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RAPID-P0005-TYO-PIP-DES-2000-0003 Attachment-1
OWNER REFERENCE
Project
Package
Originator
Discipline
Doc. Type
Unit n°
Serial n°
PIP
DES
0001
0003
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1 / 13
TPX
FE1
RAPID
CONTRACTOR REFERENCE
PETRONAS RAPID PROJECT
FEED PHASE
Project
60987R
Unit n°
Doc. Type
Doc. Code
Sequent. n°
0001
JSD
1300
0003
Project Specification – Piping Tracing
PROJECT SPECIFICATION
PIPING STEAM TRACING
OWNER Approval:
PETRONAS
Name:
Date
(DD-MMM-YY) :
Signature:
Document Class:
Z
Pages modified under this revision:
All
60987R-0001-FOR-0004_E
Adrien Rafin
2013.03.04 17:44:33
+01'00'
Jerome Chanavat
2013.03.04 17:41:36
+01'00'
Jean-Marc Maurice
2013.03.05
11:01:48 +01'00'
1
04-Mar-13
IFD – Issued Approved for Design
J.Chanavat
A.Rafin
J.M. Maurice
0
25-Oct-12
IFD – Issued Approved for Design
J.Chanavat
A.Rafin
J.M. Maurice
A
30-Mar-12
IFA – Issued for Approval
J. Martin
J.M. Maurice
REV.
DATE
DD-MMM-YY
STATUS – REVISION MEMO
A. Rafin WRITTEN BY
(name & visa)
CHECKED BY
(name & visa)
APPROVED BY
(name & visa)
Sections changed in last revision are identified by a vertical line in the margin.
Subject to the provision of Article 13 of the CONTRACT, TECHNIP hereby grant PETRONAS the copyright of this document. No part of this document may be reproduced, stored in a retrieval
system or transmitted in any form or by any means (electronic, mechanical, photocopying, recording or otherwise) without the permission of the copyright owner.
CONFIDENTIAL – Not to disclose without authorization
Electronic Filename: RAPID-FE1-TPX-PIP-DES-0001-0003_A.doc
OWNER REFERENCE
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RAPID
PETRONAS RAPID PROJECT
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0001
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2 / 13
CONTRACTOR REFERENCE
Project
60987R
Unit n°
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Sequent. n°
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JSD
1300
0003
Project Specification – Piping Tracing
CONTENTS
1. PURPOSE ............................................................................................................................................................................ 3
2. REFERENCE DOCUMENTS ........................................................................................................................................... 3
3. ACRONYMS AND DEFINITIONS .................................................................................................................................. 3
4. CODES AND STANDARDS .............................................................................................................................................. 4
4.1
4.2
A PPLICABLE C ODES & S TANDARDS .............................................................................................................................. 4
O RDER OF PRECEDENCE ................................................................................................................................................ 4
5. GENERAL PROCESS AND ENGINEERING REQUIREMENTS .............................................................................. 5
5.1
TYPE OF H EATING ......................................................................................................................................................... 5
5.3
CONDENSATE RETURN .................................................................................................................................................. 5
5.2
5.4
5.5
5.6
STEAM SUPPLY ............................................................................................................................................................. 5
LINES TO BE TRACED ..................................................................................................................................................... 5
TRACER FASTENING SYSTEM ......................................................................................................................................... 5
D ESIGN PRINCIPLE......................................................................................................................................................... 6
6. INSTRUMENTS ............................................................................................................................................................... 10
7. DETAIL ENGINEERING AND DESIGN REQUIREMENTS .................................................................................... 10
7.1
PURPOSE ..................................................................................................................................................................... 10
7.3
STEAM TRACER INSTALLATION ................................................................................................................................... 11
7.2
7.4
7.5
7.6
G ENERAL DESIGN ........................................................................................................................................................ 10
THERMAL EXPANSION ................................................................................................................................................. 11
INSTRUMENTS ............................................................................................................................................................. 11
SUPPORTING ................................................................................................................................................................ 11
8. STEAM TRACING DOSSIERS ...................................................................................................................................... 12
8.1
D RAWING REQUIREMENTS .......................................................................................................................................... 12
9. MATERIALS .................................................................................................................................................................... 13
10.
FABRICATION ............................................................................................................................................................ 13
11.
INSPECTION AND TESTING ................................................................................................................................... 13
11.1 CLEANING ................................................................................................................................................................... 13
11.2 INSPECTION ................................................................................................................................................................. 13
11.3 TESTING ...................................................................................................................................................................... 13
Subject to the provision of Article 13 of the CONTRACT, TECHNIP hereby grant PETRONAS the copyright of this document. No part of this document may be reproduced, stored in a retrieval
system or transmitted in any form or by any means (electronic, mechanical, photocopying, recording or otherwise) without the permission of the copyright owner.
CONFIDENTIAL – Not to disclose without authorization
OWNER REFERENCE
Package
Project
FE1
RAPID
PETRONAS RAPID PROJECT
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DES
0001
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3 / 13
CONTRACTOR REFERENCE
Project
60987R
Unit n°
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Sequent. n°
0001
JSD
1300
0003
Project Specification – Piping Tracing
1.
PURPOSE
This Project Specification covers the minimum requirements for Piping Steam Tracing to be used
for the PETRONAS RAPID (Refinery And Petrochemical Integrated Development) Project.
These requirements shall be used throughout all steps of the Project and by all parties:
CONTRACTOR, SUBCONTRACTORS, EPCC CONTRACTORS, Suppliers, etc.
Electrical tracing is managed by RAPID-FE1-TPX-ELE-DES-0001-0022 Electrical Trace Heating.
2.
REFERENCE DOCUMENTS
RAPID-FE1-TPX-PIP-DES-0001-9009
Project Specification – Protective Steam Heating of
Piping System
RAPID-FE1-TPX-PIP-STD-0001-0001
Project Specification – Piping Design Standard
RAPID-FE1-TPX-PIP-STD-0001-0002
Project Specification – Piping Construction Standard
RAPID-FE1-TPX-PIP-DES-0001-0021
Project Specification - Piping class Summary
RAPID-FE1-TPX-MEC-DES-0001-0401
Project Specification - Hot Insulation
RAPID-FE1-TPX-INC-DES-0001-9018
Project
Specification
-
Installation
of
on-line
instruments
3.
ACRONYMS AND DEFINITIONS
The following terms used in this document have the meaning defined below:
The Form Of Agreement together with the documents in order of
CONTRACT
priority,
including
the
exhibits,
drawings,
specifications
and
documents referred to and in the order of precedence listed in the
Form of Agreement.
