxes) Locked rotor power factor

14 Zone Code Pull up torque % FLT

15 Gas group T class Breakdown torque % FLT

16 Type of protection Protection ( ) Exe ( ) Exd ( ) Exn ( )


18 Type Inertia (GD2) kgm2 Rotor resistance PU *


20 ( ) TEFC ( ) CACA ( ) CACW Stator resistance/reactance / PU*

21 ( ) Pipe ventilated (X) Pumped liquid Magnetising resistance/reactance / PU*

22 Basic data Sub transient reactance x'd %*

23 Nameplate rating kW Open circuit time constant T'oo Secs*

24 Volts/Ph/Hz / / Rated load speed rpm


26 Rotation viewed on coupling end ( ) CW ( ) CCW Unit run-up time Secs

27 System ( ) 3 wire ( ) 4 wire Te time Secs

28 Insulation class Allow. temp. rise oC Safe stall time (cold) Secs

29 Starting conditions Safe stall time (hot) Secs

30 (X) Full volge (X) Red. Volts % No. of starts allowed (cold) 0



33 Control ( ) DOL ( ) Star/Delta Fault rating MVA










43 ( ) Yes (X) No Volt Ph Motor inertia (GD2) kgm2




47 ( ) Selector switch ( ) Relay ( ) Indicator Lube oil m3/h Heat load kcal

48 By ( ) Purchaser ( ) Manufacturer Cool'g water m3/h Heat load kcal

49 Other protection ( ) Differential ( ) Stress cones Other data to be furnished

50 Bearings (X) Speed vs. torque curve @ 100%, 80% volts

51 Type Lubrication (X) Speed vs. current curve

52 Temp. device ( ) Yes (X) No Type (X) Time vs. current curve

53 Cooling water N.A ( )

54 Temp. In. ℃ Out oC Notes: * maked data not required for low tension motors

55 Design pressure kPa.g below 37 kW.

56 Noise limitation

57 Painting

58 Notes:

59

60

R

E

V


80

440

F

IP 56 ( J / B only )

3 60

DESIGN DATA

IEC-60034

Purchaser's painting spec.

MANUFACTURER'S DATA

Absorbed

Normal

3/4

65

90/6

Sea level

85 dB(A) @ 1m

-14.1

1

IIB

IEC

T4

37

1/2N'plate

rating





1 Manufacturer

2 Type

3 Model

4



7 Efficiency %



10 Capacity Equipment speed rpm




14



17 SPL (Note 1) 31.5 63 125 250 500 1000 2000 4000 8000

18 85

19

20

21


23

24



27 SUPPLIER'S DATA


29 (Note 1) 31.5 63 125 250 500 1000 2000 4000 8000

30

31

32

33

34

35 Guaranted SPL



38

39

40


42

43

44



47 level (Note 1) 31.5 63 125 250 500 1000 2000 4000 8000

48

49

50

51


53

54




58 Remarks:

59

60

R

E

V


Att #2


P & ID

30-R-A01-32-002, Rev. 4 General Notes, Symbols and Abbreviations

30-R-A01-32-003, Rev. 3 Instrument Symbols and

31-R-B01-32-201C, Rev. 3 P & ID for LP LNG Pumps for TK-201









30-R-B01-32-005, Rev. 1 P & ID for Piping Details II (3 sheets)

30-R-A06-32-150, Rev. 5 P & ID for Unloading Line Drain Drum D-102

30-R-B05-32-340, Rev. 5 P & ID for Process Area Drain Drum D-305

30-R-A01-32-A01, Rev. 4 P & ID for Piping Details I

Column Drawing for LP LNG Pumps

For TK-201 / 202 / 203 / 204

30-M-B01-19-801, Rev. 1 Details of Pumpwell Internal Pipe 1 (M1, M2, M3)


For TK-205 / 206 / 207



Engineering Drawing for LNG Drain Pumps

30-M-A09-18-004, Rev. 0 Unloading Line Drain Drum D-102

30-M-B05-18-005, Rev. 0 Process Area Drain Drum D-305

Att #3


Piping Material Specifications

Class 1R1J for LNG, NG, LN2

Class 3R1J for LNG, NG

Class 1P1 For FG, NI, BC, DO

Instrumentation Specifications

30-I-O00-SP-205, Rev. 1 Instrument General Specification

Electrical Specifications

30-E-E00-SP-242, Rev. 0 Technical Specification for Squirrel Cage Induction Motor

(for Cryogenic Type)

KOGAS Standard Specification

- Detail Work Procedure of 3rd Party Inspector

- Inspection Results Report by 3rd Party (for Sample)

- Usage of Vendor Prints Information System

CLIENT : KOGASLOCATION : SAMCHEOK, KOREAPROJECT : SAMCHEOK LNG TERMINAL

PIPING MATERIALSPECIFICATION

JOB NO. : 080228PAGE : 6

CLASS

1R1J

SERVICELNG,NG,LN2

DESIGN TEMPERATURE-196˚C TO 65˚C

DESIGN PRESSURE(gauge) : ㎫(kg/㎠)1.77 (18 ) DAEWOO ENGINEERING COMPANY

RATINGASME CLASS 150, RF

CORROSION ALLOWANCE0.0 MM

MATERIAL304SS

BRANCH CHARTSTD-P-004

ITEM SIZE(NPS)SCH/

CLASSENDS DESCRIPTION REMARK

PIPE1/2 -1 1/2

2 -34 -6

8 -2426 -3640 -42

80S40S10S10S10

STD

PEBEBEBEBEBE

A312-TP304, SMLSA312-TP304, SMLSA312-TP304, SMLSA312-TP304, EFW, W/100 % RTA358-304 CL.1,EFWA358-304 CL.1,EFW

NIPPLESNIPPLENIPPLE

SWAGE (CON,ECC)

1/2 -1 1/21/2 -1 1/2

1/2 -2

80 S80 S80 S

PBEPOE/TOEBLE/PSE

A312-TP304, SMLS, 100MMA312-TP304, SMLS, 100MMA403-WP304-S, MSS SP-95

FITTINGS90 ELL45 ELL

TEEFULL COUPLING

SOCKOLETSPECIAL COUPLING

CAPCAP

PLUGREDUCING INSERT

90 ELL45 ELL

TEEREDUCER (CON)REDUCER (ECC)

CAP90 ELL45 ELL


ELLIPTICAL HEAD

1/2 -1 1/21/2 -1 1/21/2 -1 1/21/2 -1 1/21/2 -1 1/21/2 -1 1/21/2 -1 1/21/2 -1 1/21/4 -1/41/2 -1 1/22 -122 -122 -122 -122 -122 -3014 -4214 -4214 -4214 -4214 -4232 -42

3000LB3000LB3000LB3000LB3000LB3000LB3000LB3000LB

3000LBSAME AS PIPE

''''''''''''''''''''

SAME AS PIPE

SWSWSWSWSWSWSW

THRDTHRD

SWBWBWBWBWBWBWBWBWBWBWBWBW

A182-F304, ASME B16.11A182-F304, ASME B16.11A182-F304, ASME B16.11A182-F304, ASME B16.11A182-F304, MSS SP-97A182-F304, ASME B16.11,FOR THERMOWELLA182-F304, ASME B16.11A182-F304, ASME B16.11A182-F304, ROUND HEAD,ASME B16.11A182-F304, MSS-SP-79A403-WP304-S, ASME B16.9A403-WP304-S, ASME B16.9A403-WP304-S, ASME B16.9A403-WP304-S, ASME B16.9A403-WP304-S, ASME B16.9A403-WP304-S, ASME B16.9A403-WP304--WX, ASME B16.9A403-WP304--WX, ASME B16.9A403-WP304--WX, ASME B16.9A403-WP304--WX, ASME B16.9A403-WP304--WX, ASME B16.9A240-304, (2:1 AXIS RATIO)

TEE: REFER TO STD-P-004SPECIAL COUPLING: REFER TO

STD-P-007

VALVESGATEGATE

GLOBEGLOBEGLOBE

PISTON CHECKSWING CHECK

NON SLAM CHECKWAFER CHECK

BUTTERFLYBALL

BALL

BALLBALL

2 -46 -24

1/2 -1 1/22 -46 -10

1/2 -1 1/22 -242 -242 -248 -42

1/2 -1 1/2

1/2 -1 1/2

2 -46 -10

150LB150LB800LB150LB150LB800LB150LB300LB300LB150LB800LB

800LB

150LB150LB

BWBWSWBWBWSWBWRFRFBWSW

SW

BWBW

SS BODY(CF3) 316 SS TRIM, STELSS BODY(CF3) 316 SS TRIM, STEL, G.OSS BODY(A182-F304L) 316 SS TRIM .STELSS BODY(CF3) 316 SS TRIM, STELSS BODY(CF3) 316 SS TRIM, STEL G.OSS BODY&COVER (A182-F304L), 316 SS TRIM,STEL,H OR VSS BODY&COVER (CF3) 316 SS TRIM, STEL H OR VSS BODYW/ 316 SS TRIM, STEL H OR VSS BODYW/ 316 SS DISC/ST, DUAL PLT H OR VSS BODY (CF3) TOP INSPECTION PORT,G.OSS BODY (A182-F304L), 316 SS TRIM, Kel-F STW/ 2 PBE NIPPLESSS BODY (A182-F304L), 316 SS TRIM, Kel-F STW/ PBE,POE/TOE NIPPLESSS BODY (CF3) 316 SS TRIM, Kel-F ST.SS BODY (CF3) 316 SS TRIM, Kel-F ST. G.O

WAFER CHECK SHALL BE USED ONLY WHERE SHOWN ON P&ID

FOR INST.

