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ROYAL BOTANIC GARDENS VICTORIA
CRANBOURNE GARDENS WATER TREATMENT PLANT
EXPRESSION OF INTEREST SUPPORTING TECHNICAL INFORMATION
ROYAL BOTANIC GARDENS VICTORIA
CRANBOURNE GARDENS WATER TREATMENT PLANT EXPRESSION OF INTEREST SUPPORTING TECHNICAL
INFORMATION
PP REF : C17204
DATE 20/07/2018 REV: C
COMMERCIAL-IN-CONFIDENCE
WWW.PERMEATE.COM.AU
PAGE 2 OF 22
PROPRIETARY AND CONFIDENTIAL INFORMATION
The attached document contains proprietary and confidential information and is submitted under a confidential relationship for the
purpose defined below.
Purpose: The purpose of this report is to detail the technical supporting information for Section 2 – Specification of the Expression of
Interest document.
By accepting this document, the recipient agrees:
(a) the attached document has been prepared for ROYAL BOTANIC GARDENS VICTORIA by Permeate Partners Pty Ltd (ACN 130
112 257) (Permeate Partners) in accordance with the terms of the engagement. No liability is accepted by Permeate Partners
for use of the attached document by any other party;
(b) ownership of copyright and all other intellectual property rights in all of the attached document shall remain vested in
Permeate Partners Pty Ltd (ACN 130 112 257) (Permeate Partners). This includes all rights of redesign, manufacture,
reproduction, use or sale;
(c) the attached document contains confidential information belonging to Permeate Partners;
(d) the recipient will not use (except for the Purpose), authorise the use of, disclose, make copies of, reverse engineer, reproduce
or incorporate in other work or projects the attached document, except with the prior written approval of Permeate
Partners;
(e) the obligations of non-use and non-disclosure stated in paragraph (c) above does not apply to any information that the
recipient can demonstrate is already in the public domain through no fault of the recipient or that is already in the possession
of the recipient and not held by it under any obligation of confidentiality or similar legal restriction. Nothing in this paragraph
affects the rights of Permeate Partners under paragraph (a) above.
(f) references in the above paragraphs to ‘the attached document’ includes any part of it and includes all drawings, designs,
reports, specifications, calculations, concepts, processes and other information within the attached document or provided
in conjunction with the attached document.
PROJECT REFERENCE
Permeate Partners Reference: C17204
ROYAL BOTANIC GARDENS VICTORIA Reference: 18-003
DOCUMENT INFORMATION AND STATUS
Revision Date Comments Author Review Approve
CURRENT
C 20/07/2018 For Submission PBG AC KD
HISTORY
A 4/04/2018 First Draft PBG AC KD
B 22/05/2018 Updated Draft PBG AC KD
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TABLE OF CONTENTS
SECTION DESCRIPTION PAGE
1 Background and Introduction 4 1.1 Cranbourne Gardens 4 1.2 Project Overview 4 1.3 Document Purpose 4
2 General Information 5 2.1 Standards 5 2.2 Safety in Design 5 2.3 Location of Equipment 5 2.4 Design Life 5 2.5 Materials of Construction 6 2.6 Sampling and Drain Points 6 2.7 Chemical Storage and Dosing 6 2.8 Electrical 7
2.8.1 Instrumentation 7 2.8.3 Surge protection 7
2.9 Automation and Control Functionality 7 2.9.5 SCADA 8
3 Design Basis 9 3.1 Feed Water Quality 9 3.2 Design Flow Characteristics 10 3.3 Treated Water Requirements 11 3.4 Plant Availability 11 3.5 Treatment Process 11 3.6 General Requirements 13
4 Scope of Work 14 4.1 Work Package #2 Termination Points 15 4.2 Work Package #2 Task Summary 17
Appendix A – Reference Process Flow Diagram (PFD) 18 Appendix B – Piping and Instrumentation Diagram (P&ID) 19 Appendix C – Reference Building General Arrangement Drawing 20 Appendix D – Site Layout Drawings 21 Appendix E – Existing Irrigation Pump Shed 22
LIST OF TABLES
SECTION DESCRIPTION PAGE
Table 1 – Irrigation water maximum specified key parameters 4 Table 2 – Design life of key components 5 Table 3 – Minimum requirements for materials of construction 6 Table 4 – Key Feed water quality parameters as provided by Melbourne Water 9 Table 5 – Design flow characteristics basis summary 10 Table 6 – Additional treated water quality targets 11 Table 7 – Treatment solution process summary 11 Table 8 – Scope of work for different packages 14 Table 9 – Termination points schedule 15
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1 BACKGROUND AND INTRODUCTION
1.1 Cranbourne Gardens
Royal Botanic Gardens Victoria (RBGV) at Cranbourne Gardens is one of Victoria’s most precious areas of remnant native bushland and
offers visitors the chance to explore heathlands, wetlands and woodlands on the 363-hectare site. It is recognised as a site of State
significance for flora and fauna conservation, with over 25 species listed as endangered, threatened or at risk of extinction.
Facilities in the bushland include over ten kilometres of walking tracks, six kilometres of cycling tracks, a lookout tower, picturesque
shelters, barbecues and picnic tables. The Australian Garden, completed in October 2012, celebrates the beauty and diversity of
Australian landscapes and flora and features approximately 170,000 plants from 1,700 plant varieties. Complementing the Garden are
a visitor centre, café, gift shop and interpretive displays
1.2 Project Overview
A previous technical review of potential alternative water sources for RBGV identified that the ‘Class A’ water supplied as part of the
Eastern irrigation Scheme (EIS) (formerly TopAq) as the most sustainable long-term alternative water source. The EIS water nutrient
load for both Total Nitrogen (TN) and Total Phosphorous (TP) is higher than the maximum requirements and if used (without further
treatment) as the source of irrigation water may potentially be damaging to the soil and a long term risk to sensitive vegetation.
Consequently, in order to manage this risk, additional treatment of the EIS feed water is required to achieve the key irrigation water
targets as presented in Table 1.
Table 1 – Irrigation water maximum specified key parameters
Parameter Unit Maximum specification
(100’%tile)
Conductivity µS/cm < 750
Total dissolved salt (TDS)1 mg/l < 520
pH -- 6.5 to 7.5
Total nitrogen mg/l as N < 3
Total phosphorous mg/l as P < 1
NOTES:
1. The specified values is assumed from the conductivity based on a typical ratio of 0.7
1.3 Document Purpose
This document provides the following purpose:
Design basis for the Water Treatment Plant (WTP) to be considered in the EOI submission.
Technical requirements for the WTP.
A reference conceptual design has been included to accompany this technical specification including preliminary process and
arrangement drawings. Contractors are encouraged to offer innovative / alternate approaches which:
Improve safety and operation of the facility;
Reduce both capital and / or operating costs;
Improve process flexibility or robustness;
Improve ease of access / maintenance.
.
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2 GENERAL INFORMATION
The following section outlines the general requirements of the project.
2.1 Standards
All applicable best practice design guidelines and standards are to be referenced, followed, implemented and adhered to where
applicable, which may include, but not be limited to, the following:
Australian Standards
International (ISO) Standards
WSAA Codes
Australian Guidelines as applicable
NSF Certifications for Potable Water
Associated Australian Standards for the safe use and storage of chemicals
2.2 Safety in Design
Safety issues must be considered and addressed in the design, in particular:
a) All equipment must comply with the more stringent requirements of:
i. Relevant Regulations;
ii. Australian Standards;
iii. Industry Code of Practice and Guidelines; and
iv. Industry best practice for water infrastructure in Australia.
b) The equipment and plant layout shall be designed such that it can be operated and maintained in a safe and ergonomic
manner.
a) All equipment must be provided with isolation devices to enable it to be removed from service in a safe and practical
manner.
b) All mechanical equipment is to be fitted with an emergency stop (e-stop) button in a prominent, adjacent, and easy to
reach location and clearly labelled with the equipment description / tag number.
c) Guarding is to be provided where necessary to prevent access to moving parts during operation.
d) Interlocks shall be provided where necessary to protect personnel and / or equipment.
e) All equipment is to be designed for fail-safe operation.
2.3 Location of Equipment
All equipment, including valves, instruments, fittings, etc., must be easily accessible (i.e. between floor level and 1.2 m above floor
level) without the need for specialist access equipment (i.e. ladders, elevated work platforms, etc.).
2.4 Design Life
Table 2 summarises the compulsory design life required for key components. The design life for items that do not fall in one of the
categories below is to meet or exceed best practice for the water industry in Australia, including reference to all relevant Australian
Standards, WSAA Codes, NSF/ANSI requirements, Australian Drinking Water Guidelines and all other relevant regulations and
guidelines.
Table 2 – Design life of key components
Component Design Life (years)
Concrete structures >40
Buildings >40
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Component Design Life (years)
Tanks (including roof) >25
Pond liner >25
Pipework, fittings and valves >20
Protective coatings >15
Pumps >15
Electrical and control >15
Instruments >10
2.5 Materials of Construction
Table 3 summarises the minimum requirements for materials of construction. The materials of construction for items that do not fall
in one of the categories below is to meet or exceed best practice for the water industry in Australia, including reference to all
relevant Australian Standards, WSAA Codes, NSF/ANSI requirements, Australian Drinking Water Guidelines and all other relevant
regulations and guidelines.
Table 3 – Minimum requirements for materials of construction
Area Material
All wetted components PVC, PE100 or 316 stainless steel
Fasteners Hot dipped galvanised or 316 stainless steel
Steel tanks Colorbond steel with liner for treated water.
Steel frames and supports Hot dipped galvanised or 316 stainless steel
Plastic tanks HDPE
Chemical systems As per Australian Standards and manufacturer’s recommendations
Control panels 316 stainless steel
Thread protection Grease, denso tape or nickel based antiseize shall be applied to all threads in accordance with industry best practice.
NOTES:
Please note painted mild steel or zinc plated steel is not acceptable.
2.6 Sampling and Drain Points
The plant shall be designed with sufficient drainage and sampling points. Sampling points are to be easily accessible and located on
all major process streams. Drain points in pipework should be designed to facilitate removal of equipment with minimal spillage.
Temporary hoses may be used to direct liquid from drain points to permanent drains.
2.7 Chemical Storage and Dosing
Chemical dosing systems for the WTP are to be selected by the Contractor to ensure the compliance with the process requirements
whilst minimising operating costs; also considering the chemical availability and supply options for the region. All chemical storage
to be sized for 30 days storage based on design capacity, with an additional 20% spare capacity to allow refill.
