vedst003 - shell and tube heat exchanger specification sheet

8/10/2019 VEDST003 - Shell and Tube Heat Exchanger Specification Sheet

1/23

June 1999

Process Industry PracticesVessels

PIP VEDST003Shell and Tube Heat Exchanger Specification Sheet


2/23

PURPOSE AND USE OF PROCESS INDUSTRY PRACTICESIn an effort to minimize the cost of process industry facilities, this Practice has

been prepared from the technical requirements in the existing standards of major industrial users, contractors, or standards organizations. By harmonizing these technicalrequirements into a single set of Practices, administrative, application, and engineeringcosts to both the purchaser and the manufacturer should be reduced. While this Practiceis expected to incorporate the majority of requirements of most users, individualapplications may involve requirements that will be appended to and take precedence over this Practice. Determinations concerning fitness for purpose and particular matters or application of the Practice to particular project or engineering situations should not bemade solely on information contained in these materials. The use of trade names from

time to time should not be viewed as an expression of preference but rather recognizedas normal usage in the trade. Other brands having the same specifications are equallycorrect and may be substituted for those named. All practices or guidelines are intendedto be consistent with applicable laws and regulations including OSHA requirements. Tothe extent these practices or guidelines should conflict with OSHA or other applicablelaws or regulations, such laws or regulations must be followed. Consult an appropriate

professional before applying or acting on any material contained in or suggested by thePractice.

Process Industry Practices (PIP), Construction Industry Institute, TheUniversity of Texas at Austin, 3208 Red River Street, Suite 300, Austin,Texas 78705. PIP member companies may copy this practice for their internaluse.

Not printed with State funds


3/23

June 1999

Process Industry Practices Page 1 of 3

Process Industry PracticesVessels

PIP VEDST003Shell and Tube Heat Exchanger Specification Sheet

Table of Contents

1. Introduction ..................................21.1 Purpose ......................... .....................21.2 Scope ....................... ..........................2

2. References....................................2

3. Use of This PIP .............................23.1 Shell and Tube Heat Exchanger

Specification Sheet.............................23.2 Entering Text and Data .......................2

4. Specification Sheet andDescription ...................................34.1 Data Description ......................... ........34.2 Specification Sheet .......................... ...3

Appendix AData Format and Description

Appendix BSample Specification Sheet (Page 1)

Shell and Tube Heat Exchanger Specification Sheet


4/23

PIP VEDST003Shell and Tube Heat Exchanger Specification Sheet June 1999

Page 2 of 3 Process Industry Practices

1. Introduction

1.1 Purpose

The purpose of this Practice is to provide instruction and/or direction to designers for preparation of the Shell and Tube Heat Exchanger Specification Sheet (hereafter referred to as the Specification Sheet). The Specification Sheet, prepared inconjunction with PIP VECV1001 and PIP VESV1002 completes a specificationsuitable for obtaining comprehensive bids and subsequent purchase of shell and tubeheat exchangers. Note that PIP VEDV1003 , Vessel Drawing/Data Sheet and

Instructions , does not apply to shell and tube heat exchangers.

1.2 Scope

This Practice identifies information to be placed on the PIP Shell and Tube Heat Exchanger Specification Sheet .

2. References

Applicable requirements in the latest edition (or the edition indicated) of the following industrystandards and references shall be considered an integral part of this Practice. Short titles will

be used herein when appropriate.

Process Industry Practices (PIP)

PIP VECV1001 - Vessel/S&T Heat Exchanger Design Criteria ASME Code Section VIII, Divisions 1 and 2

PIP VEDV1003 - Vessel Drawing/Data Sheet and Instructions

PIP VESV1002 - Vessel/S&T Heat Exchanger Fabrication Specification ASME Code Section VIII, Divisions 1 and 2

3. Use of this Practice

3.1 Shell and Tube Heat Exchanger Specification Sheet

The Specification Sheet is an element of a complete shell and tube heat exchanger specification. This form provides preprinted line items to be completed by the designer and/or fabricator. Some sections of this form are optional and will not apply to somedesigns or may be omitted when agreed with the User to comply with the preparers

established work process.3.2 Entering Text and Data

Each numbered line of the Specification Sheet should be properly filled in or markedwith NA to indicate that the information is not applicable. It is suggested that lines

be left blank if the information is not known at the time. Lines not completed indicatethe form is not complete and should be filled in by the designer or manufacturer.