FLANGESSOCKET WELD

WELD NECKBLIND

WELD NECKBLIND

1/2 -1 1/22 -241/2 -2426 -4226 -42

300LB300LB300LB300LB300LB

RFRFRFRFRF

A182-F304, ASME B16.5, 125 AARHA182-F304, ASME B 16.5 125 AARHA182-F304, ASME B16.5, 125 AARHA182-F304, MSS-SP-44, 125 AARHA182-F304, MSS-SP-44, 125 AARH

GASKETSGASKETGASKET

1/2 -2426 -42

300LB300LB

RFRF

SW(316+GRAP),CENTER RING: 316SS,4.5MMSW(316+GRAP),CENTER RING: 316SS,4.5MM MSS-SP-44

BOLTINGSTUD BOLTSSTUD BOLTS

1/2 -2426 -42

300LB300LB

RFRF

A320-B8M CL.2/A194-8MAA320-B8M CL.2/A194-8MA ,MSS-SP-44

MISCELLANEOUSFIGURE 8

SPACERCIRCULAR BLANK


1 -1 1/21 -241 -2426 -4226 -42

300LB300LB300LB300LB300LB

RFRFRFRFRF

A240-304, 125 AARH,API-590A240-304, 125 AARH,API-590A240-304, 125 AARH,API-590A240-304, 125 AARH,STD-P-016,MSS-SP-44A240-304, 125 AARH,STD-P-016,MSS-SP-44

SAFTY SYSTEM 에서

FIGURE 8 이용

NOTE : 1.26" & LARGER SHALL BE USED MSS-SP-44(ASME B16.47 SERIES A) FLANGES.

2. INSPECTION/EXAMINATION/TESTING SHALL BE EXECUTED IN SEVERE CYCLIC CONDITION ACCORDING TO CHAP.Ⅵ OF ASME B31.3.3. EXTERNAL COATING FOR U/G PIPING SHALL BE PERFORMED IN ACCORDANCE WITH G01-SP-008.(PIPE, FITTING, FLANGE, WELDING POINT )



JOB NO. : 080228PAGE : 7

CLASS

3R1J

SERVICELNG,NG

DESIGN TEMPERATURE-196˚C TO 38˚C

DESIGN PRESSURE(gauge) : ㎫(kg/㎠)1.86 (19) DAEWOO ENGINEERING COMPANY



MATERIAL304SS


ITEM SIZE(NPS)SCH/


PIPE1/2 -1 1/2

2 -34 -68 -12

80S40S10S10S

PEBEBEBE

A312-TP304, SMLSA312-TP304, SMLSA312-TP304, SMLSA312-TP304,EFW,W/100% RT

NIPPLESNIPPLENIPPLE

SWAGE (CON,ECC)

1/2 -1 1/21/2 -1 1/2

1/2 -2

80 S80 S80 S

PBEPOE/TOEBLE/PSE

A312-TP304, SMLS, 100MMA312-TP304, SMLS, 100MMA403-WP304-S, MSS SP-95

FITTINGS90 ELL45 ELL

TEEPLUG

FULL COUPLINGSOCKOLET

SPECIAL COUPLINGCAPCAP

REDUCING INSERTUNION (GJ)

90 ELL45 ELL


CAP

1/2 -1 1/21/2 -1 1/21/2 -1 1/21/4 -1/41/2 -1 1/21/2 -1 1/21/2 -1 1/21/2 -1 1/21/2 -1 1/21/2 -1 1/21/2 -1 1/22 -122 -122 -122 -122 -122 -12

3000LB3000LB3000LB

3000LB3000LB3000 LB3000LB3000LB3000LB3000LB

SAME AS PIPE''''''''

SAME AS PIPE

SWSWSW

THRDSWSWSWSW

THRDSWSWBWBWBWBWBWBW

A182-F304, ASME B16.11A182-F304, ASME B16.11A182-F304, ASME B16.11A182-F304, ROUND HEAD,ASME B16.11A182-F304, ASME B16.11A182-F304, MSS-SP-97A182-F304, ASME B16.11,FOR THERMOWELLA182-F304, ASME B16.11A182-F304, ASME B16.11A182-F304, MSS-SP-79A182-F304, INTEGRAL SEATA403-WP304-S, ASME B16.9A403-WP304-S, ASME B16.9A403-WP304-S, ASME B16.9A403-WP304-S, ASME B16.9A403-WP304-S, ASME B16.9A403-WP304-S, ASME B16.9


STD-P-007

VALVESGATEGATE

GLOBEGLOBEGLOBE

PISTON CHECKSWING CHECK

BUTTERFLYBALL

BALL

BALLBALL

2 -46 -12

1/2 -1 1/22 -46 -12

1/2 -1 1/22 -128 -12

1/2 -1 1/2

1/2 -1 1/2

2 -46 -12

300 LB300 LB800 LB300 LB300 LB800 LB300 LB300 LB800 LB

800 LB

300 LB300 LB

BWBWSWBWBWSWBWBWSW

SW

BWBW

SS BODY(CF3) 316 SS TRIM, STELSS BODY(CF3) 316 SS TRIM, STEL, G.OSS BODY(A182-F304L) 316 SS TRIM STELSS BODY(CF3) 316 SS TRIM, STELSS BODY(CF3) 316 SS TRIM, STEL G.OSS BODY&COVER (A182-F304L), SS 316 TRIM,STEL,H OR VSS BODY&COVER (CF3) 316 SS TRIM, STEL H OR VSS BODY (CF3) TOP INSPECTION PORT,G.OSS BODY (A182-F304L), 316 SS TRIM, Kel-F STW/ 2 PBE NIPPLESSS BODY (A182-F304L), 316 SS TRIM, Kel-F STW/ PBE,POE/TOE NIPPLESSS BODY (CF3) 316 SS TRIM, Kel-F ST.SS BODY (CF3) 316 SS TRIM, Kel-F ST. G.O

FOR INST

FLANGESSOCKET WELD

WELD NECKBLIND

1/2 -1 1/22 -121/2 -12

300 LB300 LB300 LB

RFRFRF

A182-F304, ASME B16.5, 125 AARHA182-F304, ASME B16.5, 125 AARHA182-F304, ASME B16.5, 125 AARH

GASKETSGASKET 1/2 -12 300LB RF SW(316+GRAP),CENTER RING: 316SS,4.5MM

BOLTINGSTUD BOLTS 1/2 -12 300LB RF A320-B8M CL.2/A194-8MA

MISCELLANEOUSFIGURE 8SPACERCIRCULAR BLANK

1 -1 1/22 -122 -12

300LB300LB300LB

RFRFRF

A240-304, 125 AARH,API-590A240-304, 125 AARH,API-590A240-304, 125 AARH,API-590

SAFTY SYSTEM 에서

FIGURE 8 이용

NOTE : 1. 26" & LARGER SHALL BE USED MSS-SP-44(ASME B16.47 SERIES A) FLANGES.

2. INSPECTION/EXAMINATION/TESTING SHALL BE EXECUTED IN SEVERE CYCLIC CONDITION ACCORDING TO CHAP.Ⅵ OF ASME B31.3.



JOB NO. : 080228PAGE : 1

CLASS

1P1

SERVICEFG,NI,BC,DO

DESIGN TEMPERATURE-29˚C TO 75˚C MAX

DESIGN PRESSURE(gauge) : ㎫(kg/㎠)FG, NI:0.98(10) DO, FO:1.37(14) DAEWOO ENGINEERING COMPANY



MATERIALCS


ITEM SIZE(NPS)SCH/


PIPE1/2 -1 1/2

2 - 68 -16

XSSTDSTD

PEBEBE

A53-B, SMLSA53-B, SMLSA53-B,ERW, W/100% RT

NIPPLESNIPPLENIPPLE

SWAGE (CON,ECC)

1/2 -1 1/21/2 -1 1/2

1/2 -2

160160XS

PBEPOE/TOEBLE/PSE

A53-B,SMLS, 100MMA53-B,SMLS, 100MMA234-WPB-S, MSS SP-95

FITTINGS90 ELL45ELL

TEEPLUG

FULL COUPLINGSOCKOLET

SPECIAL COUPLINGCAPCAP

REDUCING INSERTUNION (GJ)

90 ELL45 ELL


CAP90 ELL45 ELL


1/2 -1 1/21/2 -1 1/21/2 -1 1/21/4 -1/4

1/2 -1 1/21/2 -1 1/21/2 -1 1/21/2 -1 1/21/2 -1 1/21/2 -1 1/21/2 -1 1/2

2 -142 -142 -142 -142 -142 -1616 -1616 -1616 -1616 -1616 -16

3000 LB3000 LB3000 LB

3000 LB3000 LB3000 LB3000 LB3000 LB3000 LB3000 LB

SAME AS PIPE''

''''''''''''''''

SAME AS PIPE

SWSWSW

THRDSWSWSWSW

THRDSWSWBWBWBWBWBWBWBWBWBWBWBW

A105, ASME B16.11A105, ASME B16.11A105, ASME B16.11A105, ROUND HEAD, ASME B16.11A105, ASME B16.11A105, MSS SP-97A105, ASME B16.11,FOR THERMOWELLA105, ASME B16.11A105, ASME B16.11A105, MSS SP-79A105, INTEGRAL SEAT, MSS SP-83A234-WPB-S, ASME B16.9A234-WPB-S, ASME B16.9A234-WPB-S, ASME B16.9A234-WPB-S, ASME B16.9A234-WPB-S, ASME B16.9A234-WPB-S, ASME B16.9A234-WPB-W, ASME B16.9, W/100% RTA234-WPB-W, ASME B16.9, W/100% RTA234-WPB-W, ASME B16.9, W/100% RTA234-WPB-W, ASME B16.9, W/100% RTA234-WPB-W, ASME B16.9, W/100% RT


STD-P-007

VALVESGATEGATEGATEGATE

GLOBEGLOBEGLOBE

PISTON CHECKWAFER CHECK

BALLBALLBALLBALL

1/2 -1 1/21/2 -1 1/2

2 -46 -16

1/2 -1 1/22 -46 -16

1/2 -1 1/22 -16

1/2 -1 1/21/2 -1 1/2

2 - 46 -16

800 LB800 LB150 LB150 LB800 LB150 LB150 LB800 LB150 LB800 LB800 LB150 LB150 LB

SWT/SW

RFRFSWRFRFSWRFSWSWRFRF

CS BODY W/ F6 (13 CR) TRIMCS BODY W/ F6 (13 CR) TRIMCS BODY W/ F6 (13 CR) TRIMCS BODY W/ F6 (13 CR) TRIM, G.O.CS BODY W/ F6 (13 CR) TRIMCS BODY W/ F6 (13 CR) TRIMCS BODY W/ F6 (13 CR) TRIM, G.OCS BODY W/ F6 (13 CR) TRIM, H OR VCS BODY W/ 410 SS DISC/ST, DUAL PLT, H OR VCS BODY W/ 316 SS B&S PTFE ST W/2 PBE NIPPLESCS BODY W/ 316 SS B&S PTFE ST W/PBE,POE/TOE NIPPLESCS BODY W/ 316 SS B&S PTFE STCS BODY W/ 316 SS B&S PTFE ST, G.O.