All chemical shall be bunded as per the requirements of the associated Australian Standards for the safe use and storage of
chemicals, hazardous chemical and other chemicals, and the appropriate safety equipment must be installed and functional prior to
the delivery of chemicals to site. Chemicals shall be stored in a covered area.
Appropriate spill stations, eyewashes and safety showers must be supplied in accordance with the required Australian Standards for
the storage and use of chemicals.
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2.8 Electrical
All electrical installations must comply with AS/NZS 3000. All electrical control and instrumentation must operate on extra low
voltage (24 VDC) unless specifically approved by the Principal. All electrical enclosures are to be rated to IP 56 as a minimum.
In order to minimise plant downtime, there a number of key areas with respect to electrical hardware that should be considered.
2.8.1 Instrumentation
All instrumentation is to be provided with a local display and connected to the PLC / SCADA. Furthermore:
a) All instruments to be 24VDC
b) All instrumentation to be easily accessible for both maintenance and to read/adjust the display.
c) All instrumentation to be installed as required by the manufacturer (e.g. all flow meters must allow for appropriate straight
pipe lengths before and after the meter).
d) All instrumentation must have a suitable cover to protect the display screen from UV exposure as well as to allow ease of
reading.
e) All pumped fluids shall have backup flow switch protection in addition to flow meter monitoring
Good quality instrumentation such as E&H or Hach should be installed to minimise faults and downtime.
2.8.2 Soft starters
All non VSD drives larger than 7.5kW must be fitted with a soft starter. Each soft starter shall have,
1. Inbuilt thermal overload
2. Adjustable current ramp rates
3. RUN and FAULT output contact signals to the PLC
4. Contactor bypass
2.8.3 Surge protection
Lightning and surge protections shall be provided to all instruments and equipment that could be potentially damaged by voltage
spikes.
2.9 Automation and Control Functionality
The plant shall be controlled by a master PLC which will provide the required monitoring and control signals to the plant equipment.
Given that the system will largely operate unattended, it is imperative that it identifies equipment faults and alarms in the system to
provide equipment protection.
2.9.1 Sequencing control
An automated sequence is a series of programmed steps that are executed by the required process equipment. The PLC will control
and monitor the pre-determined energising/de-energising of each piece of equipment based on the programmed sequence logic.
The system will ensure that no automated sequence proceeds under the following conditions:
a) Any of the process equipment required is in fault or unavailable.
b) Any of the process equipment required is not in auto (where duty/standby equipment is available, at least one must be in
auto).
c) The process is not initiated by the PLC or manually by the operator.
In the event that the sequence is unable to proceed, a process sequence alarm will be generated in the alarm banner or the SCADA
terminal specifying the reason for the sequence failure. The respective sequence will be aborted and the associated sub system will
be placed into “shutdown” or “fault”.
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2.9.2 Fault discrepancy logic
Fault discrepancy logic is required for each drive/machinery item to ensure that all process equipment operates in accordance with
the control logic. This logic is initiated upon request of the said equipment to start/stop or open/close. If appropriate feedback is not
received within a pre-determined time frame, the PLC will output FAILED, e.g. “P301 pump failed to start”.
2.9.3 Power failure
In the event of a power failure, the plant will cease to operate. Upon restoration of mains power, the PLC’s must restart all process
sequences automatically without operator intervention. An alarm must be generated in the SCADA alarm banner for power failures.
2.9.4 Alarms
All analogue inputs from the field will require High High and Low Low alarms as well as High and Low warnings. These alarms shall be
operator adjustable and can be accessed by clicking on the respective analogue signal on the SCADA. High/Low warnings should act
as an advisory, indicating to the operator that the given process value is nearing its respective alarm level. HighHigh/LowLow alarms
will typically shutdown the respective process they are associated with. The shutdown of any process due to alarm or equipment
failure/faults should generate a separate shutdown alarm. When configuring alarms the system will ensure that:
a) Analogue alarm/warning setpoints are not written to by any other functions in the PLC code other than the respective
analogue pop up.
b) Alarms are to latch in the PLC, only resettable by operator.
c) Warnings are not required to latch and can self-reset upon returning below the specified High or Low setpoint.
2.9.5 SCADA
The SCADA system will display control, data logging, indicating, alarming and reporting of the plants PLC control system,
communication system and other systems associated with the plant in accordance with industry best practice. The SCADA layout
should include mimic pages that follow a logical process sequence. The screens shall be easily viewed with text and data easy to
read.
The preference will be that trending shall be configured to allow for historical trending of all key process performance parameters
for 12 months. All flow rates shall have totalisers for the following time instances,
a) Today.
b) Yesterday.
c) This month.
d) Previous month.
e) Cumulative total.
The Contractor shall supply an SMS paging service either hardware or software based that will alert the required persons under the
following conditions:
a) Process Area Shutdown alarms; and
b) Critical Control Point alarm.
Each sub system of the plant shall have its own display page on the plant SCADA. The system will ensure that each sub system (each
train) has its own pop up which will display the following,
a) Sub system setpoints and control values (all setpoints must have appropriate engineering limits set to avoid setpoints being
entered outside the allowable limit)
b) Enable/Disable selection by the operator, this selection must not be written to by any other function in the PLC code.
c) Permissive/interlock display, indicating the state of all permissive’s required for the sequence to proceed.
d) Ready/Not ready indication.
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3 DESIGN BASIS
The following section outlines the design basis for the WTP.
3.1 Feed Water Quality
The EIS water is ultimately supplied by Melbourne Water. Table 4 provides a summary of the EIS water quality based on the
information provided by Melbourne Water.
Table 4 – Key Feed water quality parameters as provided by Melbourne Water
Parameter Units Max Min Average
Alkalinity mg/L 86 40 56.67
Aluminium mg/L 0.13 0.05 0.07
Ammonia (Ammonia as N) mg/L 0.2 0.1 0.10
Barium mg/L 0.005 0.003 0.00
Biochemical Oxygen Demand mg/L 4 2 2.29
Boron mg/L 0.13 0.06 0.10
Calcium mg/L 23 16 18.60
Chloride mg/L 180 120 157.50
Chromium mg/L 0.045 0.002 0.01
Coliphage somatic ORGC 1 1 1.00
Copper mg/L 0.016 0.007 0.01
Cryptosporidium oocyst/50L 68 2 18.50
E. coli (Colilert) orgs/100mL 1 0 0.04
Electrical Conductivity – Field uS/cm 950 670 848.89
Electrical Conductivity – Lab uS/cm 900 880 886.67
Enterococci ORGC 5 0 0.10
Fluoride mg/L 0.87 0.64 0.77
Giardia CY/L 2 2 2.00
Iron (Dissolved) mg/L 0.11 0.04 0.07
Lead mg/L 0.001 0.001 0.00
Lithium mg/L 0.02 0.02 0.02
Magnesium mg/L 13 8.3 11.05
Manganese (Dissolved) mg/L 0.006 0.001 0.00
Nitrate mg/L 23 8.6 14.04
Nitrate plus Nitrite mg/L 23 8.6 14.04
Nitrite mg/L 0.03 0.01 0.01
Nitrogen (total) (TCN) mg/L 25 11 15.76
OIL & GREASE – liquid mg/L 5 5 5.00
pH – Lab pH Units 7.3 6.3 6.87
Potassium mg/L 37 18 28.33
SAR meq/L 5.4 4.3 4.96
Sodium mg/L 120 85 109.36
Strontium mg/L 0.09 0.079 0.08
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Parameter Units Max Min Average
Sulphate mg/L 74 48 59.67
Suspended Solids mg/L 3 1 1.37
Total Dissolved Solids mg/L 520 380 456.40
Total Kjeldahl Nitrogen as N mg/L 2.5 0.8 1.71
Total Organic Nitrogen mg/L 2.5 0.8 1.70
Total PAH's mg/L 0.001 0.001 0.00
Total Phosphorus as P mg/L 8.8 3.1 6.40
True Colour Pt/Co 18 4 9.35
Turbidity – Lab NTU 1.3 0.1 0.61
The plant design to allow for the range of water qualities as presented, ensuring there is minimal change in plant performance even
at the maximum feed water qualities.
If required, the EOI submission to indicate any additional water quality parameters required that may influence the final design,
including the justification.
3.2 Design Flow Characteristics
The WTP is designed for a capacity of 250 kL/day product water. The design will take into account the allowance for a 5% blending in
the treated water, with the RO capacity adjusted accordingly to accommodate this. This recycle ratio is based on achieving the limiting
nutrient specification. The design will, however, allow for up to 30% blending to accommodate scenarios where the nutrient target
can be relaxed. Under this scenario the WTP will be able to produce 310 kL/day of treated water. It is proposed that the EIS transfer
pipeline is designed for 6 L/s to accommodate/offset short disruptions in supply as well as to cater for future potential scenarios.
Table 5 provides a summary of the recommended design basis for the key process components.
Table 5 – Design flow characteristics basis summary
Parameter Units Value Comment
EIS transfer line to WTP L/s 6 EIS transfer pumps and supply line to be sized for 6L/s to
offset times when there is a brief interruption in supply.
WTP Treated Water Capacity
(including blending) kL/day 250
The design to allow for a maximum treated water transfer
of up to 320 kL/day to the irrigation storage to
accommodate the higher blending ratio for the relaxed
nutrient scenario (this may be accommodated by
operating the proposed WTP Treated Water standby
pump).
RO recovery % 80
Plant design water balance and equipment sizing based on
80% RO recovery, however RO design to allow it to
operate up to 85% recovery, which will provide some
efficiency and capacity improvements.
Blending ratio % Up to 30% of
RO permeate
Under normal conditions the blending ratio will be 5 to
10% of the RO permeate, however design to allow
blending up to 30% of the RO permeate to accommodate
scenarios where the nutrient target can be relaxed.
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Parameter Units Value Comment
Media filter kL/day 330 kL/day
The pre-treatment Media filters to be configured as two
filters in a 2 x 100% arrangement under design conditions.
Under higher blend ratios the filters will operate in parallel
to achieve the increased flow.
Irrigation pumps L/s
42 L/s @ 600
kPa discharge
pressure
The irrigation pumps to be configured as two duty pumps
achieving the design capacity, with a third standby pump
of the same design capacity as a single pump.