5/23

PIP VEDST003June 1999 Shell and Tube Heat Exchanger Specification Sheet

Process Industry Practices Page3 of 3

Additional information that may be required, but does not have a preprinteddescription line, should be added in the Remarks area of the Specification Sheet.

4. Specification Sheet and Description

4.1 Data Description

Appendix A provides guidance for completion of information on Page 1 of theSpecification Sheet.

4.2 Specification Sheet

Appendix B provides a hardcopy of each page that may be required to define the shelland tube heat exchanger. Optional information may be:

Performance of One Unit (Page 1): This may be optional when the User or Process Licensor considers this information proprietary.

Connection Schedule (Page 2), Materials of Construction (Page 2), Gaskets(Page 2): Used when the Designer/User requires such level of detail to definematerials for individual components. These sections may not be necessary if theinformation is defined sufficiently on Page 1.

Thermal Expansion Design Exchanger Design Information (Page 2): This isrequired only for exchangers such as fixed tubesheet or single pass floating headtype exchangers where thermal expansion must be considered for the mechanicaldesign.

Additional Remarks, Sketches, Etc. (Page 3): Used for additional remarks whensufficient space is not available on Page 1. Also used for schematic sketches to

illustrate required features of the design and tube layouts when necessary to provide this information to the Manufacturer.

Pages 4 and 5: One or both pages may be necessary when boiling and/or condensing fluids with ranges of physical properties occur.


6/23


7/23

Appendix A

Data Format and Description


8/23


Page A-2 Process Industry Practices

PIP Shell and Tube Heat Exchanger Specification Sheet

Data Format and DescriptionAPPENDIX A

LineNo.

Data No.On Line

Specification SheetInput Item

Description DataWidth

DataType

Units TypicalComments

1 1 Client Client or end user name 40 C

1 2 Location Installation site location 40 C

2 1 Process Unit Process or operating facility name 40 C

2 2 Item No. Equipment identification number or tag 20 C

2 3 Document No. Document number 20 C

3 1 Job No. Project identification number 20 C

3 2 Fabricator Manufacturer or fabricator name 40 C

4 1 Service of Unit Service description 50 C

4 2 No. of Units Total number of service units 2 I

5 1 Size Size expressed as "shell diameter - tube length". For Kettle type this would be expressed as bundle dia./kettledia. - tube length

20 N in-in,mm-mm

5 2 TEMA Type(Hor/Ver)

TEMA type designation 20 C

5 3 Connected in Parallel Number of shells connected in parallel per unit 2 I

5 4 Series Number of shells connected in series per unit 2 I

6 1 Surface/Unit (Eff.) Effective surface area per unit; finned effective surfacewhen finned tubes are specified

12 N ft, m

6 2 Shells/Unit Number of shells per unit 2 I

6 3 Surface/Shell (Eff.) Effective surface per shell 12 N ft, m

9 1,2 Fluid Name Shell side and tube side fluid name 30 C

10 1,2 Fluid Quantity, Total Total shell side and tube side mass flow 14 N lb/hr,kg/hr


9/23


Process Industry Practices Page A-3



LineNo.

Data No.On Line



DataType


11 1,2,3,4,5,6,7,8

Vapor (MW) Shell side inlet and outlet vapor mass f low (except steam)followed by molecular weight in ( ),Tube side inlet and outlet vapor mass flow (except steam)followed by molecular weight in ( )

14,7 N,N lb/hr,kg/hr

12 1,2,3,4 Liquid Shell side inlet and outlet liquid mass flow (except water),Tube side inlet and outlet liquid mass flow (except water)

14 N lb/hr,kg/hr

13 1,2,3,4 Steam Shell side inlet and outlet steam mass flow,Tube side inlet and outlet steam mass flow

14 N lb/hr,kg/hr

14 1,2,3,4 Water Shell side inlet and outlet water mass flow,Tube side inlet and outlet water mass flow

14 N lb/hr,kg/hr

15 1,2,3,4,5,6,7,8

Noncondensable(MW)