CONTRACTOR
Company(ies), joint ventures or consortium appointed by OWNER
with specified authority to perform the WORK in accordance with the
CONTRACT, here the Consortium of Technip France and Technip
Geoproduction (M) Sdn Bhd.
Petroliam
OWNER
Nasional
Berhad
(PETRONAS)
which
includes
its
representative, successors, nominees and permitted assigns and shall
where the context so admits and requires, also include its employees,
agents and designated representative.
PROJECT
Refinery
And
Petrochemicals
Integrated
Development
(RAPID)
Project in the State of Johor, Malaysia.
SCOPE OF WORK
The scope of work to be perform ed and services to be rendered by
CONTRACTOR under the CONTRACT in relation to the realization
of the PROJECT.
WORK
Works, tasks and WORK to be performed by CONTRACTOR as
specified in or to be inferred from the CONTRACT, more specially
set out in the SCOPE OF WORK which may be modified by
CHANGE ORDER.
SUBCONTRACTOR
Any third party Subcontractor engaged by CONTRACTOR
in
connection with the WORK.
Subject to the provision of Article 13 of the CONTRACT, TECHNIP hereby grant PETRONAS the copyright of this document. No part of this document may be reproduced, stored in a retrieval
system or transmitted in any form or by any means (electronic, mechanical, photocopying, recording or otherwise) without the permission of the copyright owner.
CONFIDENTIAL – Not to disclose without authorization
OWNER REFERENCE
Package
Project
FE1
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PETRONAS RAPID PROJECT
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Project
60987R
Unit n°
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Sequent. n°
0001
JSD
1300
0003
Project Specification – Piping Tracing
LICENSOR
Process Licensors selected by OWNER for the process of LICENSED
EPCC CONTRACTORS
The person or persons, company, join venture or consortium whose
UNITS of the FACILITIES.
proposal
has
been
accepted
by
OWNER
for
Engineering,
Procurement, Construction and Commissioning Contract for the
PROJECT including its personnel, representatives, successors and
permitted assignee.
MAIN STEAM HEADER
A carbon steel header running from the battery limit in the unit.
STEAM SUPPLY LINE
A carbon steel pipe line running from the main steam header in the
unit to a steam distribution manifold.
STEAM DISTRIBUTION MANIFOLD
Carbon steel pipe manifold for the distribution
of steam, via tracer feed lines, to a number of tracers.
TRACER FEED LINE
A carbon steel line running from the steam distribution manifold to
the tracer.
TRACER
A line m ade of stainless steel pipe running from a tracer feed line
along the pipe, instrument, or equipment to be traced, ending at the
tracer return line.
TRACER RETURN LINE
A carbon steel pipe line running from the tracer to the condensate
return manifold.
CONDENSATE RETURN MANIFOLD
Carbon steel pipe manifold to collect condensate, via
tracer return lines, from a number of tracers.
CONDENSATE RETURN LINE A carbon steel pipe line running from the condensate return
manifold to the condensate header.
CONDENSATE HEADER A carbon steel header running in the unit, collecting all condensate to
the battery limit.
The acronyms used in this document have the meaning defined below:
-
FEED
Front-End Engineering Design
-
PTS
PETRONAS Technical Standard
-
RAPID
Refinery And Petrochemicals Integrated Development
-
LP
Low pressure steam
-
MP
Medium Pressure steam
-
P&ID
Process & Instrument Line Diagram
-
DM
Steam Distribution Manifold
-
CM
Condensate Return Manifold
4.
CODES AND STANDARDS
4.1
Applicable Codes & Standards
Unless otherwise specified, the latest applicable revision of codes and standards shall be
considered.
4.2
Order of precedence
In case of conflict between Laws, Project Specifications and Codes & Standards, the following
order of precedence shall be considered:
Subject to the provision of Article 13 of the CONTRACT, TECHNIP hereby grant PETRONAS the copyright of this document. No part of this document may be reproduced, stored in a retrieval
system or transmitted in any form or by any means (electronic, mechanical, photocopying, recording or otherwise) without the permission of the copyright owner.
CONFIDENTIAL – Not to disclose without authorization
OWNER REFERENCE
Project
RAPID
Package
FE1
Originator
Discipline
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Unit n°
Serial n°
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DES
0001
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5 / 13
TPX
CONTRACTOR REFERENCE
PETRONAS RAPID PROJECT
FEED PHASE
Project
60987R
Unit n°
Doc. Type
Doc. Code
Sequent. n°
0001
JSD
1300
0003
Project Specification – Piping Tracing
- 1.
Malaysian Laws and applicable regulatory requirements,
- 2.
Project Specifications and supplemented PTS,
- 3.
Applicable Malaysian Codes and Standards,
- 4.
Applicable International Codes and Standards.
If a Low er Level requirem ent is m ore stringent than an upper one in the above docum ents, a
request shall be raised to OWNER for written decision before proceeding with the Design,
Manufacture or Construction.
5.
GENERAL PROCESS AND ENGINEERING REQUIREMENTS
5.1
Type of Heating
The following media is used:
Conditions are as per RAPID-FE1-TPX-PRO-DES-0001-0001 Design Basis-Utilities Conditions.
Type
of steam
5.2
Pressure Barg
Temperature º C Design
Operating
Design
Operating
LP
295
185
25.0
22.0
MP
350
290
9.0
7.0
Steam Supply
LP and M P steam supply in Process and Offsite areas will be from the main LP and M P steam
headers.
5.3
Condensate Return
The condensate discharge from condensate return manifolds shall be connected to the main
condensate headers in Process Areas. In Offsite and Interconnecting areas, the condensate
discharge from condensate return manifold will be recovered as per RAPID-FE1-TPP-PRO-DES-
4200-0001 Process Design Basis – Steam Associated Facilities.
5.4
Lines to be traced
Traced lines and instruments are indicated on P&ID’s with proper symbol.
Lines to be traced are defined in Process & Utility Line Lists.
5.5
Tracer fastening system
-
Isolating wedges shall be provided between tracer and pipe if necessary.
-
Tracers shall be fastened to piping with stainless steel fastening bands. Bands shall be
placed every 0.5m maximum.
-
Heat transfer cement
Subject to the provision of Article 13 of the CONTRACT, TECHNIP hereby grant PETRONAS the copyright of this document. No part of this document may be reproduced, stored in a retrieval
system or transmitted in any form or by any means (electronic, mechanical, photocopying, recording or otherwise) without the permission of the copyright owner.