FOR DO,BC INST

FOR NI,FG INST,D&V

FLANGESSOCKET WELD

BLINDWELD NECK

SOCKET WELDWELD NECK

1/2 -1 1/21/2 -162 -16

1/2 -1 1/22 -16

150 LB150 LB150 LB300 LB300 LB

RFRFRFRFRF

A105, ASME B16.5, STD FINA105, ASME B16.5, STD FINA105, ASME B16.5, STD FINA105, ASME B16.5, STD FINA105, ASME B16.5, STD FIN NOTE 2

GASKETS1/2 -16 150 LB RF 1.6MM COMPRESSED GRAPHITE

BOLTINGSTUD BOLTS 1/2 -16 150 LB RF A193-B7/A194-2H

MISCELLANEOUSFIGURE 8


2 -1214 -1614 -16

150 LB150 LB150 LB

RFRFRF

A516-70, STD FIN,API-590A516-70, STD FIN,API-590A516-70, STD FIN,API-590

NOTE: 1. EXTERNAL COATING FOR U/G PIPING SHALL BE PERFORMED IN ACCORDANCE WITH G01-SP-008.(PIPE, FITTING, FLANGE, WELDING POINT)2. 300 LB RF FLANGES SHALL BE USED ONLY FOR SPEC BREAK POINTS WITH 1R1J CLASS AND IN THIS CASE, GASKETS & BOLT/NUTS OF 1R1J CLASS

SHALL APPLIED TO THE SPEC BREAK POINTS.

1 02/07/12 REVISED AS MARKEDC.M.KIM

M.S.KANGY.S.KIM N/A

0 07/15/09 FOR CONSTRUCTIONK.H.SEO / D.S.KIM

M.S.KANGY.S.KIM N/A

A 05/22/09 FOR APPROVALK.H.SEO / D.S.KIM

M.S.KANGY.S.KIM N/A

REV. DATE DESCRIPTIONDESIGN

APPROVEDCLIENT

APPROVEDCHECK Q.A

KOREA GAS CORPORATION

삼척생산기지 1단계 본설비 실시설계 및 감리기술용역SAMCHEOK LNG TERMINAL PROJECT

INSTRUMENT GENERAL SPECIFICATION

SCALE JOB NO. PHASE DOCUMENT NO. REV.

NONE 080228 I 30-I-O00-SP-205 1

POSCO ENGINEERING Co., Ltd.

30-I-O00-SP-205

- 1 -

TABLE OF CONTENTS

1.0 INTRODUCTION

2.0 GENERAL REQUIREMENTS

2.1 Units of measurement

2.2 Selection of ranges

2.3 Instrument electrical supply

2.4 Instrument air supply

2.5 Signal transmission

2.6 Instrument cables

2.7 Electrical safety in hazardous areas

2.8 Instrument nameplates

2.9 Instrument finish

2.10 Environmental conditions

2.11 Radio frequency interference (RFI)

2.12 Transmitter local indicators

2.13 Diaphragm seals

3.0 INSTRUMENTS PANELS

4.0 FLOW INSTRUMENTS

4.1 General

4.2 Flow rate measurement

4.3 Volume measurement

4.4 Sizing of differential pressure type flow meters

4.5 Orifice plates

4.6 Venturi tubes

4.7 Flow meter installation

4.8 Vortex flow meters

4.9 Turbine meters

4.10 Variable-area flow meters

4.11 Electromagnetic flow meters

4.12 Ultrasonic flowmeter

4.13 Ancillary equipment

5.0 LEVEL INSTRUMENTS

5.1 General

5.2 Gauge glasses

5.3 Differential pressure level instruments

5.4 Level switches

5.5 Ultrasonic Type Level Instruments

5.6 Guided Wave Radar Type

5.7 Connection sizes and rating

30-I-O00-SP-205

- 2-

6.0 PRESSURE INSTRUMENTS

6.1 General

6.2 Pressure gauges

6.3 Pressure transmitters

6.4 Pressure switches

7.0 TEMPERATURE INSTRUMENTS

7.1 General

7.2 Thermowells

7.3 Resistance temperature detectors (RTD)

7.4 Thermocouples

8.0 CONTROL VALVES

8.1 General

8.2 Valve type and size

8.3 Other requirements

9.0 ELECTRICAL PARAMETERS

10.0 MACHINE MONITORING

11.0 RELEVANT STANDARDS AND CODES OF PRACTICE

ATTACHMENT

#1 : CONCENTRIC SHARP EDGED ORIFICE PLATE TYPICAL DIMENSIONS

#2-1 : STANDARD CONSTRUCTION OF A 1" SOCKET WELDED THERMOWELL

(FOR NON-INSULATED PIPE LINE)

#2-2 : STANDARD CONSTRUCTION OF A 1" SOCKET WELDED THERMOWELL

(FOR INSULATED PIPE LINE)

#2-3 : STANDARD CONSTRUCTION OF A 1" , 1-1/2" & 4” FLANGED

THERMOWELL

#3 : TYPICAL INSTRUMENT AIR SUPPLY

30-I-O00-SP-205

- 3-

1.0 INTRODUCTION

The purpose of this document is to define the basic technical requirements for the

selection and installation of instruments for process applications, utilities, etc., for the

Samcheok LNG Terminal.

Details of the control, monitoring and shutdown systems shall be described elsewhere.

2.0 GENERAL REQUIREMENTS

2.1 UNITS OF MEASUREMENT

The following abbreviations shall be used ;

APPLICATION UNIT ABBREVIATIONS

Piping Inch ˝ Length Meter M

Millimeter MmArea Square meter m

2

Volume/Capacity Cubic meter m3

Time Second SMinute MinHour HDay D

Velocity Meters / second m/sAcceleration Meter / square second m/s

2

Mass Kilogram KgTon T

Flow rates- Mass Kilograms / second kg/s

Kilograms / hour kg/h- Volumetric Cubic meter / hour

Ton / hourm

3/h

t/hSound level Decibel dBaDensity Kilograms / cubic meter kg/m

3

Pressure- Barometric Pascal, Kilopascal Pa, kPa- Fluid Pascal, Kilopascal, Megapascal Pa, kPa, MPaTemperature Kelvin K

Degree centigrade ℃

Energy- Electrical Kilowatts. hour KW.h- Mechanical Joule, Kilojoule, Megajoule J, kJ, MJ- Thermal Joule, Kilojoule, Megajoule J, kJ, MJHeat capacity Joule per Kelvin J/KHeat flow Kilocalories per hour. Square meter Kcal/h.m

2

Heat transfer coefficientWatts/(Square meter. Kelvin) W/(m

2.K)

Watts/(Square meter. DegreeCentigrade)

W/(m2.℃)

Viscosity Pascal. second Pa.sCurrent Amperes A

Milliampere mAPower Watts W

Kilowatts kWVoltage Volt V

Kilovolts kVFrequency Hertz HzElec. Resistance Ohm Ω Elec. Conductance Siemens S

30-I-O00-SP-205

- 4-

Level Percent %Meter MMillimeter Mm

2.2 SELECTION OF RANGES

Unless otherwise specified, the instrument ranges shall be selected such that the

normal value will be between 50 and 75 percent of scale length, taking into account

the specified minimum and maximum values.

For trip functions the instrument ranges shall be selected such that the process trip

value will be between 25 and 75 percent of the transmitter output range.

2.3 INSTRUMENT ELECTRICAL SUPPLY

The available electrical power supply to instrument systems is 115 V AC 60 Hz, no

break (UPS).

Field instruments will generally be 24 V DC powered. For special cases where field

instrumentation require a separate supply the 115 V AC UPS should be used.

2.4 INSTRUMENT AIR SUPPLY

The instrument air compressors and dryers shall be provided by the mechanical

department.

Instrument air shall be clean, dry and oil free.

Normal operating pressure of the instrument distribution system shall be 0.65 MPa,

with a minimum/maximum operating pressure of 0.4 / 0.8 MPa.

The main instrument air header distribution ring main will be provided by piping (2"+).

The ring main will be provided with plugged 1" valves, where Instrument engineering

starts.

From the valve on the ring main, 1" branching to 3/4" galvanised carbon steel pipe and

fittings (screwed type) shall be used, down to local instrument level. Individual 1/2"

galvanised carbon steel pipe supply lines, terminating in 1/2" N.P.T. valves, shall be

provided for each instrument air consumer from the local 3/4" pipe runs. From the 1/2"

valve to the final instrument connection 1/2" or 1/4" stainless steel tube (dependant on

consumer), with stainless steel fittings, shall be used (See attachment 3).

Each instrument air user shall be fitted with an air filter, pressure regulator and

pressure gauge. Where the air user requires lubricators to be fitted, e.g. piston

actuators, these shall be fitted after the regulator and will allow refilling of oil during

operation.

30-I-O00-SP-205

- 5-

2.5 SIGNAL TRANSMISSION

2.5.1 General

Analogue transmission shall apply electric signals (2.5.2) or pneumatic signals (2.5.3).

Electric signal transmission should be used for all remote control and shutdown

functions. Pneumatic signal transmission will only be used for local control loops and

final element control.