Shell side inlet and outlet noncondensable mass flowfollowed by the molecular weight in ( ),Tube side inlet and outlet noncondensable mass flowfollowed by the molecular weight in ( )

14,7 N,N lb/hr,kg/hr

16 1,2,3,4 Temperature Shell side inlet and outlet fluid temperature,Tube side inlet and outlet fluid temperature

10 N F,C

17 1,2,3,4,5,6,7,8

Density(Vapor/Liquid)

Shell side inlet and outlet fluid density for vapor and/or liquid if present,Tube side inlet and outlet fluid density for vapor and/or liquid if present

10 N lb/ft3,kg/m 3

18 1,2,3,4,5,6,7,8

Viscosity(Vapor/Liquid)

Shell side inlet and outlet fluid viscosity for vapor and/or liquid if present,Tube side inlet and outlet fluid viscosity for vapor and/or liquid if present

10 N cP


10/23





LineNo.

Data No.On Line



DataType


19 1,2,3,4,5,6,7,8

Specific Heat(Vapor/Liquid)

Shell side inlet and outlet fluid specific heat for vapor and/or liquid if present,Tube side inlet and outlet fluid specific heat for vapor and/or liquid if present

10 N Btu/lb-F,kJ/kg-C,kcal/kg-C

20 1,2,3,4,5,6,7,8

Thermal Conductivity(Vapor/Liquid)

Shell side inlet and outlet fluid thermal conductivity for vapor and/or liquid if present,Tube side inlet and outlet fluid thermal conductivity for vapor and/or liquid if present

10 N Btu/hr-ft-F,W/m-C,kcal/m-hr-C

21 1,2,3,4 Latent Heat Shell side fluid latent heat of vaporization at the statedtemperature when boiling/condensing conditions arepresent,Tube side fluid latent heat of vaporization at the statedtemperature when boiling/condensing conditions arepresent

10 N Btu/lb, kJ/kg,kcal/kg

22 1,2 Inlet Pressure Shell side fluid pressure at the inlet nozzle,Tube side fluid pressure at the inlet nozzle

10 N psig, bar g,kg/cmg

23 1,2 Velocity Shell side and tube side fluid average velocity. Velocity isbased on nominal crossflow area and average fluidconditions.

7 N ft/s, m/s

24 1,2,3,4 Pressure Drop(Allowable/Calculated)

Shell side and tube side allowable and/or calculatedpressure drop through the exchanger including nozzlesand static head when present

5 N psi, bar,kg/cm

25 1,2 Fouling Resistance Shell side and tube side design value for resistance toheat transfer due to fouling. Value is based on the surfacewith which the fluid is in contact.

10 N hr-ft-F/Btu,m-C/W,hr-m-C/kcal


11/23





LineNo.

Data No.On Line



DataType


26 1,2 Avg. Film Coefficient Average heat transfer coefficient between the shell sideand tube side fluid and the tube. Value is based on thesurface with which the fluid is in contact.

6 N Btu/hr-ft-F,W/m-C,kcal/hr-m-C

27 1 Heat Exchanged Total energy exchanged between the shell side and tubeside fluids

12 N Btu/hr, MW,kcal/hr

27 2 MTD(Corrected/Weighted)

Logarithmic mean temperature difference corrected for the exchanger pass arrangement and weighted accordingto the heat release curve

7 N F,C

28 1,2,3 Transfer Rate(Required/Fouled/Clean)

Overall heat transfer coefficient required for the duty,surface area, and MTD and actual values under fouledand clean conditions

7 N Btu/hr-ft-F,W/m-C,kcal/hr-m-C

29 1,2,3 rV Inlet Nozzle

Bundle Entrance Bundle Exit

Momentum fluxes in the inlet nozzle, at the entrance tothe bundle, and at the exit of the bundle

5 N lb/ft-sec,kg/m-sec

31 1 Tube No. Number of tubes per shell; for the case of U tube typeexchangers, the Tube No. shall be stated as the number of U tubes

5 I

31 2 OD Outer diameter of the tubes 5 N in, mm

32 1,2 Thickness (Min/Avg) Tube wall thickness and whether the minimum or averagevalue is specified

7 N in, mm,BWG

33 1 Pitch Distance from tube centerline to tube centerline 5 N in, mm

33 2 Flow Angle Angle at which the flow meets the tube bundle


12/23





LineNo.