CONFIDENTIAL – Not to disclose without authorization
OWNER REFERENCE
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CONTRACTOR REFERENCE
PETRONAS RAPID PROJECT
FEED PHASE
Project
60987R
Unit n°
Doc. Type
Doc. Code
Sequent. n°
0001
JSD
1300
0003
Project Specification – Piping Tracing
5.6
Design principle
5.6.1
Steam tracing codes
-
Table 1: Maintenance temperature up to 55°C with LP Steam , tracing code : SL
-
Table 2: Maintenance temperature between 55°C and 130°C with LP Steam , tracing code
: SL
-
5.6.2
Table 3: Maintenance temperature up to 180°C with MP Steam, tracing code : SM
Maximum tracer length
Maximum tracer length shall be confirmed by EPCC CONTRACTORS as describe in RAPID-
FE1-TPX-PIP-DES-0001-9009.
Heat tracers used are steel piping 1/2” (OD = 21.3mm) and 3/4” (OD = 26.7mm)
TRACER
NOMINAL
SIZE
PROCESS UNIT
Efficient
(pipe)
Table 1 :SL
Max
Total Max
Length
Length (m)
(m)
ON RACK AND
INTERCONNECTING
Efficient
Total Max Length
Max Length
(m)
(m)
1/2”
30
+ 2 x 15 = 60
45
+ 2 x 15 = 75
1/2”
35
+ 2 x 15 = 65
50
+ 2 x 15 = 80
3/4”
60
+ 2 x 15 = 90
80
+ 2 x 15 = 110
1/2”
65
+ 2 x 15 = 95
90
+ 2 x 15 = 120
3/4”
95
+ 2 x 15 = 125
130
+ 2 x 15 = 160
Table 2 :SL
Table 3 :ML
5.6.3
Insulation thickness
Insulation thicknesses indicated in the hereafter Tables are in accordance with the Project
Specification –Hot Insulation RAPID-FE1-TPX-MEC-DES-0001-0401.
5.6.4
Tracer fixing lines
Insulating wedges shall be provided between tracer and pipe in accordance with tables from
following paragraph – Numbers of tracers calculation.
5.6.5
Number of tracers calculation
Number of tracer shall be confirmed by EPCC CONTRACTORS as describe in RAPID-FE1-TPX-
PIP-DES-0001-9009, based on following tables:
Subject to the provision of Article 13 of the CONTRACT, TECHNIP hereby grant PETRONAS the copyright of this document. No part of this document may be reproduced, stored in a retrieval
system or transmitted in any form or by any means (electronic, mechanical, photocopying, recording or otherwise) without the permission of the copyright owner.
CONFIDENTIAL – Not to disclose without authorization
OWNER REFERENCE
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FEED PHASE
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Unit n°
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Sequent. n°
0001
JSD
1300
0003
Project Specification – Piping Tracing
TABLE - 1
TRACING CODE: SL
PIPE MAINTENANCE TEMPERATURE: T < 55°C
Type of heating medium: Low Pressure STEAM, 5 barg / 165°C
General air Condition - Design Minimum temperature Associated wind velocity
: 20 °C
: 32.5 m/s (from General Design Specification RAPID-FE1-TPX-
ENG-PRC-0001-0202 paragraph 14.3 Design Wind velocities).
Design Maximum temperature
: 36.5 °C
Associated wind velocity
: 1 m/s (Standard value for minimum wind velocity)
MAIN LINE (to be
traced) DIAMETER
Nominal
(inch)
External
(mm)
INSULATION
TRACING
Int.
Nominal External
Thickness
Fixation
Diameter
Diameter Diameter Nbr
(mm)
System
(mm)
(inch)
(mm)
3/4
26.7
1/2
21.30
1
Spacer
48.0
30
Maximum
Real Fluid
Temperature
Inside the
Line (°C)
85.4
Steam
Flowrate
kg/h.100m
5.3
1
33.4
1/2
21.30
1
Spacer
54.7
30
82.9
5.5
3/2
48.3
1/2
21.30
1
Spacer
69.6
30
78.3
5.9
2
60.3
1/2
21.30
1
Spacer
81.6
30
75.3
6.1
3
88.9
1/2
21.30
1
Spacer
110.2
40
74.8
6.1
4
114.3
1/2
21.30
1
Spacer
135.6
40
70.9
6.4
6
168.3
1/2
21.30
2
Spacer
200.3
40
80.7
11.4
8
219.1
1/2
21.30
2
Spacer
251.1
40
75.6
12.2
10
273.1
1/2
21.30
2
Spacer
305.1
40
71.5
12.8
12
323.9
1/2
21.30
2
Spacer
355.9
40
68.3
13.2
14
355.6
1/2
21.30
3
Spacer
398.2
40
75.7
18.3
16
406.4
1/2
21.30
1
Clamp
427.7
40
97.2
31.3
18
457.2
1/2
21.30
1
Clamp
478.5
40
94.2
32.8
20
508.0
1/2
21.30
1
Clamp
529.3
40
91.5
34.2
22
558.2
1/2
21.30
1
Clamp
579.5
40
89.1
35.3
24
609.6
1/2
21.30
1
Clamp
630.9
40
86.9
36.5
26
660.4
1/2
21.30
1
Clamp
681.7
40
84.8
37.5
28
711.2
1/2
21.30
1
Clamp
732.5
40
83.0
38.5
30
762.0
1/2
21.30
1
Clamp
783.3
40
81.2
39.3
32
821.8
1/2
21.30
1
Clamp
843.1
40
79.4
40.3
34
863.6
1/2
21.30
1
Clamp
884.9
40
78.1
40.9
36
914.4
1/2
21.30
1
Clamp
935.7
40
76.8
41.6
42
1066.8
1/2
21.30
1
Clamp
1088.1
40
73.1
43.4
Subject to the provision of Article 13 of the CONTRACT, TECHNIP hereby grant PETRONAS the copyright of this document. No part of this document may be reproduced, stored in a retrieval
system or transmitted in any form or by any means (electronic, mechanical, photocopying, recording or otherwise) without the permission of the copyright owner.