3.3 Treated Water Requirements
The required treated water quality (irrigation water) are provided in Table 1, with the following additional requirements as
presented in Table 6:
Table 6 – Additional treated water quality targets
Parameter Unit Specification (100’%tile)
Free Chlorine 1, 2 mg/l 0.3 to 1.0
Langelier Saturation Index (LSI) 2 -- -1.0 to -0.5
Calcium Carbonate Precipitation Potential (CCPP) 2 -- -5.0 to -1.0
NOTES:
1. A free chlorine residual is to be maintained within the irrigation storage tank.
2. Measured at the outlet of the Irrigation tank
3.4 Plant Availability
The design will have potable top-up to the new irrigation tank, which ensures a high level of availability in terms of irrigation supply.
The following approach is proposed in terms of equipment availability with respect to the WTP equipment:
Due to the potential time required for replacement and the location of the site, it is proposed to include a duty/standby
configuration for the EIS Transfer Pumps (to be supplied by others – refer Section 3).
All process critical equipment to have installed redundancy or shelf spares unless considered to be a low risk.
o Where only duty pumps are installed, space to be allowed for an additional pump to be installed in the future.
Non-process critical equipment to either carry shelf spares and/or critical spares or ensure that equipment change-
over/restoration can be completed with a 48 hour period to minimise downtime.
General approach is for the plan to have a 95% availability based on peak production period.
3.5 Treatment Process
The treatment process is to consist of a reverse osmosis process with associated pre-treatment and post-treatment infrastructure to
provide water at a suitable quantity and at a suitable quality as per Section 3.3. The process design summary is provided in Table 7
with the PFD provided in Appendix A and the P&IDs in Appendix B.
Table 7 – Treatment solution process summary
Unit operation Purpose / Comment
EIS Transfer Pump Station
Extraction from the EIS distribution pipe line is required to be via gravity. Consequently the design has allowed for a transfer pump station to be installed alongside the EIS extraction point to pump the water to the WTP. The pump station will be located within the Cranbourne Racecourse grounds.
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Unit operation Purpose / Comment
Design, Supply and Installation of the pump station is by others (including piping to WTP), however WTP contractor to design, supply and install communication and control requirements with the pump station.
FROM HERE ONWARDS PART OF WTP CONTRACTOR SCOPE AND INCLUDED IN THIS EOI SCOPE
Feed Tank Used as a feed balance tank to ensure a reliable continuous supply to the WTP.
Media filtration
Provides pre-treatment for the RO. Filer media (e.g. sand) or similar is used to trap suspended solids within the media. The RO operation and performance is extremely sensitive to any suspended solids within the water. The requirement for this process step will be determined during detailed design with the potential of more advanced pre-treatment required before the RO.
Reverse Osmosis (RO)
Salt and nutrients will be reduced via an RO unit or similar to acceptable levels for irrigation. Reverse osmosis is a mechanical method of reversing the natural osmosis process in order to remove dissolved minerals, salts, organic molecules and other contaminants. Water from the concentrated (feed) solution is forced through semi-permeable membranes into a more dilute solution (permeate). In order to accomplish this flow reversal, a high pressure pump is used to increase the feed pressure in excess of the osmotic pressure.
Bypass / blending
This will be used to control the nutrient level within the final treated water as well as providing additional capacity without requiring all the water to be processed by the RO. Typically RO direct water is corrosive (low dissolved salt content), with the blending also allowing the final water quality to be stabilised (partial) for distribution.
Calcite Filters Calcite filters are proposed to manage the corrosion potential of the water and partially return some hardness and alkalinity into the water.
Brine disposal storage tank To manage the load on the sewer network, the waste water will be transferred to the existing sewage pump station at the Northern end of the car park. Brine will be stored through the day and discharged at night (i.e. from 12pm to 4am).
Chemical dosing systems
Scaling of RO membranes may occur when sparingly soluble salts are concentrated within the elements beyond their solubility limit. To minimise scaling, the feed to the RO is dosed with an antiscalant to limit the precipitation of problematic compounds. Antiscalants are surface active materials that interfere with precipitation reactions.
Polyamide-based RO membranes are subject to damage upon exposure to chlorine or other oxidising agents. Sodium Bisulphite (SBS) is a commonly used chemical reducing agent that destroys chlorine. SBS will be dosed in the feed to de-chlorinate the feed before the RO (NOTE: the Class A water will have a residual free chlorine level requiring neutralisation).
Biocide will be dosed to limit the biological fouling potential of the water, for both pipes and process equipment.
With the water sourced from wastewater, alternative option to be considered for chloramine dosing (or only free chlorine) to limit biological fouling of the RO membranes.
A stabilisation pH correction and/or corrosion inhibitor is recommended for further stabilisation of the treated water, after the calcite filters, provided there is no impact on the treated water quality for irrigation.
Sodium hypochlorite dosing is required to maintain a residual level of disinfection in the water to minimise any biological re-growth within the storage as well as the distribution network.
FROM HERE ONWARDS EXCLUDED FROM WTP CONTRACTOR SCOPE AND NOT PART OF THIS EOI SCOPE
Irrigation day tank Provides a buffer feed to the new irrigation pumps. This allows for maintenance activities within the treatment plant by buffering the
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Unit operation Purpose / Comment
instantaneous irrigation demand. The water is pumped to the new irrigation tank from the WTP and supplies feed to the new irrigation pumps.
NOTE: Although the tank will be supplied BY OTHERS, it will be the
contractors responsibility for the following:
Supply pipeline to tank.
Connection of potable top-up to tank, including all backflow
prevention requirements.
Supply of chlorine dosing system for hypochlorite recirculation
loop.
Design, supply and installation (including connection) of new
irrigation pumps located within the new building).
Control communication with the tank and associated systems.
3.6 General Requirements
A purpose-built new building (shed based design) is to be constructed for the Water Treatment Plant BY OTHERS. All WTP
equipment (excluding storage tanks) is to be inside the building, with a proposed foot print of 12m x 18m.
The reference building general arrangement (GA) is provided in Appendix C.
The overall site layout is provided in Appendix D.
Although the building is BY OTHERS, the contractor is to:
Advise the client if a larger footprint is required.
Take on all responsibility for site and building permits if a larger footprint is required.
Under all scenarios, provide the civil design of the floor plan, including pump/equipment plinths, drains, sumps (including
external to the building) and any required below slab conduits/piping.
.
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4 SCOPE OF WORK
The following Table 8 outlines the scope of work for the project, which is separated into four distinct Work Packages.
Table 8 – Scope of work for different packages
Description / Scope Inclusions / Termination points
Below ground EIS extraction point
Flange provided by Trility. BY OTHERS
Package #1 (WP1): EIS to Cranbourne Gardens (CG)
Connection to EIS supply flange.
Pump station at Cranbourne Training Complex (CTC).
Power supply at CTC from provided connection point.
Instrumentation installation (instrumentation issued as part of Package #2).
CTC transfer pumps.
Discharge pipeline from CTC to CG nominated connection point on new WTP site (within 1m of feed tank).
Sewer discharge line from nominated point on new WTP site to proposed sewer connection point.
Design, construct, and commission.
Civil and structural works (where applicable).
Electrical, instrumentation and control.
Power to pumps and instrumentation.
Supply and installation of mechanical equipment.
TP#1: Inlet connection from EIS termination point
TP#2: Design, supply and install of all pipework to within 1m of inlet flange connection of feed tank in Package #2.
TP#3: Design, supply and install of all pipework from within 1m of discharge flange connection of waste transfer pump from Package #2.
PACKAGE #2 (WP2): Water Treatment Plant
THIS EOI18/003
(includes power, telemetry, potable water and other connections):
WTP, using provided building footprint.
Provide instrument for extraction pump station to be installed by Package #1 contractor (to ensure common equipment).
All feed and intermediate storage tanks (as required), including waste tank.
All connections to new 500kL irrigation tank (supplied BY OTHERS).
Irrigation tank chlorine dosing recirculation loop.
New irrigation supply pumps.
Potable top-up to new irrigation tank.
Irrigation supply to existing irrigation main.
Control, including integration of CTC pump station, irrigation tank, chlorine dosing loop and irrigation pumps (including hardware, software and equipment requirements at the remote sites).
MCC and DB for connection within 1m of pump shed.
Design, construct, and commission of all aspects associated with the WTP as part of this scope.
Design (including drawings) of the building slab along with any hard stand requirements around the building for the storage tanks.
Design, construct, and commission plant sump.
TP#2: Design, supply and install connection from incoming EIS supply line provided by Package #1 to feed tank.
TP#4: Design, supply and installation of all pipework to connect to nominated inlet flange on new irrigation tank.
TP#3:1m from discharge of waste transfer pump to connect to Package #1.
TP#5: Design, supply and install connection from nominated outlet flange from new irrigation tank to new irrigation pumps.
TP#6: Design, supply, install and commission new potable water offtake connection into existing potable water supply connection to existing irrigation pumps within existing irrigation pump shed.
TP#7: Design, supply and install connection of potable water supply to nominated irrigation tank inlet flange, along with required backflow prevention and air gap.
TP#E2: Incoming electrical supply within 1m of WTP building. Electrical load to be specified by contractor.
Commissioning and water testing of new irrigation tank.
TP#8: Flange connection on irrigation tank for chlorine recirculation loop.
TP#9: Design, construct, and commission a chlorine dosing loop.
TP#10: Design, supply, install and commission new irrigation water supply line from discharge of new irrigation pumps to connect to existing irrigation supply line within existing pump
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Description / Scope Inclusions / Termination points
shed; including the disconnection of the existing irrigation supply line from the existing irrigation pumps.
TP#11: Flange connection on irrigation tank for filter backwash pump suction.
PACKAGE #3 (WP3): Treatment Shed
RBGV to:
Specify shed footprint
Tender and purchase shed
Obtain planning permit
Obtain building permit
Manage building installation including slab
WTP Contractor:
Design the plant to fit within the building footprint and to handle all costs if changes required.
Provide building slab design (drains plinths etc) during detail design which will be used for the building construction.
Design and construction of treatment building.
PACKAGE #4 (WP4): Irrigation tank (500 KL).
Separate package, with specification included penetration requirements.
WTP contractor to provide tank penetration requirements, including size, location and flange requirements.
Design and construction of irrigation tank.
4.1 Work Package #2 Termination Points
The following table provides a summary of the proposed termination points (as detailed in Table 8) for Work Package #2.
Table 9 – Termination points schedule
Termination Point # Element Details / Interface
TP#2 EIS supply line to WTP
WP1 / WP2 interface.
Within 1m on ground level of WTP feed
tank.
TP#3 Waste discharge line WP2 / WP2 interface.
Within 1 m of waste transfer pump.
TP#4 Treated water supply
WP2 / WP4 interface.
Connection of treated water from WTP
to inlet flange of new irrigation tank.
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Termination Point # Element Details / Interface
TP#5 Irrigation pump suction
WP4 / WP2 interface.