Data No.On Line



DataType


33 3,4 Inlet Shell side and tube side Inlet Nozzle Number, Size, andRating

30 C

34 1 Length Overall tube length from end to end required for theexchanger type selected; for the case of U tube typeexchangers, the tube length shall be from the tube end tothe tangent line where the tube bend begins

6 N ft, mm

34 2 Type Type of tube 20 C Straight,U-tube,Bare,Finned

34 3,4 Outlet Shell side and tube side Outlet Nozzle Number, Size, andRating

30 C

35 1 Tube-TubesheetJoint

Type of tube-to-tubesheet joint 45 C Rolled,Expanded,Hydraulic

expanded,SealWeldedStrengthWelded

35 2,3 Intermediate Shell side and tube side Intermediate Nozzle Number,Size, and Rating

30 C

36 1,2 Shell Diameter (ID/OD)

Shell diameter and whether the inner or outer diameter isspecified

4 N in, mm ID for rolledshells.NPS for pipe shells.


13/23





LineNo.

Data No.On Line



DataType


36 3,4 Vent Shell side and tube side vent nozzle number, size, andrating

30 C

37 1 Cross Baffle Type Type of baffling 16 C Segmental,DoubleSegmental,TripleSegmental,NTIW, Diskand Donut

37 2,3 Drain Shell side and tube side drain nozzle number, size, andrating

30 C

38 1 Spacing: c/c Distance from centerline to centerline of adjacent baffles 6 N in, mm

38 2 Inlet Distance from the tubesheet nearest the shell inlet to thefirst baffle

6 N in, mm

39 1,2 %Cut (Dia./Area) Percentage of the shell ID or inside cross-sectional areaout of which the baffle is cut

4 N %

40 1 Tube Support Type of supports for the tube bundle 40 C Full support@ U-bend

40 2,3 Design Pressure Design pressure for mechanical design; when requiredFV (full vacuum) shall also be specified at a specifiedtemperature

20 C 150/FV@200F

41 1 Long Baffle SealType

Type of seal for the longitudinal baffle 20 C Welded,leaf,packed,tongue andgroove


14/23





LineNo.

Data No.On Line



DataType


41 2,3,4,5 Design Temp.(Max/MDMT)

Maximum Design Temperature and Minimum DesignMetal Temperature for mechanical design

10 N F,C

42 1 By-Pass Seal Type Dummy tubes, seal strips, rods 20 C

42 2,3 No. of Passes per Shell

1 for E shells, 2 for F type, Kettle, Divided, Split, Cross:for tube side specify the number of passes, i.e.: 1,2,3,...

10 C

43 1 ImpingementProtection

Type of impingement protection 20 C Impactplate,impact rods

43 2,3 Corrosion Allowance Corrosion allowance for design of the pressurecomponents of the shell side and tube side channels

10 C

45 1 Tubes Materials of construction for the tubes 20 C

46 1 Shell Materials of construction for the shell 20 C

46 2 Shell Side Materials of construction for the shell side gaskets 40 C

47 1 Shell Cover Materials of construction for the shell cover 20 C47 2 Tube Side Materials of construction for the tube side gaskets 40 C

48 1 Channel or Bonnet Materials of construction for the channel or bonnet 20 C

48 2 Floating Head Materials of construction for the floating head gaskets 40 C

49 1 Channel Cover Materials of construction for the channel cover 20 C

49 2 Spare Sets Reqd. Number of spare sets of gaskets required or SeePurchasing Documents

25 C

50 1 Floating HeatCover/Bolts

Materials of construction for the floating heads cover andbolting components

20 C


15/23





LineNo.