CONFIDENTIAL – Not to disclose without authorization
OWNER REFERENCE
Package
Project
RAPID
PETRONAS RAPID PROJECT
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Unit n°
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Sequent. n°
0001
JSD
1300
0003
Project Specification – Piping Tracing
TABLE - 2
TRACING CODE: SL
PIPE MAINTENANCE TEMPERATURE: 55 < T < 130°C
Type of heating medium: Low Pressure STEAM, 5 barg / 165°C
General air Condition - Design Minimum temperature Associated wind velocity
: 20 °C
: 32.5 m/s (from General Design Specification RAPID-FE1-TPX-
ENG-PRC-0001-0202 paragraph 14.3 Design Wind velocities).
Design Maximum temperature
: 36.5 °C
Associated wind velocity
: 1 m/s (Standard value for minimum wind velocity)
MAIN LINE (to
be traced)
DIAMETER
TRACING
Nominal
Nominal External
Diameter
(inch)
(mm)
(inch)
External
Diameter Nbr
(mm)
Maximum Real
Steam
Fluid
Flowrate
Temperature
Inside the Line
Int.
Thickness
Diameter
kg/h.100m
(°C)
(mm)
(mm)
INSULATION
Fixation
System
3/4
26.7
3/4
26.70
1
Clamp
53.4
30
138.5
13.0
1
33.4
3/4
26.70
1
Clamp
60.1
30
137.1
13.9
3/2
48.3
1/2
21.30
2
Clamp
80.3
30
141.3
18.1
2
60.3
1/2
21.30
2
Clamp
92.3
30
139.6
19.7
3
88.9
1/2
21.30
2
Clamp
120.9
40
139.7
19.6
4
114.3
1/2
21.30
2
Clamp
146.3
40
137.2
22.1
6
168.3
1/2
21.30
3
Clamp
210.9
40
139.0
30.6
8
219.1
3/4
26.70
3
Clamp
272.5
40
139.1
38.2
10
273.1
1/2
21.30
4
Clamp
315.7
40
138.0
42.8
12
323.9
3/4
26.70
4
Clamp
377.3
40
139.2
50.9
14
355.6
3/4
26.70
4
Clamp
409.0
40
137.9
54.1
16
406.4
1/2
21.30
2
Cement
438.4
40
139.9
58.9
18
457.2
1/2
21.30
2
Cement
489.2
40
138.2
63.9
20
508.0
3/4
26.70
2
Cement
548.1
40
140.2
72.5
22
558.2
3/4
26.70
2
Cement
598.3
40
138.9
77.7
24
609.6
3/4
26.70
2
Cement
649.7
40
137.6
82.5
26
660.4
1/2
21.30
3
Cement
703.0
40
139.4
90.9
28
711.2
1/2
21.30
3
Cement
753.8
40
138.3
95.9
30
762.0
1/2
21.30
3
Cement
804.6
40
137.3
100.8
32
821.8
3/4
26.70
3
Cement
875.2
40
139.7
112.4
34
863.6
3/4
26.70
3
Cement
917.0
40
139.0
116.5
36
914.4
3/4
26.70
3
Cement
967.8
40
138.2
121.2
42
1066.8
1/2
21.30
4
Cement
1109.4
40
136.9
136.6
Subject to the provision of Article 13 of the CONTRACT, TECHNIP hereby grant PETRONAS the copyright of this document. No part of this document may be reproduced, stored in a retrieval
system or transmitted in any form or by any means (electronic, mechanical, photocopying, recording or otherwise) without the permission of the copyright owner.
CONFIDENTIAL – Not to disclose without authorization
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Unit n°
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Sequent. n°
0001
JSD
1300
0003
Project Specification – Piping Tracing
TABLE - 3
TRACING CODE: ML
PIPE MAINTENANCE TEMPERATURE: T < 180°C
Type of heating medium: Medium Pressure STEAM, 19 barg / 275°C
General air Condition - Design Minimum temperature Associated wind velocity
: 20 °C
: 32.5 m/s (from General Design Specification RAPID-FE1-TPX-
ENG-PRC-0001-0202 paragraph 14.3 Design Wind velocities).
Design Maximum temperature
: 36.5 °C
Associated wind velocity
: 1 m/s (Standard value for minimum wind velocity)
MAIN LINE (to
be traced)
DIAMETER
TRACING
Nominal
Nominal External
Diameter
(inch)
(mm)
(inch)
External
Diameter Nbr
(mm)
Maximum Real
Steam
Fluid
Flowrate
Temperature
Inside the Line
Int.
Thickness
Diameter
kg/h.100m
(°C)
(mm)
(mm)
INSULATION
Fixation
System
3/4
26.7
3/4
26.70
1
Clamp
53.4
30
138.5
13.0
1
33.4
3/4
26.70
1
Clamp
60.1
30
137.1
13.9
3/2
48.3
1/2
21.30
2
Clamp
80.3
30
141.3
18.1
2
60.3
1/2
21.30
2
Clamp
92.3
30
139.6
19.7
3
88.9
1/2
21.30
2
Clamp
120.9
40
139.7
19.6
4
114.3
1/2
21.30
2
Clamp
146.3
40
137.2
22.1
6
168.3
1/2
21.30
3
Clamp
210.9
40
139.0
30.6
8
219.1
3/4
26.70
3
Clamp
272.5
40
139.1
38.2
10
273.1
1/2
21.30
4
Clamp
315.7
40
138.0
42.8
12
323.9
3/4
26.70
4
Clamp
377.3
40
139.2
50.9
14
355.6
3/4
26.70
4
Clamp
409.0
40
137.9
54.1
16
406.4
1/2
21.30
2
Cement
438.4
40
139.9
58.9
18
457.2
1/2
21.30
2
Cement
489.2
40
138.2
63.9
20
508.0
3/4
26.70
2
Cement
548.1
40
140.2
72.5
22
558.2
3/4
26.70
2
Cement
598.3
40
138.9
77.7
24
609.6
3/4
26.70
2
Cement
649.7
40
137.6
82.5
26
660.4
1/2
21.30
3
Cement
703.0
40
139.4
90.9
28
711.2
1/2
21.30
3
Cement
753.8
40
138.3
95.9
30
762.0
1/2
21.30
3
Cement
804.6
40
137.3
100.8
32
821.8
3/4
26.70
3
Cement
875.2
40
139.7
112.4
34
863.6
3/4
26.70
3
Cement
917.0
40
139.0
116.5
36
914.4
3/4
26.70
3
Cement
967.8
40
138.2
121.2
42
1066.8
1/2
21.30
4
Cement
1109.4
40
136.9
136.6
Subject to the provision of Article 13 of the CONTRACT, TECHNIP hereby grant PETRONAS the copyright of this document. No part of this document may be reproduced, stored in a retrieval
system or transmitted in any form or by any means (electronic, mechanical, photocopying, recording or otherwise) without the permission of the copyright owner.