Connection from new irrigation tank
outlet flange for suction of new irrigation
pumps.
TP#6 Potable water supply
Existing / WP2 interface.
Connection from potable water supply
within existing irrigation pump shed to
new potable supply line to WTP.
Refer to Appendix D for in-gardens
pipeline route and Appendix E for
existing pump shed.
TP#7 Potable top-up connection
WP2 / WP4 interface.
Connection of new potable top-up line to
inlet flange on new irrigation tank
connection (with required air gap
requirement).
TP#8 Chlorine loop supply
WP4 / WP2 interface.
Chlorine loop suction line from new
irrigation tank outlet connection.
TP#9 Chlorine loop return
WP2 / WP4 interface.
Chlorine loop return to new irrigation
tank inlet connection (option to return
directly into treated water supply line).
TP#10 Irrigation water distribution
WP2 / Existing
Irrigation water supply line from
discharge of new irrigation pumps to
existing irrigation main distribution line
within existing irrigation pump shed.
Pipe to follow same pipe trench as
potable water supply with required
separation distance.
Refer to Appendix D for in-gardens
pipeline route and Appendix E for
existing pump shed.
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Termination Point # Element Details / Interface
TP#11 Filter backwash supply
WP4/WP2
Media filter backwash pump suction line
from new irrigation tank outlet.
(This may be the same suction as the
irrigation pumps, provided correct
capacity and suction pressures are
maintained)
4.2 Work Package #2 Task Summary
Work Package 2, which is the scope as part of this EOI) shall include (but not be limited to), the following main work tasks to be
executed:
EIS Transfer Pump station:
o Supply of instrumentation
o Radio and/or mobile internet communications connection to the Water Treatment Plant.
Feed storage
o 45 kL feed storage tank or as required to balance flow between supply and plant feed.
o Biocide or hypo dosing to minimise risk of biological growth/fouling. Chloramine dosing may also be considered.
Pre-Treatment Infrastructure which may include:
o 2 x 100% Multimedia filter pumps sized as per Section 3.2.
o 2 x Multi-media filters sized as per Section 3.2.
o 1 x Filter backwash pump.
o Blend flow/quality control.
RO plant which may include:
o Cartridge filtration.
o RO HP Pump.
o RO Trains sized as per Section 3.2 to meet the maximum specified recovery and design capacity
o CIP System, including allowance for permeate flush at shutdown.
o 1 x CIP/Flush tank.
o 1 x CIP/Flush pump.
o Antiscalant dosing system.
o SBS dosing system.
Post-Treatment Infrastructure may include:
o Calcite filters or as required to meet specifications in Section 3.3.
o Stabilisation dosing system (typically caustic) or as required to meet specifications in Section 3.3.
o Sodium hypochlorite dosing to maintain residual in supply to irrigation storage.
Irrigation storage may include:
o Sodium hypochlorite dosing recirculation loop to maintain fee chlorine residual within irrigation storage tank as
per specifications in Section 3.3.
o Potable top-up as per in-gardens pipeline route in Appendix D.
o Relocation of RBGV potable supply connection.
o New irrigation supply pumps sized as per Section 3.2.
o Irrigation water supply line as per in-gardens pipeline route in Appendix D.
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APPENDIX A – REFERENCE PROCESS FLOW DIAGRAM (PFD)
ANITSCALANTSBS
FROM EIS PIPELINE
POTABLE WATER
AIT
FEED TANK
HYPOCHLORITE
MEDIA FILTER
FEED PUMP
IRRIGATION TANK
CHLORINE
RECIRCULATION
PUMP
HYPOCHLORITE
CALCITE FILTER
DOSING
STABILISATION
FILTER BACKWASH
PUMP
MEDIA FILTER 1
MEDIA FILTER 2
WASTE TANK
BACKWASH WASTE
BLEND
CARTRIDGE
FILTER
TO SEWER
AIT
AIT
CIP WASTE
AIT
CIP / FLUSH
PUMP
ROC
CIP / FLUSH
TANK
IRRIGATION
VENDOR
CIP
HEATER RO
P
AIT
1
NOTES:
QUALITY CONTROL POINTS.
1
1
1
1
1
1
AIT
1
RO
HP PUMP
2
2
OPTIONAL, OPTION FOR BIOCIDE DOSING.
WASTE TRANSFER
PUMP
IRRIGATION PUMPS
HYPOCHLORITE
RO UNIT
AIT
TP
02
TP
11
TP
04TP
08
TP
07
TP
03
TP
05
TP
08
WATER TREATMENT PLANT
SYN 20/11/17DE 2011/17
NTS
PROCESS FLOW DIAGRAM
A 20/11/17 SYN DE INITIAL ISSUE
SCALE
PERMEATE PROJECT # PERMEATE DRAWING #
CLIENT PROJECT # CLIENT DRAWING #
SHEET
A3
Date
Design Drafting
Date
C17204 C17204-P-100
S:\Shared\Internal\Production\Permeate Partners\Royal Botanic Garden-Cranbourne WTP\Working Files\PFD\C17204-P-100.dwg
This document is and shall remain
the property of Permeate Partners
Pty Ltd. The document may only be
used for the purpose for which it
was commissioned in accordance
with the terms of engagement for
the commission. Unauthorised use
of this document in any form is
strictly prohibited. © Permeate
Partners Pty Ltd 2018. All rights
reserved.
PROJECT:
CLIENT
NO. DATE DRAFTER DESIGN MGMT DESCRIPTION
NAME :
P: 1300 799 155
W : www.permeate.com.au
NEWCASTLE, SYDNEY, MELBOURNE, PERTH
PERMEATEP A R T N E R S
COPYRIGHT
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CRANBOURNE WTP
B 05/04/18 SYN PG ISSUED FOR REVIEW
C 23/05/18 SYN PG ISSUED FOR EOI
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PAGE 19 OF 22
APPENDIX B – PIPING AND INSTRUMENTATION DIAGRAM (P&ID)
EQUIPMENT
VERTICAL IN-LINE PUMP
SUBMERSIBLE PUMP
METERING DOSING PUMP
CENTRIFUGAL PUMP
DIAPHRAGM PUMP
GEAR PUMP
POSITIVE DISPLACEMENT
(ROTARY LOBE)
COMPRESSED AIR DRYER
AIR COMPRESSOR
CENTRIFUGAL BLOWER
FINE BUBBLE
DIFUSERS
COARSE AIR DIFFUSER
IN-LINE MOTIONLESS MIXER
STRAINER, FILTER OR COALESCER
AIR FILTER/SILENCER
SUBMERSIBLE MIXERM
CALIBRATION COLUMN
CARTRIDGE FILTER
RO UNIT
M
FINE SCREEN
STRAINER - IN TANK
PRESSURE DIAPHRAGM SEAL
Y-STRAINER
PULSATION DAMPENER
UV DISINFECTION UNIT
M
MACERATOR
M
PACKAGED ODOUR
CONTROL SYSTEM
MF UNIT
MEMBRANE MODULE
VALVES & ACTUATORS
AIR RELIEF VALVE (ARV)
COMBINATION AIR VALVE (AVRV)
BALL CHECK VALVE (BCV)
BUTTERFLY VALVE (BFV)
BACK PRESSURE CONTROL VALVE (PCV)
SOLENOID VALVE (SV)
BALL VALVE (BV) **
PLUG VALVE (PV)
VENTED PLUG VALVE (PV)
CHECK VALVE (CV)
KNIFE GATE VALVE (KGV)
FLANGED DIAPHRAGM VALVE (DV)
DIAPHRAGM VALVE (DV)
FLOAT VALVE (FV)
GLOBE VALVE (GLV)
GATE VALVE (GV)
3 WAY VALVE (MPV)
NEEDLE VALVE (NV)
PRESSURE CONTROL VALVE (PCV)
4 WAY VALVE (MPV)
PRESSURE RELIEF VALVE (PRV)
SWING CHECK VALVE (SCV)
CYLINDER ACTUATOR
DIAPHRAGM ACTUATOR
ELECTRO HYDRAULIC ACTUATOR
ELECTRO PNEUMATIC ACTUATOR
MANUAL ACTUATOR
MOTOR ACTUATOR
SOLENOID ACTUATOR
POSITIVE DISPLACEMENT FLOW METER
NORMAL LIQUID LEVEL
MAGNETIC FLOW METER
ULTRASONIC LEVEL SENSOR
ROTAMETER WITH INTEGRAL
NEEDLE VALVE
ROTAMETER
FI
FI
RUPTURE DISC
BACK FLOW PREVENTER
PROCESS FLOW ABBREVIATIONS
AC COMPRESSED AIR
ACID ACID
AD DIGESTER AIR
AP PROCESS AIR
AR AIR RECEIVER
AS SCOUR AIR
BD BIOLOGICAL TANK DRAIN
BW BACKWASH SUPPLY
C CENTRATE
CAD COMPRESSED AIR DRYER
CF COALESCING FILTER
CH CHEMICAL FROM DRUM
CIP CLEAN IN PLACE
CIT CITRIC ACID
COAG COAGULENT
CS / CR CLEANING SUPPLY / CLEANING RETURN
D DRAIN
DS DIGESTED SLUDGE