Local pneumatic control loops should be avoided, unless specifically required for a

particular application e.g. vendor packages.

Control valves will be pneumatically operated unless specified otherwise.

Where pneumatic as well as electric signal transmission is applied (e.g. control valve),

smart E/P positioner shall be provided.

2.5.2 Electric Signal Transmission

The analogue signal transmission range should normally be 4 to 20 mA DC.

The voltage level for signal transmission should normally be 24 VDC.

The signal transmission should normally be a 2 wire system (powered by receiving

devices).

Instrumentation for special purposes, such as for machine monitoring, tank gauging

systems, fire and gas detectors, etc. may have other signal ranges, signal

transmission voltage levels and multiple wire systems.

Signals from thermocouples and resistance thermometers fitted to a package or in a

control loop shall be converted to 4 to 20 mA DC, in the field at the measuring device

or local to it, other signals will be run directly.

Electric signal transmitter shall be supplied smart with hart protocol type as “Duon or

equivalent”.

2.5.3 Pneumatic Signal Transmission

The operating range for pneumatic signal transmission shall be 0.02 to 0.1 MPa.

The length of tubing shall be as short as possible. A tubing size of 1/4” with 0.035” well

thickness shall be used, up to a maximum length of 200 m, for small volume devices

e.g. receiving bellows.

When the length of the signal line between a pneumatic controller and control valve

exceeds 75 metres, the tubing shall end in a device of small volume, for instance a

valve positioner. Volume boosters should not be used.

30-I-O00-SP-205

- 6-

2.5.4 Process Impulse Line

Annealed seamless stainless steel(316SS) tube of 1/2” with 0.049” wall thickness and

316SS compression tube fitting with double ferrules.

2.6 INSTRUMENT CABLES

In general all cables shall have copper conductors with the following minimum

conductor sizes:

a) 1.5 mm2 for single paired cable

b) 1.5 mm2 for multipaired cable

c) 1.5 mm2 for single triple cable

d) 1.5 mm2 for multitriple cable

e) 2.5 mm2 for cored cable

f) 2.5 mm2 for multicored cable

g) 4.0 mm2 for cored cable

h) 4.0 mm2 for multicored cable

i) 6.0 mm2 for cored cable

For higher load, remote instrumentation (e.g. solenoid valves, alarm horns, etc.,)

voltage drop calculations should be performed for the worst case distances, to ensure

adequate operating voltage at the instrument. If insufficient operating voltage either

larger conductor sizes or higher voltage devices (e.g. 115 VAC solenoids) should be

considered.

Cables and wires shall not be affected by humidity, every kind of harmful insect, vermin,

fungi and the like and shall be suitable for service at the climatic conditions at site.

All necessary precautions shall be taken to prevent the capacitive effects on control

circuits.

In general, the following types of cables shall be used in all areas:

a. Analogue signals

: 600/1000 volt grade, multipair/triple/quad, flame retardant, PVC insulated with

PVC outer sheath to IEC or equivalent (CVVS type). An overall copper tape,

with drain wire, shall be installed around all pairs below the PVC outer sheath.

The cable shall be approved by vertical tray flame test (KSC 3341, IEEE383 or

equivalent)

b. Digital signals

: 600/1000 volt grade, multicore, flame retardant, PVC insulated with PVC outer

sheath to IEC or equivalent (CVV type).


equivalent)

30-I-O00-SP-205

- 7-

c. Thermocouples

: Compensating extension wire with error limit +/-2.5 (-20 ~ 100) oC, total

resistance 0.8 ohm/metre, multipair, flame retardant, PVC insulated with PVC

outer sheath to IEC or equivalent. Each pair of cores shall have a copper tape

shield and an overall copper tape, with drain wire, shall be installed around all

pairs below the PVC outer sheath.


equivalent)

d. Grounding cables

: 450/750 volt grade, PVC insulated sheath to IEC or equivalent.

(minimum 4.0 mm2)

The current carrying capacity of cables shall consider derating for group factor, thermal

resistivity, depth of laying and a ground temperature factor.

The cable outersheath and core colour & identification shall be as follows:

CABLECONDUCTOR

SIZE (mm2)

CORE COLOURS OUTER SHEATH COLOUR

2 CORE 2.5, 4.0 & 6.0 RED / WHITE BLUE

4 CORE 2.5RED / WHITE / BLUE /

GREENBLUE

MULTICORE 2.5 & 4.0BLACK (No. ON EACH

CORE)BLUE

1 PAIR 1.5 RED / WHITE BROWN

MULTIPAIR 1.5 RED / WHITE

(No. ON EACH PAIR)BROWN

1 PAIR - K TC 1.5 WHITE / RED BLUE

MULTIPAIR – K

TC1.5 WHITE / RED

(No. ON EACH PAIR)BLUE

1 TRIPLE 1.5 RED / WHITE / BLUE BROWN

MULTITRIPLE 1.5 RED / WHITE / BLUE

(No. ON EACH TRIPLE)BROWN

1 QUAD 1.5RED / WHITE / BLUE /

GREENBROWN

MULTI QUAD 1.5

RED / WHITE / BLUE /

GREEN

(No. ON EACH TRIPLE)

BROWN

30-I-O00-SP-205

- 8-

The colour of earthing cables outer sheath shall be for:

Safety (dirty) earth - green

Instrument (clean) earth - green

The following multicore/pair/triple/quad sizes shall be used:

Multicore: 2 core; 4 core; 7 core; 12 core; 16 core; 24 core; 36 core; 50 core

Multipair: 2 pair; 4 pair; 8 pair; 12 pair; 16 pair; 24 pair; 36 pair

Multitriple: 2 triple; 4 triple; 9 triple; 12 triple; 16 triple

Multiquad: 8 quad; 12 quad; 16 quad

2.7 ELECTRICAL SAFETY IN HAZARDOUS AREAS

In order to prevent electrical equipment from becoming a source of ignition in

potentially flammable gas atmospheres, protective measures shall be taken, based on

the hazardous area classification of the particular area in which the electrical

equipment is being installed. The requirements of IEC-60079 shall be applied.

The Vendor shall submit the IEC Ex Certification, equipment test report and

QAR(Quality Assessment Report) etc to KOSHA (Korean Occupational Safety &

Health Agency) or KGS (Korean Gas Safety Corporation) or KTL (Korean Testing

Laboratory) for explosion proof type electrical equipment and instruments.

The preferred principal of protection will be explosionproof - Ex’d’, although for

equipment where this is not available or alternative methods of protection are

preferable, other types of certification will be considered e.g. increased safety - Ex ‘e’;

non-incendive - Ex ‘n’; intrinsically safe - Ex ‘ia’ or’ ib’.

2.8 INSTRUMENT NAMEPLATES

2.8.1 General

All instruments, junction boxes, cabinets, panels and ancillary equipment shall be

provided with nameplates indicating the tag number only or the tag number and

service description.

All descriptions will be in the English or Korean language

2.8.2 Field Mounted Nameplates

All plant-mounted instruments, e.g. transmitters, gauges, converters, control valves,

solenoid valves, etc. shall be provided with nameplates indicating the tag number and

service description.

Field-mounted junction boxes shall be provided flameproof - Exd with nameplates

indicating the tag number. In case of junction boxes with I.S. circuits, the flameproof -

Exd shall be provided and a blue label engraved ‘I.S.’ shall also be provided.

30-I-O00-SP-205

- 9-

The nameplates shall be fixed to the mounting plate, the mounting bracket, the

junction box door/cover or suitable steel work, local to the instrument position, with

stainless steel M4 bolts and nuts, self-tapping screws or pop-rivets.

The material of the nameplate should be laminated plastic, white/black, except for I.S.

junction boxes which will be blue/white.

In addition to the nameplate located by the instrument mounting, all plant-mounted

instruments shall be provided with a stainless steel tag plate securely fixed to the

instrument with stainless steel self-tapping screws, pop-rivets or wire.

Fixing arrangements for nameplates shall not adversely affect any type of instrument

protection (i.e. IP rating or hazardous area certification).

2.8.3 Nameplates for Indoor Use

All panel-mounted instruments shall be provided with nameplates, indicating tag

number, in accordance with the manufacturer's standard.

Nameplates for panel-mounted ancillary equipment such as switches, indicating lights,

etc., shall be sized to suit the particular application.

2.9 INSTRUMENT FINISH

The finish of plant-mounted instruments should be in the manufacturer's standard

colour, except red and yellow, which shall be used for shutdown, protection and safety

related equipment only. The finish shall be suitable for the specified environmental

conditions.

2.10 ENVIRONMENTAL CONDITIONS

The plant-mounted instruments shall be suitable for operation in a humid, saliferous

and corrosive atmosphere and be adequately protected against causing an explosion.

For the environmental conditions at Samcheok terminal refer to Project Data.

Instrument enclosure's "degree of protection" shall be in accordance with IEC 60529.

The minimum degree of protection for field mounted instruments shall be IP 65 or

equivalent with suitable corrosion protection and for internally mounted instruments

and cabinets shall be IP22.

2.11 RADIO FREQUENCY INTERFERENCE (RFI)

The requirements of IEC 60801 shall apply. For portable radio transmitters/ receivers

which have an electromagnetic field strength of 10 mV in the frequency range between

100 kHz and 1,000 MHz the total effect of the radio frequency interference effect shall

be equal to or less than +/-0.1 % of the output span with the instrument enclosure

30-I-O00-SP-205

- 10-

(cover) in place and equal to or less than +/-0.5 % of the output span with the

instrument enclosure (cover) removed.

2.12 TRANSMITTER LOCAL INDICATORS

Smart type transmitters using hart protocol for signal transmission with integral digital

indicators shall be used. If a transmitter output indication is required to be read from a

control valve, care should be taken in using the integrally-mounted indicators to ensure

that they can be read from the relevant location, if it is not possible separate digital

local indicators should be used.