CONFIDENTIAL – Not to disclose without authorization
OWNER REFERENCE
Project
RAPID
PETRONAS RAPID PROJECT
FEED PHASE
Package
Originator
TPX
FE1
Discipline
Doc. Type
Unit n°
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PIP
DES
0001
0003
Rev.
Page
1
10 / 13
CONTRACTOR REFERENCE
Project
60987R
Unit n°
Doc. Type
Doc. Code
Sequent. n°
0001
JSD
1300
0003
Project Specification – Piping Tracing
6.
INSTRUMENTS
Instrument requiring tracing are defined in instrument list in accordance with piping and
instrumentation diagrams.
They can be:
- Flanged-mounted instruments, such as control valves, ON-OFF valves, flow elements, rotameters,
pressure safety valves, or any flanged mounted instrument.
- Tapped-mounted and remote instruments, such as pressure transmitters, level transmitters, flow
transmitters, or any tapped mounted instrument.
7.
DETAIL ENGINEERING AND DESIGN REQUIREMENTS
7.1
Purpose
The purpose of detail engineering and design is to develop, from the documents prepare all
necessary documents and/or calculations which are required to purchase materials, fabricate, install
and test the Steam tracing network.
7.2
General design
Caution shall be taken that tracer feed lines, tracers and tracer return lines do not interfere with
valves, equipment, instruments, etc. in hindering of access, operation, maintenance and removal.
-
Each tracer feed line shall have a separate valved connection on the steam distribution
manifold. Each tracer return line shall be provided with its own steam trap.
-
Steam Supply /Condensate Return M anifolds shall be prefabricated in accordance with
Construction Standards rules.
-
Installation of manifold is preferred in vertical position rather than horizontal position for
space and size matters.
-
Vertical and horizontal steam supply manifolds shall have a maximum of 12 tracer
connections, including dedicated connections for instruments and spare.
-
Vertical and horizontal condensate return manifolds shall have a maximum of 12 tracer
connections, including dedicated connections for instruments and spare.
-
Tracer isometric drawings shall show the tracer route in dotted line, the tracer feed
sequence number from steam manifold and the tracer return sequence number to
condensate return manifold, as well as tracer feed and tracer return pipe length.
-
All valves and traps shall be accessible from grade or platform.
Each tracer supply shall be routed, to the object to be traced, as short as possible, in
accordance with Construction Standards. The tracer shall start at the highest point and be
routed downwards to the steam trap at the condensate collector.
-
Tracer feed and tracer return lines shall be insulated in accordance with the Project
Specification – Thermal Insulation - RAPID-FE1-TPX-MEC-DES-0001-9002
-
.
If a line needs more than one tracer, a tracer may run back and forward along the line as
long as the maximum length is not exceeded.
Subject to the provision of Article 13 of the CONTRACT, TECHNIP hereby grant PETRONAS the copyright of this document. No part of this document may be reproduced, stored in a retrieval
system or transmitted in any form or by any means (electronic, mechanical, photocopying, recording or otherwise) without the permission of the copyright owner.
CONFIDENTIAL – Not to disclose without authorization
OWNER REFERENCE
Project
RAPID
PETRONAS RAPID PROJECT
FEED PHASE
Package
FE1
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TPX
Discipline
Doc. Type
Unit n°
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PIP
DES
0001
0003
Rev.
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1
11 / 13
CONTRACTOR REFERENCE
Project
60987R
Unit n°
Doc. Type
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Sequent. n°
0001
JSD
1300
0003
Project Specification – Piping Tracing
-
Tracing of two different objects with the same tracer is not permitted. Suction and
discharge piping on two or more parallel pumps shall also be treated separately to enable
dismantling at those pumps while others remain in operation.
-
7.3
Tracers that follow the contour of equipment shall start at the highest point to be traced.
Steam tracer installation
-
Single tracers shall run along the bottom half of the horizontal pipe line to be traced.
M ultiple tracers shall run at an angle to the vertical axis of the horizontal pipe line and
equally spaced at vertical pipe lines (see PTS.31.38.30.11 sheet 20).
-
Flange connections shall be used for tracer dismantling but their use shall be limited as
much as possible.
-
Flange connections shall be installed at pumps, equipment, control valves, relief valves,
special break-out flanges, spectacle blinds and orifice flanges. They shall be installed
outside the insulation to permit dismantling.
-
Vents, drains, equipment nozzles, chemical cleaning connections and/or steam-out
connections, and all other dead ends at a traced object shall be traced to its extremity or up
to and including its first shut-off valve.
7.4
Thermal expansion
-
The thermal expansion for tracing will be define by EPCC CONTRACTORS following
tracer material final choice:
Type of steam
Material
Thermal Expansion
LP Steam at 185 ºC
Stainless steel pipe
To be defined during EPCC
stage
MP Steam at 290 °C
Stainless steel pipe
To be defined during EPCC
stage
-
On long runs, tracers shall be provided with expansion loops. The loops shall be extended
outside the insulation and shall be insulated separately.
-
7.5
Installing flange connections in loops is not allowed.
Instruments
Tracing of instruments shall be as per the Project Specification - Installation of on-line instruments
- RAPID-FE1-TPX-INC-DES-0001-9018 and as per Instrument Hook-up.
7.6
Supporting
-
Tracer feed and return lines (lines running from manifold to tracer or from tracer to
manifold) shall be adequately supported with an acceptable method, preferably from, but
not attached to, adjacent structural steel and not from process lines.
-
The distance between support points shall not exceed 3 m. Supply and return lines, coming
from or going to the same manifold, shall be grouped together as much as possible for
common supports.
-
Tracer supply and return lines shall not be pocketed except where absolutely necessary for
head room, operation and maintenance.
Subject to the provision of Article 13 of the CONTRACT, TECHNIP hereby grant PETRONAS the copyright of this document. No part of this document may be reproduced, stored in a retrieval
system or transmitted in any form or by any means (electronic, mechanical, photocopying, recording or otherwise) without the permission of the copyright owner.
CONFIDENTIAL – Not to disclose without authorization
OWNER REFERENCE
Project
RAPID
PETRONAS RAPID PROJECT
FEED PHASE
Package
Originator
TPX
FE1
Discipline
Doc. Type
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PIP
DES
0001
0003
Rev.