DWS DEWATERED SLUDGE
FA FOUL AIR
FD FLOOR DRAIN
FI FILTRATE
HYPO SODIUM HYPOCHLORITE
MD MEMBRANE TANK DRAIN
MFE MF FILTRATE
MLF MIXED LIQUOR FEED
MLR MIXED LIQUOR RETURN
OF OVERFLOW
PLW PLANT WASTE
PO POLYMER
PTW POST TREATED WATER
RAS RETURN ACTIVATED SLUDGE
RS RAW SEWAGE
RW RECYCLE WATER
SCE SCREENED EFFLUENT
SH SODIUM HYDROXIDE
SOF FINE SCREENS OVERFLOW
SP SAMPLE
UV UV EFFLUENT
WAS WASTE ACTIVATED SLUDGE
PROCESS NOMENCLATURE
MF MEMBRANE FILTRATION
OIT OPERATOR INTERFACE TERMINAL
PC PNEUMATIC CONTROLLER
RO REVERSE OSMOSIS
RTU REMOTE TERMINAL UNIT
RIO REMOTE I/O
UF ULTRA FILTRATION
EQUIPMENT / FUNCTIONAL
IDENTIFICATION
ACMP AIR COMPRESSOR
BWR BLOWER
C CENTRIFUGE
CAD COMPRESSED AIR DRYER
CC CALIBRATION COLUMN
CMP COMPRESSOR
EDR EDUCTOR
F FILTER
FCV FLOW CONTROL VALVE
GDD GRAVITY DRAINAGE DECK
GRDR MACERATOR
M MECHANICAL EQUIPMENT
MP METERING PUMP
MX MIXER
P PUMP
PD PULSATION DAMPENER
PDS PRESSURE DIAPHRAGM SEAL
PPS POLYMER PREPARATION SYSTEM
S SUMP
SAM SUBMERSIBLE AERATOR MIXER
SCR SCREENS
SIL SILENCER
STR STRAINER
T TANK
VSD VARIABLE SPEED DRIVE
RO RO UNIT
MF MEDIA FILTER
CF COALESCING FILTER
= FAIL OPEN (FO)
= FAIL CLOSED (FC)
NOTE: DIRECTIONAL ARROW ON VALVE ACTUATOR
INDICATES FAILURE POSITION
** OPTIONAL VALVE DESIGNATION:
NC = NORMALLY CLOSED
NO = NORMALLY OPEN
INSTRUMENT AIR SUPPLY
EXHAUST
IAS
EXH
BV 1
NC
VENT
DRAIN
EDUCTOR
FLEXIBLE HOSE
REDUCER
EXPANSION JOINT
FLANGED CONNECTION
HOSE CONNECTION
QUICK CONNECT, CAMLOCK TYPE (QC)
PIPE MATERIAL CODES
C20 SCHEDULE 40 CARPENTER 20 ALLOY PIPE
CMLS CEMENT MORTAR LINED STEEL PIPE
CPVC SCHEDULE 80 CPVC PIPE
CS CAST IRON SOIL PIPE
CU COPPER TUBING
DI DUCTILE IRON PIPE
FRP 150 PSI PRESSURE CLASS FIBERGLASS REINFORCED PLASTIC PIPE
HDPE 150 PSI PRESSURE CLASS POLYPROPYLENE PIPE
PE POLYETHYLENE PIPE
PVC SCHEDULE 80 PVC PIPE
PVC/D PVC GRAVITY SEWER PIPE
PVDF 230 PSI PRESSURE CLASS PVDF PIPE
RCP REINFORCED CEMENT PIPE
SS TYPE 316/316L STAINLESS STEEL PIPE
SST STAINLESS STEEL TUBING
STL FABRICATED STEEL PIPE
STL/EL EPOXY LINED FABRICATED STEEL PIPE
PIPING SPECIALITY
FEEDBACK EQUIPMENT
T-STRAINER
INJECTION QUILL WITH
CORPORATION STOP
INJECTION QUILL WITH
INTEGRAL CHECK VALVE
HEATING ELEMENT
SECONDARILY
CONTAINED PIPING
BELT FILTER PRESS
MIXER VERTICAL
PROGRESSIVE CAVITY PUMP
AIR RELEASE VALVE (VA)
TREATMENT PROCESS AREA CODES
AREA TREATMENT PROCESS
00 PRETREATMENT
05 TREATED WATER
20 REVERSE OSMOSIS
40 CIP / BACKWASH
60 AIR COMPRESSOR
70 CHEMICAL DOSING
80 IRRIGATION
85 WASTE
SUBMERSIBLE AEREATOR
CENTRIFUGE FILTER
GRAVITY DRAINAGE DECK
ROTAMETER (RO)
M
ELECTRICAL ACTUATOR
E
PROGRESS PRINT
PROCESS AND INSTRUMENTATION DIAGRAM
WATER TREATMENT PLANT
LEGEND AND ABBREVIATIONS - I
NTS
A 13/12/17 SYN DEINITIAL ISSUE
SYN 13/12/17DE 13/12/17
B 23/05/18 SYN DEISSUED FOR EOI
SCALE
PERMEATE PROJECT # PERMEATE DRAWING #
CLIENT PROJECT # CLIENT DRAWING #
SHEET
A3
Date
Design DraftingDate
C17204 C17204-PID-200
This document is and shall remain
the property of Permeate Partners
Pty Ltd. The document may only be
used for the purpose for which it
was commissioned in accordance
with the terms of engagement for
the commission. Unauthorised use
of this document in any form is
strictly prohibited. © Permeate
Partners Pty Ltd 2018. All rights
reserved.
PROJECT:
CLIENT
NO. DATE DRAFTER DESIGN MGMT DESCRIPTION
NAME :
P: 1300 799 155
W : www.permeate.com.au
NEWCASTLE, SYDNEY, MELBOURNE, PERTH
PERMEATEP A R T N E R S
COPYRIGHT
ROYAL BOTANIC GARDENS
-
INSTRUMENT/DEVICE FUNCTION OR CONTROL DESCRIPTORS
ANALYTICAL DESCRIPTORS
CL2 FREE CHLORINE
COND CONDUCTIVITY
DCL2 DECHLORINATION ANALYZER
DP DIFFERENTIAL PRESSURE
LEAK LEAK DETECTION
NH3 AMMONIA
ORP OXIDATION REDUCTION POTENTIAL
PART PARTICLE COUNTER
pH
HYDROGEN ION CONCENTRATION
TCL2 TOTAL CHLORINE
TEMP TEMPERATURE
TURB TURBIDITY
TDS TOTAL DISSOLVED SOLIDS
SWITCH/DEVICE DESCRIPTORS
AK OR ACK ACKNOWLEDGE
ANN ANNUNCIATOR
ES EMERGENCY STOP
H/O/A HAND-OFF-AUTOMATIC
J/O/R JOG-OFF-REMOTE
L/O/R LOCAL-OFF-REMOTE
LO/S LOCKOUT/STOP
L/R LOCAL/REMOTE
M/A MANUAL-AUTOMATIC
O/C OPEN-CLOSE
O/C/R OPEN-CLOSE-REMOTE
O/O ON-OFF
O/O/A ON-OFF-AUTO
O/O/R ON-OFF-REMOTE
O/S/C OPEN-STOP-CLOSE
PB PUSHBUTTON
POS POSITIONER OR POSITION
POT POTENTIOMETER
SEL SELECTOR
S/S START-STOP
A C14118-P-XXX
XXX
XXXXXX
PAGE CONNECTOR
INDICATES DIRECTION OF FLOW
EQUIPMENT/SYSTEM REFERENCE
PROCESS STREAM
CONTINUATION DRAWING NO.
INTERFACE COORDINATION
ALPHA DESIGNATION: PROCESS LINE CONTINUATION
NUMBER DESIGNATION: CONTROL LINE CONTINUATION
CONNECTOR SHOWS PROCESS FLOW CONTINUES ON
DRAWING C14118-P-XXX AT INTERFACE A
BC14118-P-XXX
XXX
XXXXXX
BI-DIRECTIONAL PAGE CONNECTOR
INDICATES BI-DIRECTIONAL FLOW
EQUIPMENT/SYSTEM REFERENCE
PROCESS STREAM
CONTINUATION DRAWING NO.
INTERFACE COORDINATION
ALPHA DESIGNATION: PROCESS LINE CONTINUATION
NUMBER DESIGNATION: CONTROL LINE CONTINUATION
CONNECTOR SHOWS PROCESS FLOWS TO AND FROM
DRAWING C14118-P-XXX AT INTERFACE B
MAJOR PROCESS PIPING OR FLOW CHANNEL
MINOR PROCESS PIPING OR COMPONENTS
FUTURE PIPING AND COMPONENTS
ARROW INDICATES DIRECTION OF PROCESS FLOW
PROCESS LINES CROSSING (NOT CONNECTED)
AIR PIPING
ELECTRICAL SIGNAL (DISCRETE)
INTEGRAL SYSTEM SIGNAL LINK (SOFTWARE OF DATA LINK)
ANALOG SIGNAL
ARROW INDICATES DIRECTION OF FLOW OF INFORMATION
SIGNAL CONNECTION POINT
PROCESS SYMBOLS
PIPING MATERIAL
( REFER LEGEND AND ABBREVIATIONS - I )
LINE SIZE (DN)
PROCESS FLOW
( REFER LEGEND AND ABBREVIATIONS - I )
TREATMENT PROCESS AREA CODE
( REFER LEGEND AND ABBREVIATIONS - I )
PIPE LINE NUMBERING
1ST & 2ND DIGIT 3RD DIGIT 4TH & 5TH DIGIT - 6TH DIGIT
05 3 01 - 1
TREATMENT
PROCESS
AREA CODE
SEQUENTIAL
NUMBERING
(00 - 99)
TRAIN NO.
(IF APPLICABLE)
SUB - AREA
0 TANKS
1 MECHANICAL EQUIPMENTS
2 INSTRUMENTS
3 VALVES
4 CONTROLS
5 OTHERS
VALVE TAG SYSTEM
M-05301-1GV-
VALVE TYPE
(REFER VALVES & ACTUATORS IN
LEGEND AND ABBREVIATIONS - I)
VALVE CONTROL
M MANUAL
P PNEUMATIC
E ELECTRIC
S SOLENOID
05102-2 P -
EQUIPMENT TYPE
(REFER EQUIPMENT / FUNCTIONAL IDENTIFICATION
IN LEGEND AND ABBREVIATIONS - I)
EQUIPMENT TAG SYSTEMINSTRUMENT TAG SYSTEM
AND
ADDITIONAL DESIGNATIONS
SUCCEEDING LETTERS
FIRST LETTER(S)
INSTRUMENT IDENTIFICATION
(REFER TABLE - ISA INSTRUMENT
SYMBOLS AND IDENTIFICATION)
NUMBER OF DUPLICATE INDICATORS OR DEVICES
INSTRUMENT FUNCTION OR CONTROL DESCRIPTOR
(REFER INSTRUMENT/DEVICE FUNCTION OR CONTROL
DESCRIPTORS LIST)
PANEL REFERENCE NUMBER
ADDITIONAL FUNCTION DESCRIPTORS
SYSTEM I/O INTERFACE
DIRECTION OF ARROW INDICATES WHETHER IS INPUT OR OUTPUT
LETTERS, TAG NUMBERS, ABBREVIATIONS AND
OTHER ANNOTATIONS ARE SIMILAR TO THE ABOVE
INSTRUMENT TAGGING SYSTEM.
INDICATES PANEL MOUNTED INSTRUMENT
INSTRUMENT TAG
00 - RS - 300 - PVC
ISA INSTRUMENT SYMBOLS AND IDENTIFICATION
FIRST LETTER SUCCEEDING LETTERS
LETTER PROCESS OR INITIATING VARIABLE MODIFIER READOUT OR PASSIVE FUNCTION OUTPUT FUNCTION MODIFIER
A ANALYSIS ALARM
B BURNER FLAME
USERS CHOICE (*) USERS CHOICE (*) USERS CHOICE (*)
C CONDUCTIVITY CONTROL CLOSED
D
DENSITY (S.G.)