All local indicators shall have a scale calibration as follows:-

Flow* Actual range (t/h or kg/h)

Level Actual range (%, m, mm)

Pressure Actual range

Temperature Actual range

Other variables Actual range

2.13 DIAPHRAGM SEALS

Diaphragm seals shall normally be integral with the instrument. The application of

diaphragm seals with capillary extensions shall be kept to an absolute minimum.

When a diaphragm seal is required, the largest practical size should be applied.

Special coating materials may be considered where these will improve the corrosion

resistance of the diaphragm. The capillary tubing material shall be of 316 stainless

steel and be shielded by flexible stainless steel tubing with a neoprene or PVC cover,

according to manufacturer's standard.

The length of the capillary tubing shall suit the application, but the length should be at

least 5.0 metre. For differential pressure applications the capillary tubes shall be of the

same length.

The maximum and minimum allowable operating temperature for liquid-filleddiaphragms shall be observed.

3.0 INSTRUMENTS PANELS

For the basic requirements of instrument panels located locally and in equipment

rooms see the “General Panel & Wiring Specification (30-I-O00-SP-207)”.

30-I-O00-SP-205

- 11-

4.0 FLOW INSTRUMENTS

4.1 GENERAL

Differential Pressure (DP) type flowmeters or vortex flowmeters will form the basis of

most of the flow measuring activities in the KOGAS Samcheok LNG Terminal. However,

other types of meter may be considered for certain duties.

The basis for the design of differential pressure-type flowmeters is the publication ISO

5167-1~4, 'Measurement of fluid flow by means of orifice plates, nozzles and Venturi

tubes inserted in circular cross-section conduits running full'.

Where a flow measurement is to be used in a shutdown as well as an operating

function a single primary element with separate transmitters should be used. i.e. For

an orifice plate, two DP transmitters each with its own set of process connections; for

vortex meters, the same bluff body with two sensors/amplifiers/power supplies.

4.2 FLOW RATE MEASUREMENT

Differential pressure type flow instruments or vortex flowmeters up to 6", should

generally be applied for flow rate measurement. The selection of which type of

instrument to use should be on a cost basis of the complete installation.

Special considerations on particular services may require the use of alternative

methods such as:-

- variable-area flowmeters

- electromagnetic flowmeters

- thermal flowmeters

NOTE: Installation requirements similar to those for differential pressure-type flow

instruments also apply for electromagnetic or vortex flow meters, with regard to

straight length requirements, upstream and downstream of the instrument. Moreover

the supplier’s maximum allowable distance between the flow meter head and the

related electronic converter shall be observed.

The volume corrector shall be supplied with flow meter or flow transmitter in the F/G

line.

4.3 VOLUME MEASUREMENT

Turbine or ultrasonic meters shall be specified when necessary for custody transfer.

They may also be considered for applications where a higher accuracy or a higher

rangeability is required than is obtainable with the flow rate instruments listed.

4.4 SIZING OF DIFFERENTIAL PRESSURE TYPE FLOW METERS

Flow element sizing calculations will be based on ISO 5167-1.

30-I-O00-SP-205

- 12-

The primary elements should be sized for use with differential pressure transmitters

having one of the following preferred ranges: 0-5, 0-12.5, 0-25 or 0-50 all in kPa.

Based on a linearized scale of 0-10, the flowmeter shall be ranged for a reading at:

1) Maximum flow between 8.0 and 9.5 of the scale.

2) Normal flow between 5.0 and 6.0 of the scale.

3) Minimum flow not below 2.0 of the scale for flowmeters used in accounting,

material balancing and alarm or tripping applications.

4) Minimum flow not below 1.0 of the scale for all other applications.

The d/D (Beta) ratio shall be between 0.3 and 0.7. The "top of chart" flow rate shall

generally be chosen as a rounded value conveniently greater than the maximum flow.

The preferred flowmeter range is 0-25 kPa. Ranges above 50 kPa shall not normally

be used.

Where the above requirements are conflicting, two or a maximum of three flowmeters,

having different but overlapping ranges shall be selected.

Square root flow signals shall be linearized in the transmitter not at the systems,

unless the square root signal is required in the system calculations.

4.5 ORIFICE PLATES

The "measurement uncertainty" for an uncalibrated orifice plate flow measurement

loop is +/- 1 to 5% flow, utilising a +/- 0.1% analogue DP transmitter (smart type) and

the straight length requirements specified in ISO 5167-1, within a turndown not

exceeding 4:1.

Orifice plates shall conform with the dimensions and tolerances specified in attachment 1.

Sharp edged, concentric orifice plates should be used. The minimum orifice bore shall

not be less than 12.5 mm diameter.

The minimum pipe size for orifice plates shall be 2". Where the pipe size is less than 2",

it should be increased to 2" for the meter run.

Flange taps shall normally be used. Orifice taps are socket welded or threaded in

accordance with the data sheet. Threaded taps shall be 1/2" NPT. Tap locations for

horizontal lines shall be on the horizontal centre line.

Orifice flanges should be the weld neck type. The Minimum Orifice Flange Rating shall

generally be ANSI Class 300. The use of other rating flanges or facings, other than

raised face, shall be used as required by the piping specifications. The plate surface

finish in the gasket joint area shall be appropriate for the gasket materials, which will

be supplied by the orifice plate manufacturer.

30-I-O00-SP-205

- 13 -

Orifice plates shall include a vent or drain hole when appropriate for the service and

application. e.g. A horizontal line installed orifice in "wet" vapour or saturated steam

service shall have a drain hole. A horizontal line installed orifice in a liquid service

where the liquid may include entrained gas or be close to being dual phase shall have

a vent hole.

Orifice plates in vertical lines shall not have vent or drain holes.

The plate material shall be 316 stainless steel unless other materials are more suitable

or are specified for the intended application.

4.6 VENTURI TUBES

Venturi Tubes or low loss flow tubes shall be considered:

- where high pressure recovery is required,

- where only low inlet pressure is available,

- where extreme high beta ratios would be required with an orifice plate,

- where resistance to abrasion is required ,

- where suspended solids must be passed,

- where meter run space is limited.

4.7 FLOW METER INSTALLATION

Because the pressure measurements are small, DP transmitters on flow service shall

be installed with great care, with the minimum lengths of impulse piping, to prevent

errors affecting the accuracy of the installation.

The possibility of changing and/or different levels (static heads) of liquid occurring in

the high and low pressure legs of the connecting impulse lines shall be prevented.

These problems can particularly occur in cryogenic service, where a build up of ice can

affect the heat transfer rate from impulse lines, so heat tracing on the impulse lines

shall be installed to ensure continuous vaporisation of liquid and hence a consistent

and reliable liquid/vapour interface level (static head) in both impulse connections.

Generally liquid service transmitters shall be mounted below the line with diaphragm

seals and vapour/gas/LNG service transmitter above the line. Where this is not

possible using an alternative flow measurement instrument should be considered,

although there are various solutions that can be considered to over come these

problems, e.g. seal pots.

The installation in pipelines of orifice plates and venturi tubes, shall be in accordance

to ISO 5167-1, with a +/ - 0.5% additional uncertainty value, at a Beta Ratio of 0.7.

Exceptions to these installation recommendations may be necessary or acceptable for:

- High accuracy applications required for accounting or mass balance measurements

where increased lengths may be required.

30-I-O00-SP-205

- 14-

- Costly and awkward piping arrangements created to provide the specified straight

lengths, where by taking account of the Beta Ratio of the actual element if <0.7 a

shorter length, which will simplify the arrangement, can be considered

Straightening vanes shall not be used as a means of decreasing the upstream straight

pipe requirements until every effort has been made to avoid their use, and then only

when the source of upstream flow disturbance is other than that caused by a single

elbow, tee, or reducer. Straightening vanes shall not be used in lines smaller than 3".

Pre-fabricated Meter Tubes shall be supplied where required, which will be identified

on the P&ID's and where a 2" meter run is fitted in a line <2". The meter run shall be

manufactured by a specialty fabricator and the upstream and downstream pipe

between the orifice plate and the nearest fittings shall conform to the tolerances and

practices as recommended by ASME "Fluid Meters".

Flow elements shall be installed upstream of a controlling globe, or throttling gate valve

unless permitted otherwise.

4.8 VORTEX FLOW METERS

Although vortex meters are a higher cost device than an orifice plate the overall

installation costs can be less. Also the rangeability is more than the 3 : 1 of an orifice

plate. Therefore each required installation should be reviewed to determine whether a

vortex meter should be used or not.

Further points for consideration are:

- the maximum allowable operating temperature

- the maximum allowable line size (6" typical)

- the minimum allowable pipe Reynold number (20,000 typical)

For use on cryogenic service the meters should have a proven record.

In special cases, a vortex meter may also be considered for line sizes >6".

The meter shall have flanged connections and the body material shall be carbon steel

with stainless steel internals, unless the application requires other materials.

The method for sensing the vortices shall be suitable for the particular application.

4.9 TURBINE METERS

The meter shall have flanged connections and the body material shall be carbon steel

with stainless steel internals, unless the application requires other materials.

On non-lubricating services (such as LNG) the turbine meter bearings shall be

tungsten carbide.

30-I-O00-SP-205

- 15-

Due consideration shall be given to prevent turbine meters from over-ranging and from

suffering hydraulic shock.

Turbine meters for custody transfer shall have two pick-up coils for use with an

electronic pulse integrity input circuit in the read-out system.

All turbine meters shall have signal amplifiers mounted close to the meter.

Turbine meter systems shall be in accordance with ISO 9951

Flow straighteners may be used with turbine meters.

All turbine meters shall be compensated by volume corrector.

Turbine meter systems shall be in accordance with ISO 9951

Flow straighteners may be used with turbine meters.

4.10 VARIABLE-AREA FLOW METERS

The use of variable-area flowmeters shall be restricted to simple local indication

applications, such as measurement of purge, cooling or sealing fluids, or in sample

loops for on-line process stream analysers.

The meters shall have a metal metering tube, with a pressure rating which is

compatible with the maximum process conditions.