Page
1
12 / 13
CONTRACTOR REFERENCE
Project
60987R
Unit n°
Doc. Type
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Sequent. n°
0001
JSD
1300
0003
Project Specification – Piping Tracing
-
Tracers shall be supported from the traced object by means of Stainless Steel bands. No
deformation of tracing, due to bending shall be allowed. In all cases the tracer shall be held
tight to the object to be traced without sags.
-
On pipe rack or pipe way, in offsite or in interconnecting, expansion loops shall be
provided.
-
Fastening bands shall be installed allowing tracer thermal expansion expect for anchor
points which shall be more tightened.
-
Tracer bands shall be located as close as possible to the back face of each flange.
8.
STEAM TRACING DOSSIERS
8.1
Drawing requirements
8.1.1
Location of steam distribution manifolds (DM) and condensate return manifolds (CM)
The location of steam distribution manifolds (DM) and condensate return manifolds (CM) shall be
specified on drawings called “Location plan for Steam Supply (DM) and Condensate Return (DM)
manifolds. All manifolds shall be tagged as per RAPID-FE1-TPX-PIP-STD-0001-0002 sheet 655.
If manifolds are located on platform, elevation shall be indicated. Plot Plans shall be used as
background for those Location plans.
8.1.2
Steam supply and condensate Return Manifolds P&IDs
Steam supply and condensate Return Manifolds P&IDs shall be prepared by Piping group.
It includes:
8.1.3
-
Manifold arrangement (tag number, line number, design area allocation)
-
Tracer size, tracer sequence number, tracer destination (line to be traced)
-
From/to connection to steam/condensate P&IDs
Isometrics
Steam supply line, condensate return line and manifolds isometrics.
8.1.4
List of traced lines
List of traced lines (including line number, piping class, diameter, insulation code and design area
number).
8.1.5
Traced isometrics
Traced isometrics (mark-up isometric) including the following information
-
Tracer feed line number from steam manifold and tracer return line number to condensate
return manifold.
-
Pipe length of tracer feed line and tracer return line
Subject to the provision of Article 13 of the CONTRACT, TECHNIP hereby grant PETRONAS the copyright of this document. No part of this document may be reproduced, stored in a retrieval
system or transmitted in any form or by any means (electronic, mechanical, photocopying, recording or otherwise) without the permission of the copyright owner.
CONFIDENTIAL – Not to disclose without authorization
OWNER REFERENCE
Project
RAPID
PETRONAS RAPID PROJECT
FEED PHASE
Package
FE1
Originator
TPX
Discipline
Doc. Type
Unit n°
Serial n°
PIP
DES
0001
0003
Rev.
Page
1
13 / 13
CONTRACTOR REFERENCE
Project
60987R
Unit n°
Doc. Type
Doc. Code
Sequent. n°
0001
JSD
1300
0003
Project Specification – Piping Tracing
8.1.6
Heat tracing nomenclature
Table which sums up all above information in order to trace stream traced line and ensure proper
installation during construction activities. Refer to RAPID-FE1-TPX-PIP-STD-0001-0002 Project
Specification – Piping Construction Standard for manifold nomenclature.
9.
MATERIALS
-
Materials for the tracing systems shall be in accordance with the applicable piping classes .
Substitutions, including thicker wall materials, are not permitted without written approval
of Purchaser.
-
Components shall be new, clean and unused.
For all threaded pipe to tube connections, shall be in accordance with ASME/ANSI
B1.20.1 and shall be seal welded with a full strength fillet weld
-
For attachment of tracing, fully softened 18-8 Stainless Steel bands, 10 x 0.4 mm, shall be
used. Seal or buckles for use with bands shall be from 18-8 fully softened Stainless Steel
10.
FABRICATION
-
Installation shall be done in accordance with Steam Tracing Dossiers, Construction
Standards and this specification.
-
Welding shall be in accordance with Project Specification for Shop and field fabrication of
piping system.
-
All carbon steel exterior surfaces, except machined flange faces, shall receive surface
preparation and primer coating, in accordance with applicable project specification.
11.
INSPECTION AND TESTING
11.1
Cleaning
Tracing systems shall be cleaned of weld spatter, pipe scale, rust and other debris prior to testing
and operation by using either steam or air.
11.2
Inspection
The following visual inspections shall be made prior to testing and insulating:
-
Tracing shall be visually inspected for kinked or flattened sections. All such sections shall
be cut out and replaced.
-
Tracer attachments shall be checked to ensure freedom of movement towards expansion
loops.
-
Tracer attachments shall be inspected at expansion loops, at equipment breakpoints, and
other changes of direction where movement of tracer could damage the insulation.
11.3
Testing
The tracer systems shall be pressure tested, prior to insulation.
Subject to the provision of Article 13 of the CONTRACT, TECHNIP hereby grant PETRONAS the copyright of this document. No part of this document may be reproduced, stored in a retrieval
system or transmitted in any form or by any means (electronic, mechanical, photocopying, recording or otherwise) without the permission of the copyright owner.