Data No.On Line



DataType


50 2 Test Ring Reqd.(Y/N)

Whether or not a test ring is required for the exchanger bundle

3 C Y,N

51 1 Tubesheets Materials of construction for the tubesheets 20 C

51 2 Insulation: Shell Shell insulation material and thickness 20 C

52 1 Baffles & SupportPlates

Materials of construction for the baffles and support plates 20 C

52 2,3 Channel Inlet/Exit Insulation material and thickness for the inlet and outletchannels

20 C

53 1 Expansion Joint Type Type of expansion joint, if required 20 C Bellows,Flued,Flangedand Flued

53 2 Expansion JointMaterial

Materials of construction for the expansion joint 20 C

54 1 Code Requirements Applicable Codes which must be applied to the design of the heat exchanger

36 C ASME Sect.VIII D1,Sect. I,Lethal, etc.

54 2 Calc. MAWP (Y/N) Whether or not the maximum allowable working pressuremust be calculated

1 C Y,N

54 3 TEMA Class The TEMA Class specifying the requirements for thedesign of the heat exchanger

1 C R,C,B

55,56,57,58

1 REMARKS: Further remarks, comments, and notes about the heatexchanger

1000 C


16/23





LineNo.

Data No.On Line



DataType


59 1,2 Originator/Check: Initials of the originator and checker of the heat exchanger design

3 C

59 3 Approved: Initials of the approver of the final heat exchanger design 3 C

59 4 Issue Date Date of issue of the heat exchanger design 9 D

59 5 Issue No. Issue/revision number of the heat exchanger design. 3 C


17/23

Appendix B

Sample Specification Sheet (Page 1)


18/23

SHELL AND TUBE HEAT EXCHANGERSPECIFICATION SHEET

1 Client 1 Location 2 Pag x of2 Process Unit 1 Item No. 2 Document No. 33 Job No. 1 Fabricator 2

4 Service of Unit 1 No. of Un5 Size 1 TEMA Type (Hor/Vert) 2 Connected in 3 Parallel 46 Surface/Unit (Eff.) 1 ft Shells/Unit 2 Surface/Shell (Eff.) 37 PERFORMANCE OF ONE UNIT (Optional)8 Fluid Allocation (Inlet) SHELL SIDE (Outlet) (Inlet) TUBE SIDE (Outle9 Fluid Name 1 2

10 Fluid Quantity, Total lb/hr 1 211 Vapor (MW) lb/hr 1,2 3,4 5,6 7,812 Liquid lb/hr 1 2 3 413 Steam lb/hr 1 2 3 414 Water lb/hr 1 2 3 415 Noncondensable (MW) lb/hr 1,2 3,4 5,6 7,816 Temperature F 1 2 3 417 Density (Vapor/Liquid) lb/ft 1 2 3 4 5 6 718 Viscosity (Vapor/Liquid) cP 1 2 3 4 5 6 719 Specific Heat (Vapor/Liquid) Btu/lb F 1 2 3 4 5 6 7

20 Thermal Conductivity (Vapor/Liquid) Btu/hr ft F 1 2 3 4 5 6 721 Latent Heat Btu/lb @ F 1 @ 2 3 @ 422 Inlet Pressure psia/psig 1 223 Velocity ft/s 1 224 Pressure Drop (Allowable/Calculated) psi 1 2 3 425 Fouling Resistance hr ft F/Btu 1 226 Avg. Film Coefficient Btu/hr ft F 1 227 Heat Exchanged 1 Btu/hr MTD (Corrected) (Weighted) 228 Transfer Rate (Required/Fouled/Clean) 1 2 3 Btu/h29 V - lb/ft-s 2 : Inlet Nozzle 1 Bundle Entrance 2 Bundle Exit 330 CONSTRUCTION PER SHELL31 Tube No 1 OD 2 in NOZZLES - No. Size & Rating (Optional)32 Thickness 1 in/BWG (Min./Avg.) 2 SHELL SIDE TUBE SIDE33 Pitch 1 in 2 Inlet 3 4

34 Length 1 ft Type 2 Outlet 3 435 Tube-Tubesheet Joint 1 Intermediate 2 336 Shell Diameter (ID/OD) 1,2 in Vent 3 437 Cross Baffle Type 1 Drain 2 3

[3] 38 Spacing: c/c 1 in No. of Crosspasses 239 % Cut (Dia./Area) 1,240 Tube Support 1 Design Pressure psig 2 341 Long Baffle Seal Type 1 Design Temp(Max/MDMT) F 2,3 4,542 By-Pass Seal Type 1 No. of Passes per Shell 2 343 Impingement Protection (Y/N) 1 Corrosion Allowance in 2 344 MATERIALS OF CONSTRUCTION (Optional)45 Tubes 1 Gaskets 246 Shell 1 Shell Side 247 Shell Cover 1 Tube Side 2