4.11 ELECTROMAGNETIC FLOW METERS

Electromagnetic flowmeters may be considered where no restrictions in the flow

stream are allowed, or a rangeability of more than 3 : 1 is required. The fluid shall have

a conductivity of at least 200 S/m at a temperature below the specified limit. For

measurement of fluid velocities below 1 m/s the instrument shall be of the DC-field

type.

4.12 ULTRASONIC FLOWMETER

Ultrasonic flow meter shall be used wherever the line sizes are very big and very

accurate metering may not be required such as the main flare header. They may be

used also in cases where other types of flow measurements are not feasible because

of service conditions or economic reasons.

Transit time type flowmeter shall meet the following minimum requirement:

- Accuracy : ±0.5% of Reading (or Rate)

- Measuring tube material : Compatible with the process piping

- Sensor mount : Outside of the measuring tube

- No. of path : Double-paths or more

- Output signal : 4~20 mA DC, forward / reverse measurement

- Local display : Actual flow rate, totalizing

- Signal converter mounting : Separate type

30-I-O00-SP-205

- 16-

- Accessary : Straightening vanes (if necessary)

4.13 ANCILLARY EQUIPMENT

4.13.1 Strainers

Strainers shall be provided immediately upstream of the flow straighteners or upstream

of the minimum straight length of piping for turbine meters. In the clean condition, the

strainer shall have a pressure drop of not more than 0.02 MPa, and in a dirty condition

the strainer internals shall be capable of withstanding a pressure drop of at least 0.3

MPa.

NOTE: The latter requirement is more stringent than that specified by most suppliers,

but is considered necessary to prevent the collapse of a dirty strainer.

A differential pressure indicator shall be installed across the strainer and a

differential-pressure alarm shall be provided:

- on all applications for custody transfer

- where frequent clogging of the strainer is expected.

The strainer enclosure shall be of the quick-opening type with valved vent and drain

connections. The strainer shall have replaceable stainless steel inserts.

The mesh size for the screen will be as recommended by the meter supplier.

4.13.2 Flow Straighteners

Flow straighteners may be considered for reducing the required upstream straight

length for turbine meters, especially where strong swirls are expected.

Flow straighteners should not be used in the upstream piping of differential

pressure-type flow meters.

5.0 LEVEL INSTRUMENTS

5.1 GENERAL

Where only local indication of liquid level is required, level gauge glasses or level

indicators with magnetic coupling should be used.

For remote transmission or local control, displacer level instruments or

differential-pressure level instruments should be used. These instruments can also be

considered for local indication.

30-I-O00-SP-205

- 17-

Level gauges or external level displacers shall not be used on cryogenic

vessels/drums (temperatures less than -60 oC).

The preferred type of level measurement for cryogenic applications is differential

pressure, with the transmitter mounted above the top tapping point on an access

platform, with a self purged process hook-up. (NOTE: all cryogenic vessels, where DP

transmitters are to be installed, would require platforms on top of the vessel.)

For special applications, other principles of measurement may be considered, such as

ultrasonic instruments or instruments based on capacity, conductivity, radioactivity,

radar/laser or bubbler type.

Standpipes for level instrumentation should be used, where appropriate, to reduce the

number of vessel connections for closed and pressure vessels containing flammable

or toxic fluids. The exception to this is for safety instruments, which shall be directly

connected.

Special provisions such as purging or heating should be considered to ensure proper

operation of level instruments for highly viscous liquids, or for liquids containing water

or solids, especially if the latter tend to form sediments.

The difference between liquid density and gas/ vapour density should be taken into

account when specifying displacer instruments or calculating the range for

differential-pressure instruments.

5.2 GAUGE GLASSES

Level gauges shall be normally of the “armoured” reflex glass type with bolted covers

and tempered glass. Tube type glasses should not be used. No glass shall be used

above 10.5MPa or 315C.

Reflex gauge glass columns shall have a minimum rating equivalent to ANSI

600#.Transparent gauge glass columns shall have a minimum rating equivalent to

ANSI 300#. Glasses operating below 0C shall have frost block extensions. Gauge

glasses shall not be used for cryogenic service (<-60C)

Gauge glass columns shall consist of size 9 sections and shall not be longer than four

sections. Gauge glasses shall be equipped with top and bottom gauge cocks, fitted

with ball checks to isolate the gauge if the glass breaks. Gauge cocks shall be the

offset type to allow pushing of a cleaning rod down the glass face without removing the

gauge.

Flanged vessel connections should be used. The Piping Group will provide isolation

valves and proper length spools or nipples to fit the gauge to the vessel or standpipe.

5.3 DIFFERENTIAL PRESSURE LEVEL INSTRUMENTS

30-I-O00-SP-205

- 18-

The make and type of differential-pressure level instruments shall be the same as for

flow transmitters (smart type), with range suppression or elevation if so required by the

application.

Range suppression or elevation dependent on the instrument location and the

densities of the various fluids, shall be applied where necessary.

The instrument should generally be ranged for the distance between the nozzles,

although if necessary the zero can be elevated or top of range depressed.

5.4 LEVEL SWITCHES

Level switches should be specified for external mounting, wherever possible. The

level measuring chamber of external level switches shall be provided with vent and

drain connections. Float type switches with a pivoted horizontal float are preferred.

Float switches shall generally be used only in clean services with 0.6 or greater

specific gravity. Solid floats should be considered for pressures over 4 MPa.

For liquids with an specific gravity of less than 0.6 careful consideration should be

given to the selection of the switch type.

Switches will be hermetically sealed micro-switches, with single pole double throw gold

plated contacts.

If internal level switches have to be used, stilling wells or cages should be provided.

5.5 ULTRASONIC TYPE LEVEL INSTRUMENTS

The sensor material shall be 316 stainless steel.

Electric power supply to the control unit shall be 115VAC, 60Hz.

The supplier shall provide all the necessary cables and accessories for the installation

according to the specification sheet.

The supplier shall provide the electrical and mechanical planes(drawings) for a

suitable installation.

5.6 GUIDED WAVE RADAR TYPE

Guided Wave radar type Level Transmitter shall be considered in suitable applications

up to 2500mm range where the exact density of the liquid cannot be accurately

determined and the density keeps changing from time to time. This Selection shall be

approved by the owner.

30-I-O00-SP-205

- 19-

The Transmitter shall be Hart compatible and shall have the following diagnostic

functions

- Probe coated

- Transmitter electronic failure

- Microwave transmitter failure

- Microwave receiver failure

5.7 CONNECTION SIZES AND RATING

Level instrument flange type and rating shall comply with the piping specification and

shall be sized as follows:-

Level glasses 3/4" ANSI or ASTM FLANGE

Float Switch 2" ANSI or ASTM FLANGE

DP Transmitter 1” ANSI or ASTM FLANGE W/1” ISOLATION V/V

AND

1/2" NPT BLIND FLANGE

DP Transmitter (with seals) 3" ANSI or ASTM FLANGE

Standpipe/Bridle 2" ANSI FLANGE

Ultrasonic Level Type 8" ANSI or ASTM FLANGE

Guided Wave Radar Type 2" or 4” ANSI or ASTM FLANGE

6.0 PRESSURE INSTRUMENTS

6.1 GENERAL

The span is to be selected such that the normal operating pressure is at approximately

70 percent of the span.

For ranges with suppressed zero, the additions of the suppression plus the span must

not exceed the measuring range limit of the sensing element.

The sensing element must be capable of withstanding the design pressure applicable

to the line or vessel to which the pressure tapping is connected, without calibration

shift. In the case of DP measurement the element must be able to withstand the design

pressure being applied:

- Simultaneously to both the high and low sides of the element.

- To the high side when the low side is vented.

- To the low side when the high side is vented.

Where this is not possible over range protection devices must be employed.

6.2 PRESSURE GAUGES

30-I-O00-SP-205

- 20 -

Heavy duty, liquid filled, Bourdon tube-type, pressure gauges fitted with safety glass

and rear blow out disc, shall be used for local indication of pressure. Where this type of

gauge is not suitable owing to corrosion, plugging, etc., pressure gauges with

diaphragm seals shall be used.

When measuring pulsating pressure, pulsation dampening devices shall be fitted

Pressure gauges should have a minimum nominal diameter of 100 mm or 150mm for

d/p gauge.

Wetted parts should be 316 stainless steel. Housing material should be 304 stainless

steel or impact resistant, flame retardant plastic.

Ranges will be either 0.1, 0.2, 0.5, 1, 1.5, 2, 2.5, 4, 6, 10, 16, 25, 40 or 60 MPa.

6.3 PRESSURE TRANSMITTERS

Pressure transmitters should operate on one of the following principles:

- Capacitive (silicon)

6.4 PRESSURE SWITCHES

Pressure switches shall have a lockable, adjustable, set point and differential gap.

Wetted parts shall be 316 stainless steel.

Switches will be hermetically sealed micro-switches, with single pole double through

gold plated contacts.

7.0 TEMPERATURE INSTRUMENTS

7.1 GENERAL

Temperature measurements for remote indication and control purposes are generally

made with thermocouples or Resistance thermometer elements (RTDs). RTDs shall be

used for temperatures up to 600 oC, thermocouples for temperatures over 600 oC.

Local process temperature indicators shall be 100 mm diameter dial, “any angle”

thermometers with a thermowell protected filled system type sensing element.

Process condition temperature measurement sensing elements shall generally be

protected by thermowells, which are inserted into connections on vessels and pipe

work - although for some applications, such as LNG unloading line temperature

monitoring, skin temperature measurement sensors held mechanically in contact with,

or bonded to the surface of a vessel or pipe may be used.

30-I-O00-SP-205

- 21 -

The dual type temperature detector head shall include a 4 - 20 mA transmitter for

control loops and on packages, for other services the RTD/thermocouple signal will be

run directly to the relevant system. They shall be spring loaded type with a vibration

proof design

7.2 THERMOWELLS

Standard thermowell types are as depicted in Attachment 2.

Standard thermowell material shall be 304L stainless steel for LNG & NG service and

316 stainless steel service for other service unless other material is dictated by the

process conditions. They will be generally manufactured from drilled bar stock.