CONFIDENTIAL – Not to disclose without authorization
B MIN
SPARE
SPARE
B
INSTRUMENTS TRACING (WITH TUBING)
STEAM TRAP STEAM TRAP
TO GRADE TO GRADE
BYPASS
SPARE SPARE
STEAM TRAP
TO GRADE BYPASS
RAPID-P0005-TYO-PIP-DES-2000-0003 Attachment-3
TABLE-1 TRACING CODE: SL PIPE MAINTENANCE TEMPERATURE: T < 55 °C
Type of heating medium: Low Pressure Steam, 5 barg / 165 °C, Saturated temperature 158.8 °C General air condition – Design Minimum temperature: 20 °C Main Line
Tracer
Insulation
Nominal Diameter (DN)
External Diameter (mm)
Nominal Diameter (DN)
Numbers of Tracer
Tracer Fixation
Thickness (mm)
20
26.7
15
1
Fastening Band
30
25
33.4
15
1
Fastening Band
30
40
48.3
15
1
Fastening Band
30
50
60.3
15
1
Fastening Band
30
80
88.9
15
1
Fastening Band
30
100
114.3
15
1
Fastening Band
30
150
168.3
15
1
Fastening Band
30
200
219.1
15
1
Fastening Band
30
250
273.1
15
2
Fastening Band
30
300
323.9
15
2
Fastening Band
30
350
355.6
15
2
Fastening Band
30
400
406.4
15
2
Fastening Band
30
450
457.2
15
2
Fastening Band
30
500
508.0
15
2
Fastening Band
30
550
558.2
15
2
Fastening Band
30
600
609.6
15
3
Fastening Band
30
650
660.4
15
3
Fastening Band
30
700
711.2
15
3
Fastening Band
30
750
762.0
15
3
Fastening Band
30
800
821.8
15
3
Fastening Band
30
850
863.6
15
3
Fastening Band
30
900
914.4
15
4
Fastening Band
30
1050
1066.8
15
4
Fastening Band
30
RAPID-P0005-TYO-PIP-DES-2000-0003 Attachment-4
TABLE-2 TRACING CODE: SL PIPE MAINTENANCE TEMPERATURE: 55 °C < T < 100 °C
Type of heating medium: Low Pressure Steam, 5 barg / 165 °C, Saturated temperature 158.8 °C General air condition – Design Minimum temperature: 20 °C Main Line
Tracer
Insulation
Nominal Diameter (DN)
External Diameter (mm)
Nominal Diameter (DN)
Numbers of Tracer
Tracer Fixation
Thickness (mm)
20
26.7
15
1
Heat Transfer Cement
20
25
33.4
15
1
Heat Transfer Cement
30
40
48.3
15
1
Heat Transfer Cement
30
50
60.3
15
1
Heat Transfer Cement
30
80
88.9
15
1
Heat Transfer Cement
30
100
114.3
15
1
Heat Transfer Cement
30
150
168.3
15
1
Heat Transfer Cement
30
200
219.1
15
1
Heat Transfer Cement
30
250
273.1
15
1
Heat Transfer Cement
30
300
323.9
15
1
Heat Transfer Cement
30
350
355.6
15
1
Heat Transfer Cement
30
400
406.4
15
1
Heat Transfer Cement
30
450
457.2
15
1
Heat Transfer Cement
30
500
508.0
15
1
Heat Transfer Cement
30
550
558.2
15
1
Heat Transfer Cement
30
600
609.6
15
1
Heat Transfer Cement
30
650
660.4
15
1
Heat Transfer Cement
30
700
711.2
15
1
Heat Transfer Cement
30
750
762.0
15
1
Heat Transfer Cement
30
800
821.8
15
1
Heat Transfer Cement
30
850
863.6
15
2
Heat Transfer Cement
30
900
914.4
15
2
Heat Transfer Cement
30
1050
1066.8
15
2
Heat Transfer Cement
30
RAPID-P0005-TYO-PIP-DES-2000-0003 Attachment-5
TABLE-3
B
TRACING CODE: SM PIPE MAINTENANCE TEMPERATURE: 100 °C < T < 130 °C
Type of heating medium: Medium Pressure Steam, 19 barg / 275 °C, Saturated temperature 212.4 °C General air condition – Design Minimum temperature: 20 °C Main Line
Tracer
Insulation
Nominal Diameter (DN)
External Diameter (mm)
Nominal Diameter (DN)
Numbers of Tracer
Tracer Fixation
Thickness (mm)
20
26.7
15
1
Heat Transfer Cement
30
25
33.4
15
1
Heat Transfer Cement
30
40
48.3
15
1
Heat Transfer Cement
30
50
60.3
15
1
Heat Transfer Cement
30
80
88.9
15
1
Heat Transfer Cement
40
100
114.3
15
1
Heat Transfer Cement
40
150
168.3
15
1
Heat Transfer Cement
40
200
219.1
15
1
Heat Transfer Cement
40
250
273.1
15
1
Heat Transfer Cement
40
300
323.9
15
1
Heat Transfer Cement
40
350
355.6
15
1
Heat Transfer Cement
40
400
406.4
15
1
Heat Transfer Cement
40
450
457.2
15
2
Heat Transfer Cement
40
500
508.0
15
2
Heat Transfer Cement
40
550
558.2
15
2
Heat Transfer Cement
40
600
609.6
15
2
Heat Transfer Cement
40
650
660.4
15
2
Heat Transfer Cement
40
700
711.2
15
2
Heat Transfer Cement
40
750
762.0
15
3
Heat Transfer Cement
40
800
821.8
15
3
Heat Transfer Cement
40
850
863.6
15
3
Heat Transfer Cement
40
900
914.4
15
3
Heat Transfer Cement
40
1050
1066.8
15
3
Heat Transfer Cement
40
RAPID-P0005-TYO-PIP-DES-2000-0003 Attachment-6
Calculation Basis for Number and Size of Tracers Basis of Calculation for Decision of Number of Tracers is in accordance with “THERMAL INSULATION HANDBOOK” (by William C. Turner; Publisher: Krieger Pub Co; 2nd edition (June 1, 1969)).
Case 1 : Fluid in traced pipe is flowing
Q = Qi + Qo
Qi =
Qo =
Ta − Ti = πd i1a a (Ta − Ti ) d i1 1 1 ln( ) + 2πli di2 πd i1a a Ta − To d 1 1 1 λn( o1 ) + + d o2 πd o1a o πd o 2a a 2πλi
Q = nπd t1a a (Tt − Ta )
(1) (2)
(3)
(4)
The equation (5) is calculated from equation (1) through (4):
Ta =
1 To R 1 d i1 a a + n d t1 a a + R
d i1 a a Ti + n d t1 a a Tt +
(5)
where
R=
1 2 λo
λn(
d o1 1 1 )+ + d o2 d o1 a o d o 2 a a
If Ta ≥ Ti is satisfied, it is judged that number of tracers is sufficient enough to keep maintenance temperature. Case 2 : Fluid in traced pipe is not flowing
Q = Qi + Qo In this case Qi need not be considered, hence:
Qi = 0 Q = Qo Ta =
(6)
1 To R 1 n d t1 a a + R
n d t1 a a Tt +
(7)
RAPID-P0005-TYO-PIP-DES-2000-0003 Attachment-6
where Q: Qi : Qo : To : Ti : Ta :