DIFFERENTIAL
E VOLTAGE PRIMARY ELEMENT
F FLOW RATE RATIO
G GAUGE GLASS GATE
H
HAND (MANUAL)
HIGH/HIGH-HGIH
I CURRENT INDICATE
J POWER SCAN
K TIME OR SCHEDULE CONTROL STATION
L LEVEL
LIGHT (PILOT)
LOW/LOW-LOW
M MOTION MIDDLE
N TORQUE
USERS CHOICE (*) USERS CHOICE (*) USERS CHOICE (*)
O
USERS CHOICE (*)
ORIFICE OPENED
P
PRESSURE (OR VACUUM) POINT (TEST CONNECTION)
QQUANTITY OR EVENT (*)
INTEGRATE INTEGRATE
R RECORD OR PRINT
S SPEED OR FREQUENCY SAFETY SPEED OR FREQUENCY SWITCH
T TEMPERATURE TRANSMIT
U
MULTIVARIABLE (*) MULTIFUNCTION (*)
V VISCOSITY VALVE
W WEIGHT OR FORCE WELL
X
UNCLASSIFIED (*) UNCLASSIFIED (*) UNCLASSIFIED (*) UNCLASSIFIED (*)
Y
USERS CHOICE (*) RELAY OR COMPUTE (*)
Z POSITION
DRIVE, ACTUATE OR UNCLASSIFIED
CONTROL ELEMENT
SCALE
PERMEATE PROJECT # PERMEATE DRAWING #
CLIENT PROJECT # CLIENT DRAWING #
SHEET
A3
Date
Design DraftingDate
C17204 C17204-PID-200
This document is and shall remain
the property of Permeate Partners
Pty Ltd. The document may only be
used for the purpose for which it
was commissioned in accordance
with the terms of engagement for
the commission. Unauthorised use
of this document in any form is
strictly prohibited. © Permeate
Partners Pty Ltd 2018. All rights
reserved.
PROJECT:
CLIENT
NO. DATE DRAFTER DESIGN MGMT DESCRIPTION
1 2 3 4 5 6 7 8
A
B
C
D
E
NAME :
P: 1300 799 155
W : www.permeate.com.au
NEWCASTLE, SYDNEY, MELBOURNE, PERTH
PERMEATEP A R T N E R S
COPYRIGHT
1 2 3 4 5 6 7 8
A
B
C
D
E
ROYAL BOTANIC GARDENS
-
PROCESS AND INSTRUMENTATION DIAGRAM
WATER TREATMENT PLANT
LEGEND AND ABBREVIATIONS - II
NTS
A 13/12/17 SYN DEINITIAL ISSUE
SYN 13/12/17DE 13/12/17
B 23/05/18 SYN DEISSUED FOR EOI
PROGRESS PRINT
MODEL : TBC
MOTOR : TBC
DUTY : 2X100%
BFV-M-00300
REMOTELY CONTROLLED FROM WTP.
NOTES:
1
BFV-P-00301
(T-00002)
TO WTP FEED TANK
C17204-PID-202A
CV-00303-1
CV-00303-2 BFV-M-00304-2
BFV-M-00304-1
P-00101
EIS TRANSFER PUMP STATION
1
RBGV
TRILITYLOCAL CONTROL
FROM EIS MAIN
TRILITY OFFTAKE
P-00102
ALL ITEMS SHOWN ON THIS DRAWING ARE LOCATED WITHIN THE CRANBOURNE RACECOURSE GROUND.2
AV-E-00302
T-00001
PROCESS AND INSTRUMENTATION DIAGRAM
SUPPLY SYSTEM
WATER TREATMENT PLANT
NTS
A 17/01/18 SYN DEINITIAL ISSUE
SYN 17/01/18DE 17/01/18
SCALE
PERMEATE PROJECT # PERMEATE DRAWING #
CLIENT PROJECT # CLIENT DRAWING #
SHEET
A3
Date
Design DraftingDate
C17204 C17204-PID-201
This document is and shall remain
the property of Permeate Partners
Pty Ltd. The document may only be
used for the purpose for which it
was commissioned in accordance
with the terms of engagement for
the commission. Unauthorised use
of this document in any form is
strictly prohibited. © Permeate
Partners Pty Ltd 2018. All rights
reserved.
PROJECT:
CLIENT
NO. DATE DRAFTER DESIGN MGMT DESCRIPTION
NAME :
P: 1300 799 155
W : www.permeate.com.au
NEWCASTLE, SYDNEY, MELBOURNE, PERTH
PERMEATEP A R T N E R S
COPYRIGHT
ROYAL BOTANIC GARDENS
-
B 23/05/18 SYN DEISSUED FOR EOI
PROGRESS PRINT
T-00002
FEED TANK
CAPACITY : 40kL
PUMP(MP70115)
FROM BIOCIDE DOSING
C17204-PID-208B
FROM EIS TRANSFER
C17204-PID-201B
IQ
-70358
BFV-P-00305
BFV-M-00307
BV
-M
-00308
P-00102-2
MEDIA FILTER
FEED PUMPS
MODEL : TBC
MOTOR : TBC
DUTY : 2X100%
CV -00310
MF-00103
MEDIA FILTER
DUTY : 1X100%
DUTY : 1X100%
BFV-M-00311
BV
-M
-00312
BFV-P-00313
MF-00104
MEDIA FILTER
BV
-M
-00314
PRV-00315
BFV-M-00325
BV
-M
-00326
BFV-P-00327
PRV-00328
BFV-P-00316 BFV-M-00317
(T-85001)
TO WASTE TANK
C17204-PID-204B
BFV-P-00330 BFV-M-00331BFV-M-00329
BV
-M
-00332
BFV-P-00320 BFV-M-00321BFV-M-00318
TO RO
C17204-PID-203A
GV
-M
-00322
BFV-P-00323GV-M-00324
BFV-P-00335 BFV-M-00336BFV-M-00333
BF
V-M
-00337
BFV-P-00338BFV-M-00339
PUMP (P-80103)
FROM FILTER BACKWASH
C17204-PID-206C
(T-05001)
TO TREATED WATER TANK
C17204-PID-205B
BFV-M-00340 BFV-P-00341CV -00342
BV
-M
-00306
SP
BV
-M
-00309
BFV-P-00319
BFV-P-00334
FLOW CONTROL BASED ON CONDUCTIVITY BLEND FEEDING PERMEATE TANK.
NOTES:
1
1
ZC
00217
P-00102-1
SCALE
PERMEATE PROJECT # PERMEATE DRAWING #
CLIENT PROJECT # CLIENT DRAWING #
SHEET
A3
Date
Design DraftingDate
C17204 C17204-PID-202
This document is and shall remain
the property of Permeate Partners
Pty Ltd. The document may only be
used for the purpose for which it
was commissioned in accordance
with the terms of engagement for
the commission. Unauthorised use
of this document in any form is
strictly prohibited. © Permeate
Partners Pty Ltd 2018. All rights
reserved.
PROJECT:
CLIENT
NO. DATE DRAFTER DESIGN MGMT DESCRIPTION
NAME :
P: 1300 799 155
W : www.permeate.com.au
NEWCASTLE, SYDNEY, MELBOURNE, PERTH
PERMEATEP A R T N E R S
COPYRIGHT
ROYAL BOTANIC GARDENS
-
PROCESS AND INSTRUMENTATION DIAGRAM
PRETREATMENT
WATER TREATMENT PLANT
NTS
A 17/01/18 SYN DEINITIAL ISSUE
SYN 17/01/18DE 17/01/18
B 23/05/18 SYN DEISSUED FOR EOI
PROGRESS PRINT
(PV-00103,00104)
FROM MEDIA FILTERS
C17204-PID-202B
PUMP (MP-70107)
FROM ANTISCALANT DSOING
C17204-PID-207C
PUMP (MP-70103)
FROM SBS DOSING
C17204-PID-207B
P-20102
CV -20304
RO HIGH PRESSURE
PUMP (HP)
MODEL : TBC
MOTOR : TBC
DUTY : 1X100%
CARTRIDGE FILTER
CF-20101
PRESSURE VESSEL 1-3
CAPACITY : TBC
RO-20105
PRESSURE VESSEL 4-5
CAPACITY : TBC
RO-20106
PRESSURE VESSEL 6
CAPACITY : TBC
GV-M-20311
GV-M-20316
(F-05103,F-05104)
TO CALCITE FILTERS
C17204-PID-205B
(T-85001)
TO WASTE TANK
C17204-PID-204B
IQ
-70359
IQ
-70360
TYPICAL
BV
-M
-20309
BV
-M
-20314
BV
-M
-20317
PUMP (P-20102)
FROM CIP
C17204-PID-210C
RO-20103
(T-40001)
TO CIP TANK
C17204-PID-210B
BV
-M
-20302
SP
BV
-M
-20306
SP
BV
-M
-20307
SP
SP
SP
BV
-M
-20308
SP
BV
-M
-20319
SP
BV
-M
-20322
SP
BV
-M
-20312
SP
BV
-M
-20313
SP
TYPICAL RO DESIGN SHOWN, CONFIGURATION TO BE CONFIRMED DURING DETAIL
DESIGN BASED ON VENDOR PACKAGE.
NOTES:
1
RO-20102
RO-20101
RO-20104
CONCENTRATE RECYCLE
1
BFV-M-20321
BFV-M-20324
BV
-M
-20325
SP
NV-M-20327
NV-M-20323
(T-40001)
TO CIP TANK
C17204-PID-210B
BFV-M-20326
BFV-M-20300 BFV-M-20301 BFV-M-20303
BV
-M
-20328
BFV-M-20305
PCV-20310
BV-M-20315
BV-M-20318
BFV-P-20320
PROCESS AND INSTRUMENTATION DIAGRAM
RO SYSTEM
WATER TREATMENT PLANT
NTS
A 17/01/18 SYN DEINITIAL ISSUE
SYN 17/01/18DE 17/01/18
SCALE
PERMEATE PROJECT # PERMEATE DRAWING #
CLIENT PROJECT # CLIENT DRAWING #
SHEET
A3
Date
Design DraftingDate
C17204 C17204-PID-203
This document is and shall remain
the property of Permeate Partners
Pty Ltd. The document may only be
used for the purpose for which it
was commissioned in accordance
with the terms of engagement for
the commission. Unauthorised use
of this document in any form is
strictly prohibited. © Permeate
Partners Pty Ltd 2018. All rights
reserved.