The preferred bore diameter for thermowells is 6.5 to 6.7 mm to suit a 6.4 mm

diameter standard sensor.

The thermowells shall be 1" socket welded type for pipe line of LNG and NG, 1” ANSI

flanged type for pipe line of utility, 1-1/2” ANSI flanged type for vessel and drum and 4”

ANSI flanged type for pipe line of sea water. Thermowell lengths shall be standardised,

with the number of different lengths used on the project kept to a minimum. Preferred

insertion lengths (u) for vessels is 325 mm and for pipes are as follows:-

Pipe Size

1” Socket Welded 1” , 1-1/2” & 4” Flanged

Insulated

(mm)

Non-Insulated

(mm)

(with 150mm stand out)

(mm)

4”

see attachment 2-1, 2 see attachment 2-36”

8” - 14”

> or = 16”

For temperature measurements on lines sizes less than 4" the line should be swaged

up to 4" for fitting a thermowell.

If a thermowell length must be adjusted due to fluid velocity or for special cases,

thermowell immersion into a flowing stream should not be less than 75 mm.

Thermowells installed in non-flowing static fluids should have an immersion of at least

150 mm.

Safe thermowell lengths shall be confirmed by calculation, carried out in accordance

with ASME Volume 81 (PTC 19.3), where the following fluid velocity criteria are

exceeded:-

Thermowell length (mm) 200 250 300 350

Fluid Velocity (m/s) 6 8 6 5

30-I-O00-SP-205

- 22 -

If the thermowell design is unsafe this should be rectified either by relocating the

thermowell or modifying the design (e.g. shorter or thicker well).

7.3 RESISTANCE TEMPERATURE DETECTORS (RTD)

Resistance elements shall normally be platinum type Pt 100, in accordance with IEC

60751, with a resistance of 100 ohms at 0 oC.

RTDs shall be mounted in 6.4 mm OD 316 stainless steel vibration proof sheathes

7.4 THERMOCOUPLES

Thermocouples shall be of the 6.4 mm OD mineral insulated 316 stainless steel sheath

type with hot junction free from earth.

ISA type K chromel - alumel thermocouples shall be used up to 1000 oC.

8.0 CONTROL VALVES AND ACCESSORIES

8.1 GENERAL

Sizing and calculations for control valves shall be based on the selected

manufacturer’s standard but should be verified against ISA S75.01.

Produced noise levels should not exceed 85 dBa measured 1 meter downstream and

1 meter to the side of the valve. For high pressure drop, cavitating and flashing

services, special valves or valve trims can be used for noise reduction.

Flow direction shall be clearly marked on the valve body and actuator.

Valve opening shall be indicated on a stationary scale by a moving index attached to

the valve stem.

Modulating control valves should not be used to provide tight shut off.

Valves with separate flanges or split bodies should not be used.

Materials connections and ratings shall generally conform to Piping Specifications,

while control valve stems and trims shall be stainless steel as a minimum. Control

valve manufacturer’s recommendations should also be considered based on the

service conditions for each valve.

Face to face dimensions of flanged valves shall normally conform to ANSI B16.10 or

ISA-S75.03 for below 600# rating, ISA-S75.16 for 900#-1500# rating. Flangeless

bodies such as ball and butterfly valves need not meet this requirement.

8.2 VALVE TYPE AND SIZE

30-I-O00-SP-205

- 23 -

Single port, cage guided globe valves shall generally be used for control. Butterfly type

valves shall be considered for larger sizes (8" and above) and where there is

requirement for low pressure drops. Wafer type butterfly valves should be used.

Angle valves can be considered where there are extremely large pressure drops or

severely corrosive service.

Ball valves shall only be used for on-off and shutdown service, where tight shut off is

required. Ball valves for shutdown service shall be fireproofed for 15 minutes and have

a fail safe fuse plug, in case of fire, installed in the air signal line just before the

actuator.

Other valve types may be considered for special cases.

The following standard body sizes shall be used for control valves:-

1", 1-1/2", 2", 3", 4", 6”, 8", 10", 12" and over.

Where necessary reduced trims shall be used, but the valve must be capable of taking

a full size trim.

8.3 OTHER REQUIREMENTS

For erosive service the fluid impact area shall be covered with welded stellite or similar.

A cooling extension bonnet shall be provided for flowing temperatures above 175 oC.

An extension bonnet shall also be supplied for valves on cold service with

temperatures below -10 oC.

PTFE lip seal or packing rings shall normally be used for fluid temperatures up to 200oC, graphite type with lubricator above this temperature.

Plugs, cages, seat rings and stems shall be a minimum 316 stainless steel, unless

process conditions dictate a more suitable material.

Equal percentage characteristics shall normally be selected, although dependant on the

particular application, linear characteristics can be considered for the following cases:

- where the pressure drop across the valve, under all operating conditions, is

more than 2/3 of the pressure drop across the valve in the closed position.

- level control in gravity service

- compressor anti-surge

- where two valve are used in parallel

- control valves which are only operated via a manual control station.

- minimum flow protection for pumps

- depressuring valves

30-I-O00-SP-205

- 24 -

Valve actuators shall normally be of the spring opposed diaphragm or piston type with

a normal operating range of 0.02 - 0.1 MPa for full stroke. Where service conditions

preclude the use of a spring return pneumatic actuator, double acting pneumatic or

hydraulic actuators can be used.

Hydraulic or electric actuators can be applied where they offer advantages in economy,

weight, operation etc.

The force requirements of the actuator shall be advised by the valve manufacturer. The

actual force of the actuator in both directions shall be 25% higher than the calculated value.

Electro-pneumatic positioners shall be supplied where required (generally valves >2").

They shall normally be direct acting, but reversible in the field.

Where required, continuously connected side mounted handwheels shall be supplied.

Where required, magnetically operated limit switches shall be supplied. Contacts shall

be open during valve travel, closed at travel limit. The switches shall be wired to a

single junction box mounted on the valve.

Air lock up devices shall be provided where it is required that the valve remains in last

position prior to air failure.

For valves fitted with a positioner, when solenoid valves or lock up devices are

required these shall be fitted between the positioner output and the actuator.

Solenoid valves shall not be fitted directly in a process line. However, if required, theymay be fitted in lube and seal oil lines.

Solenoid valve coils shall normally operate on 24 V DC. Although, careful

consideration should be given to voltage drop due to cable lengths. If cable sizes are

too large 115 V AC coils may be used.

Smart type positioner using hart protocol for signal transmission shall be used.

9.0 ELECTRICAL PARAMETERS

Signals between instrument control systems (DCS, ESD, DPS, etc.) and electrical

systems (switchgear, motor control, generation, etc.) shall be routed via

instrument/electrical interface cabinets, located in the relevant substation or switch

room.

Unless volt free contacts are provided in the electrical switchgear, suitable for an

instrument wetting voltage of 24 V DC, interposing relays shall be provided in the

interface cabinet to provide isolation of the instrument and electrical circuits.

30-I-O00-SP-205

- 25 -

Where measurement of electrical parameters, such as AC current, voltage and power

consumption or temperatures in electrical equipment, such as transformers and motors,

is required, signal converters shall be installed in the electrical equipment to provide 4

to 20 mA DC signals.

All signals (digital and analogue) shall be routed via the instrument/electrical interface

cabinet. Instruments shall provide cabling to the instrument side, while Electrical shall

provide the cabling to the electrical side of the interface cabinet.

10.0 MACHINE MONITORING

For monitoring the vibration and shaft position of large rotating equipment, the probes

and oscillator/demodulators are generally supplied with the equipment, but, to be

consistent throughout, the type and make shall be agreed with the mechanical

department at an early stage of the project.

Monitoring will be generally be in accordance with API 670 and API 678.

30-I-O00-SP-205

- 26 -

11.0 RELEVANT STANDARDS AND CODES OF PRACTICE

The latest issue, prior to July 2009, of the following standards and codes

should be used. The requirements of this and any other relevant project

specifications take precedent over the requirements of the listed standards.

ANSI B1.20 General purpose pipe thread

ANSI B16.5 Pipe flanges and flanged fittings

ANSI B16.10 Face of face dimensions of flanged valve

ANSI B46.1 Surface Texture.

API 550 Manual on Installation of Refinery Instruments and Control

Systems

API 670 Vibration, Axial Position and Bearing Temperature Monitoring

System.

API 678 Accelerometer Based Vibration System.

ISA.RB31.1 Specification, Installation & Calibration of Turbine Flow Meters

ISA.S75.01 Flow equations for sizing control valves

ISA.S5.1 Instrumentation in symbols and identification

ISA.S5.2 Primary logic diagrams for process operation

IEC 60034-1 Rotating Electrical Machines - Rating and performance motor

operated valves

IEC 60073 Basic and Safety Principles for Man-Machine Interface, Marking

and Identification-Coding Principles for Indication Devices and

Actuators

IEC 60079 Electrical apparatus for explosive gas atmosphere

Part 10: Classification of hazardous areas

Part 14: Electrical installations in explosive gas atmospheres

IEC 60529 Classification of degrees of protection provided by enclosures

IEC 60584 Thermocouples for temperature measurement

Part 1: Reference tables

Part 2: Tolerances

IEC 60654 Operating conditions for industrial-process measurement & control

equipment

Part 1: Temperature, humidity and barometric pressure

Part 3: Mechanical influences

Part 4: Corrosive and erosive influences

IEC 60751 Industrial Platinum Resistance Thermometer Sensors.

IEC 60801 Electromagnetic compatibility for process measurement and

control equipment

Part 3: Radiated electromagnetic field

IEC 61508 Functional safety of electrical/electronic/programmable electronic

safety related systems

30-I-O00-SP-205

- 27 -

IEC 61511 Functional safety - safety instrumented systems for the process

industry sector

ISO 5167-1 Measurement of fluid flow by means of orifice plates, Nozzles &

venturi tubes.