48 Channel or Bonnet 1 Floating Head 249 Channel Cover 1 Spare Sets Req'd 250 Floating Head Cover/Bolts 1 Test Ring Req'd (Y/N) 251 Tubesheets 1 Insulation: Shell 252 Baffles & Support Plates 1 Channel Inlet/Exit 2,353 Expansion Joint Type 1 Expansion Joint Material 254 Code Requirements 1 Calc. MAWP (Y/N) 2 TEMA Clas55 REMARKS: 156 157 158 159 Originator/Check: 1 / 2 Approved: 3 Issue Date: 4 Issue No.

Form PIP VEDST003 (04/99) (English


19/23

SHELL AND TUBE HEAT EXCHANGERSPECIFICATION SHEET

1 Client Location Page 1 of 2 Process Unit Item No. Document No.3 Job No. Fabricator

4 Service of Unit No. of Units 5 Size TEMA Type (Hor/Vert) Connected in Parallel Series

6 Surface/Unit (Eff.) ft Shells/Unit Surface/Shell (Eff.) ft 7 PERFORMANCE OF ONE UNIT (Optional)

8 Fluid Allocation (Inlet) SHELL SIDE (Outlet) (Inlet) TUBE SIDE (Outlet)9 Fluid Name

10 Fluid Quantity, Total lb/hr11 Vapor (MW) lb/hr12 Liquid lb/hr13 Steam lb/hr14 Water lb/hr15 Noncondensable (MW) lb/hr16 Temperature F17 Density (Vapor/Liquid) lb/ft 18 Viscosity (Vapor/Liquid) cP 19 Specific Heat (Vapor/Liquid) Btu/lb F 20 Thermal Conductivity (Vapor/Liquid) Btu/hr ft F 21 Latent Heat Btu/lb @ F @ @22 Inlet Pressure psia/psig23 Velocity ft/s24 Pressure Drop (Allowable/Calculated) psi

25 Fouling Resistance hr ft F/Btu 26 Avg. Film Coefficient Btu/hr ft F

27 Heat Exchanged Btu/hr MTD (Corrected) (Weighted) F28 Transfer Rate (Required/Fouled/Clean) Btu/hr ft F

29 V - lb/ft-s 2 : Inlet Nozzle Bundle Entrance Bundle Exit 30 CONSTRUCTION PER SHELL 31 Tube No. OD in NOZZLES - No. Size & Rating (Optional) 32 Thickness in/BWG (Min./Avg.) SHELL SIDE TUBE SIDE 33 Pitch in Inlet 34 Length ft Type Outlet

35 Tube-Tubesheet Joint Intermediate36

Shell Diameter (ID/OD) in Vent 37 Cross Baffle Type Drain[3] 38 Spacing: c/c in No. of Crosspasses 39 % Cut (Dia./Area) 40 Tube Support Design Pressure psig 41 Long Baffle Seal Type Design Temp(Max/MDMT) F 42 By-Pass Seal Type No. of Passes per Shell 43 Impingement Protection (Y/N) Corrosion Allowance in 44 MATERIALS OF CONSTRUCTION (Optional)

45 Tubes Gaskets46 Shell Shell Side47 Shell Cover Tube Side48 Channel or Bonnet Floating Head49 Channel Cover Spare Sets Req'd

50 Floating Head Cover/Bolts Test Ring Req'd (Y/N)

51 Tubesheets Insulation: Shell52 Baffles & Support Plates Channel Inlet/Exit 53 Expansion Joint Type Expansion Joint Material 54 Code Requirements Calc. MAWP (Y/N) TEMA Class

55 REMARKS:56575859 Originator/Check: / Approved: Issue Date: Issue No.

Form PIP VEDST003 (04/99) (English Units)


20/23

Job No. * Page 2 ofClient *LocationItem No.Document No. Issue No.