Heating value from tracer [kcal / (m * h)] Heating value to process fluid [kcal / (m * h)] Qo Heating value to atmosphere [kcal / (m * h)] Temperature at atmosphere [deg C] Temperature of Fluid [deg C] Temperature of air layer between insulation and process pipe [deg C] Ta T t : Temperature of Tracer [deg C] α o : Heat transfer coefficient at the surface of Insulation [ 20 kcal / (h * m2 * deg C)] α a : Heat transfer coefficient between insulation and process pipe [ 5 kcal / (h * m2 * deg C)] λ o : Thermal conductivity of insulation [kcal / (h * m * deg C)] λ i : Thermal conductivity of process pipe [kcal / (h * m * deg C)] n: Number of tracers d o1 , d o2 : Outside / Inside diameter of insulation d i1 , d i2 : Outside / Inside diameter of process pipe d t1 , d t2 : Outside / Inside diameter of tracer
To Qo
Ti
Qi QT
Case 3 : Heat Transfer Compound is provided between tracer pipe and process pipe
Qo = Qa + Qb
(8)
Qi = Qb
(9)
Qi = n qi S1 (Tt − Ti )
(10)
Qb = (π d i1 − n S1 ) a a (Ti − Ta )
(11)
Qa = n S 2 a a (Tt − Ta )
(12)
Qo =
Ta − To d 1 1 1 + λn( o1 ) + 2πλo πd o1a o πd o 2a a d o2
Ta = Ti −
nqi S1 (Tt − Ti ) (πd i1 − nS1 )a a
(13)
(14)
The equation (15) is calculated from equation (8) through (13)
Ti =
where
K To )+ R' R' 1 K + A + AK + BK + R' R'
Tt ( A + AK + BK +
A = nS 2a a B = (πd i1 − nS1 )a a
(15)
RAPID-P0005-TYO-PIP-DES-2000-0003 Attachment-6
nqi S1 nq S = i 1 (πd i1 − nS1 )a a B d 1 1 1 R λn( o1 ) + + = R' = 2πλo d o2 πd o1α o πd o 2α α π K=
S1 : S2 : qi :
Contact area between heat transfer compound and process pipe [m2] Qo Contact area between heat transfer compound and air layer inside insulation [m2] Heat transfer coefficient in case that heat transfer compound is used and radiant heat of tracer is transferred to process pipe [kcal / (h * m2 * deg C)] qi = 167 qi = 159 qi - 142 qi = 131 qi = 116
Qa : Qb : Qi : Qo :
(DN 40 and under) (DN 50) (DN 80) (DN 100) (DN 150)
qi = 105 qi = 89 qi = 71 qi = 59 qi = 47
To Qo
Ta
Tt (DN 200) (DN 250) (DN 300) (DN 350) (DN 400 and larger)
Qi
Ti Qb Qa
(quoted from “Thermal Insulation Handbook”) Heat value from tracer to air layer inside insulation [kcal / (m * h)] Heat value from process pipe to to air layer inside insulation [kcal / (m * h)] Heat value from tracer to process pipe [kcal / (m * h)] Heating value to atmosphere [kcal / (m * h)]
RAPID-P0005-TYO-PIP-DES-2000-0003 Attachment-7 (1/3)
RAPID-P0005-TYO-PIP-DES-2000-0003 Attachment-7 (2/3)
RAPID-P0005-TYO-PIP-DES-2000-0003 Attachment-7 (3/3)
RAPID-P0005-TYO-PIP-DES-2000-0003 Attachment-8 (1/4)
B
DELETED
RAPID-P0005-TYO-PIP-DES-2000-0003 Attachment-8 (2/4)
RAPID-P0005-TYO-PIP-DES-2000-0003 Attachment-8 (3/4)
RAPID-P0005-TYO-PIP-DES-2000-0003 Attachment-8 (4/4)
RAPID-P0005-TYO-PIP-DES-2000-0003 Attachment-9 Typical Installation Detail
As a rule, steam tracers shall be arranged as per following sketches. Fig-1: For Piping (1/2 – 2/2) Fig-2: For Control Valves (1/2 – 2/2) Fig-3: For Vessel Nozzles (1/1) Fig-4: For In-line Instruments and Equipment (1/3 – 3/3) Fig-5: For Sampling Points (1/1) Fig-6: For Pump Piping and Pump (1/4 – 4/4)
B
RAPID-P0005-TYO-PIP-DES-2000-0003 Attachment-9 Typical Installation Detail
Fig-1 For Piping (1/2)
B
RAPID-P0005-TYO-PIP-DES-2000-0003 Attachment-9 Typical Installation Detail Fig-1 For Piping (2/2)
B
RAPID-P0005-TYO-PIP-DES-2000-0003 Attachment-9 Typical Installation Detail Fig-2: For Control Valves (1/2)
DELETED
B
DELETED B
B
Flange connection to be provided on tracer for control valve.
B
Flange connection to be provided on tracer for control valve.
RAPID-P0005-TYO-PIP-DES-2000-0003 Attachment-9 Typical Installation Detail Fig-2: For Control Valves (2/2)
B
B
Flange connection to be provided on tracer for control valve.
RAPID-P0005-TYO-PIP-DES-2000-0003 Attachment-9 Typical Installation Detail Fig-3: For Vessel Nozzles (1/1)
B
Flange connection on tracer for dismantling
B
Flange connection on tracer for dismantling
B
RAPID-P0005-TYO-PIP-DES-2000-0003 Attachment-9 Typical Installation Detail Fig-4: For In-Line Instruments and Equipment (1/3)
B
Tubing can be applied If difficult to install tracer piping
Flange connection on tracer for dismantling
B
RAPID-P0005-TYO-PIP-DES-2000-0003 Attachment-9 Typical Installation Detail Fig-4: For In-Line Instruments and Equipment (2/3)
B
B
Flange connection on tracer for dismantling
Tracer to be run along with bottom of discharge flange of PSV and piping.
B
Flange connection on tracer for dismantling
B
Flange connection on tracer for dismantling B
B Flange connection on tracer for dismantling
Flange connection on tracer for dismantling B
Flange connection on tracer for dismantling B
B Flange connection on tracer for dismantling
Flange connection on tracer for dismantling
RAPID-P0005-TYO-PIP-DES-2000-0003 Attachment-9 Typical Installation Detail Fig-4: For In-Line Instruments and Equipment (3/3)
B
Flange connection on tracer for dismantling B
Flange connection on tracer for dismantling
Flange connection on tracer for dismantling B
B
RAPID-P0005-TYO-PIP-DES-2000-0003 Attachment-9 Typical Installation Detail
Fig-5: For Sampling Points (1/1)
B
RAPID-P0005-TYO-PIP-DES-2000-0003 Attachment-9 Typical Installation Detail
Fig-6: For Pump Piping and Pump (1/3)
B
RAPID-P0005-TYO-PIP-DES-2000-0003 Attachment-9 Typical Installation Detail Fig-6: For Pump Piping and Pump (2/3)
B
RAPID-P0005-TYO-PIP-DES-2000-0003 Attachment-9 Typical Installation Detail Fig-6: For Pump Piping and Pump (3/3)
B