ISO 8310 Refrigerated Light Hydrocarbon Fluids:

Measurement of Temperature in Tanks Containing Liquefied Gases

Resistance Thermometers and Thermocouples

NFPA 59A Standard for the Production, Storage, and Handling of

Liquefied Natural Gas (LNG)

NFPA 70: National Electric Codes

NFPA 72: National Fire Alarm Code

NFPA 496: Purged Enclosures for Electrical Equipment

EN 1473 Installation and Equipment for Liquefied Natural Gas –

Design of Onshore Installations

EN 1532 Installation and Equipment for Liquefied Natural Gas – Ship

to Shore Interface

0 2010/12/09 FOR CONSTRUCTIONC.J.OH S.K.LEE

M.S.KANGC.B.PARK N/A

A 2010/01/28 FOR APPROVALC.J.OH S.K.LEE

M.S.KANGC.B.PARK N/A

REV. DATE DESCRIPTIONDESIGN

APPROVEDCLIENT

APPROVEDCHECK Q.A


삼척생산기지 1단계 본설비 실시설계 및 감리기술용역SAMCHEOK LNG TERMINAL PROJECT

TECHNICAL SPECIFICATION FOR SQUIRREL CAGE INDUCTION MOTOR

(FOR CRYOGENIC TYPE)

SCALE JOB NO. PHASE DOCUMENT NO. REV.

NONE 080228 I 30-E-E00-SP-242 0

DAEWOO ENGINEERING COMPANY

Manufacturer Two (2) months before inspection & test

KOGAS Within 5 days

after receipt of request

Manufacturer

3rd Party Inspection Agency

Manufacturer

KOGAS Issue within 5 days before F.A.T

3rd Party Inspection Work & Flow Schematic

Description Actioned by

Existing

Manufacturer 3rd Party Inspector KOGAS

New

Request for Approval of 3rd

Party Inspector(s)

Approval of 3rd Party

Inspector(s)

Manufacturing

Issue Inpsection & Test

Report by 3rd Party

Inspector

Request Approval of the

Inspection & Test Report

Approval of the Inspection

& Test Report

Request for Approval of 3rd

Party Inspector(s)

Approval of 3rd Party

Inspector(s)

Manufacturing

Perform Shop Inspection &

Test

Submit of Inspection & Test

Report

Request for Factory

Acceptance Test

`

No

After discussion with KOGAS

(Foreign : befor two (2) weeks,

Domestic : before one (1) week)

Yes

Before shipping

Issue Result within seven (7) days after rece No

Yes

Perform of Factory

Acceptance Test

Submit of Final Inspection

& Test Report

Perform of Shop Inspection

& Test

Manufacturing of Other

Remaining Material

Report Inspection & Test

Result

Perform Factory Acceptance

Test

`

Confirm of Inspection Report


`



Inspection Results Report by 3rd Party

Inspection Company

Name Symbol

INSPECTION CERTIFICATE

Certification Number:

CONTRACT NUMBER

Client(Purchaser) KOGAS

Manufacturer

Place of Inspection

Date of Inspection

Subject of Inspection Item/No Q.ty

Applicable Document/Standard

Scope of Inspection

Attached Report/Document

Result

Date of Issue Name Sign

Other Notes

* It shall be written in English

* Document list and order shall be as follows. 1. Material (Mill) Certificate.

- BOM(Bill of Material)

2. NDT Certification

-NDT inspector's certification

3. Visual and Dimension inspection

4. Pressure test

5. FAT(Factory Acceptance Test)

6. Painting test

7. Various Certification(calibration, safety, etc)

8. Others

* Part map shall be attached(NDT, Mill Certificate)

Usage of Vendor Prints Information System

CASE 1) Submit documents by system

1. Access site address(http://pmis.kogas.or.kr/vpis)

2. Install PLUG-IN

3. Log-in this page by given ID, password

4. Select the contract

5. Select the documents list to submit.

6. Press the button.

7. Fill in the description.

8. Double click the attachment and upload the file.


10. Document status are changed as submitted.

※ The contents of letter are sent by e-mail automatically.

CASE 2) Check the comments which are sent by kogas.

1. Comments are sent by e-mail and letter. you can check e-mail as below.

2. Also you can check comments by system. Double click the received letter.


4. You can check the comments as below.

Att #4

ATTACHMENT #4. PURCHASER’S STANDARD FORMS

Vendor prints index / schedule

Spare parts list for installation and commissioning

Recommended spare parts list for 2-years operation

Special tool list

Lubricants list

Electric load list

Utility consumption list

Painting schedule

Rust prevention schedule

Vendor document title block

Mechanical data book cover format

Site acceptance test completion certificate

Att #4 - 1

VENDOR PRINTS INDEX / SCHEDULE

Project SAMCHEOK LNG Terminal Project Vendor

PEN Project No. 080228 Vendor Project No.

Item No. Contract No.

Service

No.Vendor

Document No.Document Title

For ApprovalFor Final

Rev. No. Rev. No. Rev. No. Rev. No.

Out In Res Out In Res Out In Res Out In Res Out In Res

1 VP-SC-LNGpumps-G-xxxx General documentsS

A

2 VP-SC-LNGpumps-M-xxxx Mechanical documentsS

A

3 VP-SC-LNGpumps-E-xxxx Electrical documentsS

A

4 VP-SC-LNGpumps-I-xxxx Instrument documentsS

A

5 VP-SC-LNGpumps-Q-xxxx QA documents (included Test report, etc)S

A

6S

A

7S

A

8S

A

9S

A

10S

A

NOTE : S : SCHEDULE

A : ACTUAL

RESULT (RES) MEAN AS FOLLOWS

R : RESUBMIT I : INFORMATION ONLY A : APPROVED N : APPROVED AS NOTED

Att #4 - 2

SPARE PARTS LISTFOR

INSTALLATION, COMMISSIONING & START-UP




Service

Item

no.Part name

Drawing

no.Part no.

Spec

(material)

Installed

Q’ty per

unit

Recom

mende

d Q’ty

SketchUnit

price

Total

price

Att #4 - 3

RECOMMENDED SPARE PARTS LISTFOR

2-YEARS OPERATION




Service

Item

no.Part name

Drawing

no.Part no.

Spec

(material)

Installed

Q’ty per

unit

Recom

mende

d Q’ty

SketchUnit

price

Total

price

Att #4 - 4

SPECIAL TOOL LIST




Service

No. Tool name Q’ty Sketch Unit price Total price

Att #4 - 5

LUBRICANTS LIST




Service

Equipment Parts to be lubricated Lubricant Q’ty per unit & interval

NotesItem no. Q’ty Part name

Part

Q’ty

per

unit

Brand

Type

Initial

charge

(L)

Replacement

chargeMake-up

Q’ty

(L/set)interval

Q’ty

(L/set)

Interva

l

Att #4 - 6

ELECTRIC LOAD LIST




Service

Item no.

Power

source

(V/ph/hz)

Rating

(kW)

BHP

(kW)

RPM at

FL

Current (A) Eff. (%)Power

factorTime WL

(kg)

Brg

lub.

Fr.

no.

Brg no. RTD Space heater Hub

(in)ST FL LR NL 3/4 FL 3/4 FL ST STL Fr. Re. No/ph Mat Ohm V/Ph/hz kW oC

Att #4 - 7

UTILITY CONSUMPTION LIST




Service

Item no. Utility name Consumption Unit

Conditions Connection

RemarkPressure

(MPa.g)Temp (oC) Size

Rating &

facing

Att #4 - 8

PAINTING SCHEDULE

Project SAMCHEOK LNG Terminal Vendor



Service

Item no.Part to be

painted

Painting

system no.

Max.

operating

temp (oC)

Insulation

Yes / noPreparation

Paint name / thickness (micron) Net

painting

area

(m2)

RemarkPrimer 2nd 3rd 4th

Att #4 - 9

RUST PREVENTION SCHEDULE




Service

Item no.Parts to be rust

prevented

Name of rust

preventiveApplying procedure Removing procedure Protective property Remark

Vendor Document Title Block

REV. NO. DATE DESCRIPTION DRN DGN CK APP CL. APP


SAMCHEOK LNG TERMINALPHASE I PROJECT

POSCO Engineering Co., Ltd. Vendor Title

PROJECT NO. 080228 PURCHASER’S PO NO.

ITEM NO. VENDOR’S JOB NO.

TITLE:

SCALE DOCUMENT NO. REV.

VP – SC – LNGpumps – x – xxxx

Mechanical Data Book Cover Format

Front View Side View


SAMCHEOK LNG TERMINAL

PHASE I PROJECT

VENDOR NAME

P.O NO. :EQUIPMENT :VOL. NO. :

8 cm

4 cm

18#

Transparent VinylPocket

MECHANICAL DATA BOOK50#

POSCO Engineering Co., Ltd.

28#

KOREAGASCORPORATION

SAMCHEOKLNGTERMINAL

PHASEI PROJECT

VENDORNAME

P.ONO. :

EQUIPMENT :

VOL. NO. :

4cm

3cm

4#

MECHANICALDATABOOK

12#

POSCOEngineeringCo., Ltd.

7#

Mechanical Data Book Cover Format

Front View Side View

Note : Detail of KOGAS logo will be informed upon request

SITE ACCEPTANCE TEST COMPLETION CERTIFICATE

CONTRACT No.:

EQUIPMENT No.:

BETWEEN:

KOREA GAS CORPERATION (hereinafter called KOGAS)

CONTRACTOR:

1. Pursuant to Section 5.3.3 of Technical specification, KOGAS hereby certifies that Site

Acceptance Test is completed and the equipment meet the guaranteed performance values

together with all associated testing in accordance with the requirements of the CONTRACT

2. KOGAS confirms CONTRACTOR submitted MECHANICAL DATA BOOK PACKAGE (for final)

pursuant to section 11.2 and 11.4 of technical specification.

3. This certificate shall not relieve CONTRACTOR from his warranty obligations and other

provisions of the CONTRACT.

For and on behalf of For and on behalf ofKOGAS CONTRACTOR……………………… ………………….……

Signature Signature

Name Name

Position Position