[3] 1 CONNECTION SCHEDULE (Optional) THERMAL EXPANSION DESIGN INFORMATION2 Mark No. Size Rating Facing Description Shell Shell Tubesheet Tube Tube3 Req'd. (Optional) Mean Metal Press. Mean Metal Mean Metal Press.

4 Temp. F psig Temp. F Temp. F p5 Design6 Normal7 Startup8 Shutdown9 Upset #1

10 Upset #211 Steamout12 Expansion Joint Design Life Cycles13

14 MATERIALS OF CONSTRUCTION (Optional) Corr. Al15 Shell:16 Head:17 Pipe/Stubends:18 Nozzle Necks:19 Nozzle Flanges:20 Body Flanges:21 Expansion Joint:22 Supports:23 Bolting (internal):24 Bolting (external):25 Nozzle Reinforcement:26 Tubes:27 Tubesheets:28 Bonnet/Channel:29 Bonnet Head(s):30 Channel Cover(s):31 Body Flanges:32 Pipe/Stubends:33 Bolting (internal):34 Bolting (external):35 Nozzle Reinforcement:36 Nozzle Necks:37 Nozzle Flanges:38 Baffles, Spacers, Tie Rods: in3940414243

4445464748

49 GASKETS (Optional) MECHANICAL DATA (Optional) 50 Shell Side: Thickness: in MAWP (hot and corroded): psi 51 y= psi m= MAP (new and cold): psi 52 Tube Side: Thickness: in Hydrotest Pressure: 53 y= psi m= Field: psig Shop: psig 54 Floating Head: Thickness: in Weights: Empty: lbs Bundle: lbs 55 y= psi m= Full of Water: lbs

Form PIP VEDST003 (04/99) (English Unit


21/23

Job No. * Page 3 ofClient * (OPTIONALocationItem No.Document No. Issue No.

ADDITIONAL REMARKS, SKETCHES, ETC.



22/23

Job No. * Page 4 of Client * (OPTIONAL PAGE)LocationItem No.Document No. Issue No.

Fluid Name: Ref . Pressure 1: PSI (ABS)

Pressure Temp. Enthalpy Mass Vapor

PSI (ABS) F BTU/LB Fraction

Density Density Viscosity Viscosity Thermal Thermal Sp. Heat Sp. Heat Surface Liquid Liq. C

Vapor Liquid Vapor Liquid Cond., Vap Cond., Liq Vapor Liquid Tension Critcal Press. Temp.

LB/FT3 LB/FT3 CP CP BTU/HR-FT-F BTU/HR-FT-F BTU/LB-F BTU/LB-F DYNE/CM PSIA F

Fluid Name: Ref . Pressure 2: PSI (ABS)

Pressure Temp. Enthalpy Mass Vapor


Density Density Viscosity Viscosity Thermal Thermal Sp. Heat Sp. Heat Surface Liquid Liq. C

Vapor Liquid Vapor Liquid Cond., Vap Cond., Liq Vapor Liquid Tension Critcal Press. Temp.

LB/FT3 LB/FT3 CP CP BTU/HR-FT-F BTU/HR-FT-F BTU/LB-F BTU/LB-F DYNE/CM PSIA F


Heat Release Curve

0.00

0.20

0.40

0.60

0.80

1.00

1.20

Temperature (F)

E n

t h a

l p y

( B T U / L B )

0.0000

0.2000

0.4000

0.6000

0.8000

1.0000

1.2000

M a s s

V a p o r

F r a c

t i o n

Enthalpy Mass Vapor Frac

Heat Release Curve

0.00

0.20

0.40

0.60

0.80

1.00

1.20

Temperature (F)

E n

t h a

l p y

( B T U / L B )

0.0000

0.2000

0.4000

0.6000

0.8000

1.0000

1.2000

M a s s

V a p o r

F r a c

t i o n

Enthalpy Mass Vapor Frac


23/23

Job No. * Page 5 of Example Data Client * (OPTIONAL PAGE)

LocationItem No.Document No. Issue No.

Fluid Name: Hot Fluid Ref. Pressure 1: 31.58 PSI (ABS)Pressure Temp. Enthalpy Mass Vapor


31.58 100.1 0.00 1.0000

31.55 91.4 6.88 1.0000

31.49 82.7 13.77 1.0000

31.46 80.0 16.18 1.0000