PROJECT:
CLIENT
NO. DATE DRAFTER DESIGN MGMT DESCRIPTION
NAME :
P: 1300 799 155
W : www.permeate.com.au
NEWCASTLE, SYDNEY, MELBOURNE, PERTH
PERMEATEP A R T N E R S
COPYRIGHT
ROYAL BOTANIC GARDENS
-
B 23/05/18 SYN DEISSUED FOR EOI
PROGRESS PRINT
T-85001
(T-40001)
FROM CIP WASTE
C17204-PID-210B
WASTE TANK
CAPACITY : 40kL
(P-20106)
FROM ROC
C17204-PID-203E
(PV-00103,00104)
FROM FILTER BACKWASH
C17204-PID-202A
TO SEWER
GV-M-85300
TO WETLAND DISPOSAL
BFV-M-85302
BFV-P-85301
BFV-M-85303
P-85101-1
P-85101-2
WASTE TRANSFER PUMP
MODEL : TBC
MOTOR : TBC
DUTY : 2x75%
PROCESS AND INSTRUMENTATION DIAGRAM
WASTE TANK
WATER TREATMENT PLANT
NTS
A SYN DEINITIAL ISSUE
SYN 17/01/18DE 17/01/18
17/01/18
SCALE
PERMEATE PROJECT # PERMEATE DRAWING #
CLIENT PROJECT # CLIENT DRAWING #
SHEET
A3
Date
Design DraftingDate
C17204 C17204-PID-204
This document is and shall remain
the property of Permeate Partners
Pty Ltd. The document may only be
used for the purpose for which it
was commissioned in accordance
with the terms of engagement for
the commission. Unauthorised use
of this document in any form is
strictly prohibited. © Permeate
Partners Pty Ltd 2018. All rights
reserved.
PROJECT:
CLIENT
NO. DATE DRAFTER DESIGN MGMT DESCRIPTION
NAME :
P: 1300 799 155
W : www.permeate.com.au
NEWCASTLE, SYDNEY, MELBOURNE, PERTH
PERMEATEP A R T N E R S
COPYRIGHT
ROYAL BOTANIC GARDENS
-
B 23/05/18 SYN DEISSUED FOR EOI
PROGRESS PRINT
FROM RO PERMEATE
C17204-PID-203D
FROM BLEND WATER
C17204-PID-202E
(T-80001)
TO IRRIGATION TANK
C17204-PID-206B
BFV-M-05308
BF
V-M
-05309
BF
V-M
-05310
F-05103
PUMP (MP-70111)
FROM STABILISATION DOSING
C17204-PID-207E
NOTES:
1CONNECTION FOR CORROSION COUPON RACK.
F-05104
CALCITE FILTERS
BF
V-M
-05311
BF
V-M
-05312
FROM HYPOCHLORINE DOSING
C17204-PID-208C
BV
-M
-05313
SAMPLE1
IQ
-70364
IQ
-70363
PROCESS AND INSTRUMENTATION DIAGRAM
CALCITE FILTERS
WATER TREATMENT PLANT
NTS
A 17/01/18 SYN DEINITIAL ISSUE
SYN 17/01/18DE 17/01/18
SCALE
PERMEATE PROJECT # PERMEATE DRAWING #
CLIENT PROJECT # CLIENT DRAWING #
SHEET
A3
Date
Design DraftingDate
C17204 C17204-PID-205
This document is and shall remain
the property of Permeate Partners
Pty Ltd. The document may only be
used for the purpose for which it
was commissioned in accordance
with the terms of engagement for
the commission. Unauthorised use
of this document in any form is
strictly prohibited. © Permeate
Partners Pty Ltd 2018. All rights
reserved.
PROJECT:
CLIENT
NO. DATE DRAFTER DESIGN MGMT DESCRIPTION
NAME :
P: 1300 799 155
W : www.permeate.com.au
NEWCASTLE, SYDNEY, MELBOURNE, PERTH
PERMEATEP A R T N E R S
COPYRIGHT
ROYAL BOTANIC GARDENS
-
B 23/05/18 SYN DEISSUED FOR EOI
PROGRESS PRINT
T-80001
(F-05103,F-05104)
FROM CALCITE FILTERS
C17204-PID-205B
IRRIGATION TANK
CAPACITY : TBC
FROM POTABLE WATER
BFV-M-80306-1
P-80102-1
BFV-M-80303
P-80101
CHLORINE RECIRCULATION PUMP
MODEL : TBC
MOTOR : TBC
DUTY : 1x100%
70362
IQ
-
CHLORINE DOSING PUMP (MP-70123)
FROM IRRIGATION WATER HYPO
C17204-PID-208D
BFV-M-70361
BFV-M-80300 BFV-P-80302
BV
-M
-80304
CV-80305
RPZ-80301
1
POTABLE WATER TOP-UP TO HAVE VISIBLE AIR GAP
NOTES:
1
BFV-M-80307
P-80103
FILTER BACKWASH PUMP
MODEL : TBC
MOTOR : TBC
DUTY : 1x100%
CV -80309BFV-M-80310
BACKWASH
TO MEDIA FILTER
C17204-PID-202D
BV
-M
-80308
2
2LAYOUT TO ALLOW SPACE FOR FUTURE STAND BY PUMPS.
BFV-M-80306-2
P-80102-2
TO IRRIGATION
EXISTING
NEW
BFV-M-80306-3
P-80102-3
IRRIGATION PUMPS
MODEL : TBC
MOTOR : TBC
DUTY : TBC
PROCESS AND INSTRUMENTATION DIAGRAM
IRRIGATION TANK
WATER TREATMENT PLANT
NTS
A 17/01/18 SYN DEINITIAL ISSUE
SYN 17/01/18DE 17/01/18
SCALE
PERMEATE PROJECT # PERMEATE DRAWING #
CLIENT PROJECT # CLIENT DRAWING #
SHEET
A3
Date
Design DraftingDate
C17204 C17204-PID-206
This document is and shall remain
the property of Permeate Partners
Pty Ltd. The document may only be
used for the purpose for which it
was commissioned in accordance
with the terms of engagement for
the commission. Unauthorised use
of this document in any form is
strictly prohibited. © Permeate
Partners Pty Ltd 2018. All rights
reserved.
PROJECT:
CLIENT
NO. DATE DRAFTER DESIGN MGMT DESCRIPTION
NAME :
P: 1300 799 155
W : www.permeate.com.au
NEWCASTLE, SYDNEY, MELBOURNE, PERTH
PERMEATEP A R T N E R S
COPYRIGHT
ROYAL BOTANIC GARDENS
-
B 23/05/18 SYN DEISSUED FOR EOI
PROGRESS PRINT
MATERIAL : TBC
NOMINAL CAPACITY : TBC
T - 70003
STABILISATION TANK
STABILISATION
DOSING PUMP
MODEL: TBC
DUTY : TBC
1 x 100%
MATERIAL : TBC
NOMINAL CAPACITY : TBC
T - 70002
ANTISCALANT TANK
ANTISCALANT DOSING
PUMP
MODEL: TBC
DUTY : TBC
2 x 100%
MATERIAL : TBC
NOMINAL CAPACITY : TBC
T - 70001
SBS TANK
SBS
DOSING PUMP
MODEL: TBC
DUTY : TBC
2 x 100%
TO RO FEED
C17204-PID-203B
TO TREATED WATER TRANSFER
C17204-PID-205E
MP- 70103
PRV-70304
PD-70104
PCV-70308
STR-70102
CC
-70101
BV-M-70300
1
TO RO FEED
C17204-PID-203B
BV-M-70302
BV
-M
-70301
BV
-M
-70303
BV
-M
-70305
BV
-M
-70306
BV
-M
-70307
BV-M-70309
FI
70201
MP- 70107
PRV-70314
PD-70108
PCV-70318
STR-70106
CC
-70105
BV-M-70310
1
BV-M-70312
BV
-M
-70311
BV
-M
-70313
BV
-M
-70316
BV
-M
-70317
BV-M-70319
BV
-M
-70315
MP- 70111
PRV-70324
PD-70112
PCV-70328
STR-70110
CC
-70109
BV-M-70320
1
BV-M-70322
BV
-M
-70321
BV
-M
-70323
BV
-M
-70326
BV
-M
-70327
BV-M-70329
BV
-M
-70325
FI
70205
FI
70209
NOTES:
HIGH POINT VENT TO EXTEND ABOVE TANK HIGH LEVEL
1
PROCESS AND INSTRUMENTATION DIAGRAM
PRETREATMENT CHEMICALS
WATER TREATMENT PLANT
NTS
A 17/01/18 SYN DEINITIAL ISSUE
SYN 17/01/18DE 17/01/18
SCALE
PERMEATE PROJECT # PERMEATE DRAWING #
CLIENT PROJECT # CLIENT DRAWING #
SHEET
A3
Date
Design DraftingDate
C17204 C17204-PID-207
This document is and shall remain
the property of Permeate Partners
Pty Ltd. The document may only be
used for the purpose for which it
was commissioned in accordance
with the terms of engagement for
the commission. Unauthorised use
of this document in any form is
strictly prohibited. © Permeate
Partners Pty Ltd 2018. All rights
reserved.
