DEP SPECIFICATION
SYMBOLS SYMBOL S AND IDENTIFICATION IDENTIFICATION SYSTEM - MECHANICAL e l a s e r r o f t o N . l l e h S m o r f e s n e c i l t u o h t i w d e t t i m r e p g n i k r o w t e n r o n o i t c u d o r p e r o N . s e i n a p m o C f o p u o r G l l e h S t h g i r y p o C
DEP 31.10.03.10-Gen. February 2013
DESIGN AND ENGINEERING PRACTICE
© 2013 Shell Group of companies All rights reserved. No part of this publication may be reproduced, stored in a retrieval system, published or transmitted, in any form or by any means, without the prior written permission of the copyright owner or Shell Global Solutions International BV.
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PREFACE DEP (Design and Engineering Practice) publications reflect the views, at the time of publication, of Shell Global Solutions International B.V. (Shell GSI) and, in some cases, of other Shell Companies. These views are based on the experience acquired during involvement with the design, construction, operation and maintenance of processing units and facilities. Where deemed appropriate DEPs are bas ed on, or reference international, regional, national and industry standards. The objective is to set the standard for good design and engineering practice to be applied by Shell companies in oil and gas production, oil refining, gas handling, gasification, chemical processing, or any other such facility, and thereby to help achieve maximum technical and economic benefit from standardization. The information set forth in these publications is provided to Shell companies for their consideration and decision to implement. This is of particular importance where DEPs may not cover every requirement or diversity of condition at each locality. The system of DEPs is expected to be sufficiently flexible to allow individual Operating Units to adapt the information set forth in DEPs to their own environment and requirements. When Contractors or Manufacturers/Suppliers use DEPs, they shall be solely responsible for such use, including the quality of their work and the attainment of the required design and engineering standards. In particular, for those requirements not specifically covered, the Principal will typically expect them to follow those design and engineering practices that will achieve at least the same level of integrity as reflected in the DEPs. If in doubt, the Contractor or Manufacturer/Supplier shall, shall, without detracting from his own respons bility, consult the Principal. The right to obtain and to use DEPs is restricted, and is typically granted by Shell GSI (and in some cases by other Shell Companies) under a Service Agreement or a License Agreement. This right is granted primarily to Shell companies and other companies receiving technical advice and services from Shell GSI or another Shell Company. Consequently, three categories of users of DEPs can be distinguished: 1)
Operating Units having a Service Agreement with Shell GSI or another Shell Company. The use of DEPs DEPs by these Operating Units is subject in all respects to the terms and conditions of the relevant Service Agreement.
2)
Other parties who are authorised to use DEPs subject to appropriate contractual arrangements (whether as part of a Service Agreement or otherwise).
3)
Contractors/subcontractors Contractors/subcontra ctors and Manufacturers/Supplie Manufacturers/Suppliers rs under a contract with users referred to under 1) or 2) which requires that tenders for projects, materials supplied or - generally - work performed on behalf of the said users comply with the relevant standards.
Subject to any particular terms and conditions as may be set forth in specific agreements with users, Shell GSI disclaims any liability of whatsoever nature for any damage (including injury or death) suffered by any company or person whomsoever as a result of or in connection with the use, application or implementation of any DEP, combination of DEPs or any part thereof, even if it is wholly or partly caused by negligence on the part of Shell GSI or other Shell Company. The benefit of this disclaimer shall inure in all respects to Shell GSI and/or any Shell Company, or companies affiliated to these companies, that may issue DEPs or advise or require the use of DEPs. Without prejudice to any specific terms in respect of confidentiality under relevant contractual arrangements, DEPs shall not, without the prior written consent of Shell GSI, be disclosed by users to any company or person whomsoever and the DEPs shall be used exclusively for the purpose for which they have been provided to the user. They shall be returned after use, including any copies which shall only be made by users with the express prior written consent of Shell GSI. The copyright of DEPs vests in Shell Group of companies. Users shall arrange for DEPs to be held in safe custody and Shell GSI may at any time require information satisfactory to them in order to ascertain how users implement this requirement. All administrative administrative queries should be be directed to the DEP Administrator Administrator in Shell GSI. GSI.
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DEP 31.10.03.10-Gen. February 2013 Page 3 TABLE OF CONTENTS 1. 1.1 1.2 1.3 1.4 1.5 1.6 1.7
INTRODUCTION ........................................................................................................ 4 SCOPE........................................................................................................................ 4 DISTRIBUTION, INTENDED USE AND REGULATORY CONSIDERATIONS ......... 4 DEFINITIONS AND ABBREVIATIONS ...................................................................... 4 CROSS-REFERENCES ............................................................................................. 5 SUMMARY OF MAIN CHANGES ............................................................................... 5 COMMENTS ON THIS DEP ....................................................................................... 6 DUAL UNITS ............................................................................................................... 6
2.