PROJECT:
CLIENT
NO. DATE DRAFTER DESIGN MGMT DESCRIPTION
NAME :
P: 1300 799 155
W : www.permeate.com.au
NEWCASTLE, SYDNEY, MELBOURNE, PERTH
PERMEATEP A R T N E R S
COPYRIGHT
ROYAL BOTANIC GARDENS
-
B 23/05/18 SYN DEISSUED FOR EOI
PROGRESS PRINT
MATERIAL : TBC
NOMINAL CAPACITY : TBC
HYPO CHLORITE TANK
HYPO CHLORITE
DOSING PUMP
MODEL: TBC
DUTY : TBC
2 x 100%
TO TREATED WATER
C17204-PID-205B
RECIRCULATION
TO IRRIGATION TANK
C17204-PID-206B
T - 70004
MP- 70119
PRV-70344
PD-70120
PCV-70348
STR-70118
CC
-70117
BV-M-70340
2
BV-M-70342
BV
-M
-70341
BV
-M
-70343
BV
-M
-70346
BV
-M
-70347
BV-M-70349
BV
-M
-70345
IRRIGATION WATER
HYPO CHLORITE
DOSING PUMP
MODEL: TBC
DUTY : TBC
1 x 100%
MP- 70123
PRV-70354
PD-70124
PCV-70358
STR-70122
CC
-70121
BV-M-70350
2
BV-M-70352
BV
-M
-70351
BV
-M
-70353
BV
-M
-70356
BV
-M
-70357
BV-M-70359
BV
-M
-70355
FI
70217
FI
70221
DESIGN TO ALLOW CHEMICAL TANK TO VENT TO SAFE LOCATION
NOTES:
1
1
2
HIGH POINT VENT TO EXTEND ABOVE TANK HIGH LEVEL
MATERIAL : TBC
NOMINAL CAPACITY : TBC
BIOCIDE DOSING TANK
BIOCIDE DOSING
PUMP
MODEL: TBC
DUTY : TBC
2 x 100%
TO MEDIA FILTER PUMPS
C17204-PID-202B
T - 70004
MP- 70115
PRV-70334
PD-70116
PCV-70338
STR-70114
CC
-70113
BV-M-70330
2
BV-M-70332
BV
-M
-70331
BV
-M
-70333
BV
-M
-70336
BV
-M
-70337
BV-M-70339
BV
-M
-70335
FI
70213
1
BV
-M
-70360
PROCESS AND INSTRUMENTATION DIAGRAM
FEED AND TREATED CHLORINE
WATER TREATMENT PLANT
NTS
A 17/01/18 SYN DEINITIAL ISSUE
SYN 17/01/18DE 17/01/18
SCALE
PERMEATE PROJECT # PERMEATE DRAWING #
CLIENT PROJECT # CLIENT DRAWING #
SHEET
A3
Date
Design DraftingDate
C17204 C17204-PID-208
This document is and shall remain
the property of Permeate Partners
Pty Ltd. The document may only be
used for the purpose for which it
was commissioned in accordance
with the terms of engagement for
the commission. Unauthorised use
of this document in any form is
strictly prohibited. © Permeate
Partners Pty Ltd 2018. All rights
reserved.
PROJECT:
CLIENT
NO. DATE DRAFTER DESIGN MGMT DESCRIPTION
NAME :
P: 1300 799 155
W : www.permeate.com.au
NEWCASTLE, SYDNEY, MELBOURNE, PERTH
PERMEATEP A R T N E R S
COPYRIGHT
ROYAL BOTANIC GARDENS
-
B 23/05/18 SYN DEISSUED FOR EOI
PROGRESS PRINT
M-60308BV - M-60310BV -60309PCV-
1
EQUIPMENT, INSTRUMENTATION AND CONTROL WITH IN
THE BOX ARE A PACKAGED UNIT.
NOTES:
M-60302BV -
S-60301GV -
60300PRV-
1
AIR
M-60305BV -
S-60304GV -
60303PRV-
AIR
M-60307
BV
-
M-60306
BV
-
AIR RECEIVER
AIR RECEIVER
COMPRESSED
AIR DRYER
AIR
COMPRESSOR
1
CAD - 60103
COALESCING
FILTER
FILTER
CF-60104 F-60105
TO VALVE
COMPRESSED AIR
C17204-PID-XXXB
ACMP-60102
ACMP-60101
AIR
COMPRESSOR
SCALE
PERMEATE PROJECT # PERMEATE DRAWING #
CLIENT PROJECT # CLIENT DRAWING #
SHEET
A3
Date
Design DraftingDate
C17204 C17204-PID-209
This document is and shall remain
the property of Permeate Partners
Pty Ltd. The document may only be
used for the purpose for which it
was commissioned in accordance
with the terms of engagement for
the commission. Unauthorised use
of this document in any form is
strictly prohibited. © Permeate
Partners Pty Ltd 2018. All rights
reserved.
PROJECT:
CLIENT
NO. DATE DRAFTER DESIGN MGMT DESCRIPTION
NAME :
P: 1300 799 155
W : www.permeate.com.au
NEWCASTLE, SYDNEY, MELBOURNE, PERTH
PERMEATEP A R T N E R S
COPYRIGHT
ROYAL BOTANIC GARDENS
-
PROCESS AND INSTRUMENTATION DIAGRAM
AIR COMPRESSORS
WATER TREATMENT PLANT
NTS
A 17/01/18 SYN DEINITIAL ISSUE
SYN 17/01/18DE 17/01/18
B 23/05/18 SYN DEISSUED FOR EOI
PROGRESS PRINT
FROM RO REJECT
C17204-PID-203E
T-40001
MATERIAL : TBC
NOMINAL CAPACITY : TBC
FLUSH / CIP TANK
HT - 40101
P-40102
CIP PUMP
MODEL : TBC
MOTOR : TBC
DUTY : TBC
BFV-M-40302
(T-85001)
TO WASTE TANK
C17204-PID-204B
BFV-M-40307
BV
-M
-40300
BF
V-M
-40301
TO RO FLUSHING
C17204-PID-203C
BFV-P-40306
FROM RO PERMEATE
C17204-PID-203D
BFV-M-40304
BFV-M-40305
CIP TANK DESIGN TO ALLOW ADDITION OF BOTH LIQUID AND POWDER CIP SPECIALITY CHEMICALS
NOTES:
1
1
CV-40303
SCALE
PERMEATE PROJECT # PERMEATE DRAWING #
CLIENT PROJECT # CLIENT DRAWING #
SHEET
A3
Date
Design DraftingDate
C17204 C17204-PID-210
This document is and shall remain
the property of Permeate Partners
Pty Ltd. The document may only be
used for the purpose for which it
was commissioned in accordance
with the terms of engagement for
the commission. Unauthorised use
of this document in any form is
strictly prohibited. © Permeate
Partners Pty Ltd 2018. All rights
reserved.
PROJECT:
CLIENT
NO. DATE DRAFTER DESIGN MGMT DESCRIPTION
NAME :
P: 1300 799 155
W : www.permeate.com.au
NEWCASTLE, SYDNEY, MELBOURNE, PERTH
PERMEATEP A R T N E R S
COPYRIGHT
ROYAL BOTANIC GARDENS
-
PROCESS AND INSTRUMENTATION DIAGRAM
FLUSH / CIP TANK
WATER TREATMENT PLANT
NTS
A 17/01/18 SYN DEINITIAL ISSUE
SYN 17/01/18DE 17/01/18
B 23/05/18 SYN DEISSUED FOR EOI
PROGRESS PRINT
ROYAL BOTANIC GARDENS VICTORIA
CRANBOURNE GARDENS WATER TREATMENT PLANT EXPRESSION OF INTEREST SUPPORTING TECHNICAL
INFORMATION
PP REF : C17204
DATE 20/07/2018 REV: C
COMMERCIAL-IN-CONFIDENCE
WWW.PERMEATE.COM.AU
PAGE 20 OF 22
APPENDIX C – REFERENCE BUILDING GENERAL ARRANGEMENT DRAWING
4M W
IDE
x 3.
6M H
IGH
ROLL
ER D
OO
R
MEMBRANEREMOVAL
AREA
ROUNIT
MEDIA FILTERFEED PUMPS
(DUTY :2X100%)IRRIGATION
TRANSFER PUMPS
CIPTANK
AIRCOMPRESSOR
RO-CIPPUMP
WASTE PUMPS(DUTY: 2X75%)
FILTERBACKWASH
PUMP
FEEDTANK
WASTETANK
STABILIZATIONDOSING TANK
SBSDOSING TANK
ANTI-SCALANTDOSING TANK
BIOCIDEDOSING TANK
HYPO-CHLORITEDOSING TANK
ANAL
YZER
WET
RAC
K
CALC
ITE
FILT
ERS
CONTROLROOM
MCC/PLC
A 26/02/18 SYN DE INITIAL ISSUE
DE 26/02/18 SYN 26/02/18
PROCESS BUILDING
PLANT LAYOUT
1:35
MEDIA FILTERS
18000
3300
5000 1000 1500 1500 1500 1500 1500 4500
Ø1000
Ø1000
1150
1400
12000
MEMBRANEREMOVAL
AREA
1440 1780 1050 800 1000
3600
SAFETYSHOWER
SAFETYSHOWER
CHEMICAL LAY DOWNAND
STORAGE AREA
SHEL
VING
AND
SPA
RES
3150 6000 8850
W
S
N
E
TO BE
CONFIRMED
SCALE
PERMEATE PROJECT # PERMEATE DRAWING #
CLIENT PROJECT # CLIENT DRAWING #
SHEET
A3
Date
Design Drafting
Date
C17204 C17204-GA-001
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NEWCASTLE, SYDNEY, MELBOURNE, PERTH
PERMEATEP A R T N E R S
COPYRIGHT
ROYAL BOTANIC GARDENS
-
2000
3000
1150
2500
Ø1200
1180
1000 800 1550 1400 1600 1350 1550 1500
Ø1200
Ø1200
B 23/05/18 SYN DE ISSUED FOR EOI
200049002000 13502300 4000
ROYAL BOTANIC GARDENS VICTORIA
CRANBOURNE GARDENS WATER TREATMENT PLANT EXPRESSION OF INTEREST SUPPORTING TECHNICAL
INFORMATION
PP REF : C17204
DATE 20/07/2018 REV: C
COMMERCIAL-IN-CONFIDENCE
WWW.PERMEATE.COM.AU
PAGE 21 OF 22
APPENDIX D – SITE LAYOUT DRAWINGS
Cranbourne Gardens Water Treatment Plant SKETCH 01SITE COMPONENTS
Legend
AG
Extraction Pump Station
In Gardens Pipeline 1
Irrigation Pump Shed (Existing)
Sewer(New)
Tank Hardstand
Treated Water tank
Treatment Shed
Trility-CG Pipleline
300 m
N
➤➤
N© 2018 Google
© 2018 Google
© 2018 Google
Cranbourne Gardens Water Treatment Plant SKETCH 02SITE ELEMENTS
Legend
In Gardens Pipeline 1
Irrigation Pump Shed (Existing)
Sewer(New)
Tank Hardstand
Treated Water tank
Treatment Shed
Trility-CG Pipleline
90 m
N
➤➤
N© 2018 Google
© 2018 Google
© 2018 Google
ROYAL BOTANIC GARDENS VICTORIA
CRANBOURNE GARDENS WATER TREATMENT PLANT EXPRESSION OF INTEREST SUPPORTING TECHNICAL
INFORMATION
PP REF : C17204
DATE 20/07/2018 REV: C
COMMERCIAL-IN-CONFIDENCE
WWW.PERMEATE.COM.AU
PAGE 22 OF 22
APPENDIX E – EXISTING IRRIGATION PUMP SHED
FOR POTABLE WATER CONNECTION & IRRIGATION WATER SUPPLY