GENERAL ...................................................................................................................7
3. 3.1 3.2 3.3 3.4 3.5 3.6 3.7 3.8 3.9 3.10
IDENTIFICATION OF EQUIPMENT ........................................................................... 8 GENERAL ...................................................................................................................8 TRAIN NUMBER "N" (OPTIONAL) ............................................................................. 8 EQUIPMENT FUNCTION CODE " AA ".......................................................................8 PROCESS UNIT NUMBER "XXX".............................................................................. 8 SEQUENCE NUMBER "YY" ....................................................................................... 8 IDENTICAL EQUIPMENT CODE "Z".......................................................................... 9 EXAMPLES OF EQUIPMENT NUMBERS ................................................................. 9 EXAMPLES OF THE LETTER CODES OF TABLE 1 .............................................. 11 EQUIPMENT NUMBERING OF PACKAGE UNITS ................................................. 11 SPECIAL PIPING ITEMS.......................................................................................... 11
4. 4.1 4.2 4.3 4.4 4.5
IDENTIFICATION OF PIPING SYSTEMS ................................................................ 12 GENERAL .................................................................................................................12 LINE NUMBERING ................................................................................................... 12 INSULATION CODES ............................................................................................... 14 EXAMPLES OF LINE NUMBERS IN SI UNITS........................................................ 16 EXAMPLES OF LINE NUMBERS IN US CUSTOMARY UNITS .............................. 17
5. 5.1 5.2 5.3 5.4 5.5
IDENTIFICATION OF TRA NSMISSION PIPELINES AND FL OWLINES ............... 18 GENERAL .................................................................................................................18 PIPELINE/FLOWLINE NUMBERING ....................................................................... 18 INSULATION CODES ............................................................................................... 19 EXAMPLES OF PIPELINE/FLOWLINE NUMBERS IN SI UNITS ............................ 19 EXAMPLES OF PIPELINE/FLOWLINE NUMBERS IN US CUSTOMARY UNITS ....................................................................................................................... 20
6. 6.1 6.2 6.3
IDENTIFICATION OF SPECIA L PIPE SUPPORTS ................................................ 21 GENERAL .................................................................................................................21 PROCESS UNIT NUMBER "XXX"............................................................................ 21 SEQUENCE NUMBER "YYY" .................................................................................. 21
7.
REFERENCES ......................................................................................................... 22
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INTRODUCTION
1.1
SCOPE This DEP specifies requirements and gives recommendations for: a.
Symbols for the graphical presentation of equipment and piping in process flow schemes (PFSs), utility flow schemes (UFSs) process engineering flow schemes (PEFSs) and utility engineering flow schemes (UEFSs).
b.
Identification numbering system for equipment and piping in PFSs, UFSs, PEFSs, UEFSs and other documents.
This is a revision of the DEP of the same number dated February 2012; see (1.5) regarding the changes. 1.2
DISTRIBUTION, INTENDED USE AND REGULATORY CONSIDERATIONS Unless otherwise authorised by Shell GSI, the distribution of this DEP is confined to Shell companies and, where necessary, to Contractors and Manufacturers/Suppliers nominated by them. This DEP is intended for use in facilities related to oil and gas production, gas handling, oil refining, chemical processing, gasification, distribution and supply/marketing. This DEP may also be applied in othe r similar facilities. When DEPs are applied, a Management of Change (MOC) process shall be implemented; this is of particular importance when existing facilities are to be modified. If national and/or local regulations exist in which some of the requirements could be more stringent than in this DEP, the Contractor shall determine by careful scrutiny which of the requirements are the more stringent and which combination of requirements will be acceptable with regard to the safety, environmental, economic and legal aspects. In all cases the Contractor shall inform the Principal of any deviation from the requirements of this DEP which is considered to be necessary in order to comply with national and/or local regulations. The Principal may then negotiate with the Authorities concerned, the objective being to obtain agreement to follow this DEP as closely as possible.
1.3
DEFINITIONS AND ABBREVIATIONS
1.3.1
General defin iti ons
The Contractor is the party that carries out all or part of the design, engineering, procurement, construction, commissioning or management of a project or operation of a facility. The Principal may undertake all or part of the duties of the Contractor. The Manufacturer/Supplier is the party that manufactures or supplies equipment and services to perform the duties specified by the Contractor. The Principal is the party that initiates the project and ultimately pays for it. The Principal may also include an agent or consultant authorised to act for, and on behalf of, the Principal. The word shall indicates a requirement. The word should indicates a recommendation. 1.3.2
Specific definitio ns Term
Definition
Very toxi c (substances)
Substances that are very hazardous for the environment or human health, as specified in DEP 01.00.01.30-Gen. (which also identifies "toxic" substances by reference to chemical substances databases).
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1.4
Abbreviations Term
Definition
PEFS
process engineering flow scheme
PFS
process flow scheme
UEFS
utility engineering flow scheme
UFS
utility flow scheme
CROSS-REFERENCES Where cross-references to other parts of this DEP are made, the referenced section number is shown in brackets. Other documents referenced by this DEP are listed in (5).
1.5
SUMMARY OF MAIN CHANGES This is a revision of the DEP of the same number dated February 2012. The following are the main non-editorial changes. Section
Change
3
Renumbered sections – 3.1, 3.2, 3.3, 3.4, 3.5, 3.6, 3.7 as 3.2, 3.3, 3.4, 3.5, 3.6 and 3.7.
3.1
Incorporated optional concept of train number in identification equipment.
3.2
Incorporated requirement for train number.
3.3
Table 1 has been updated to include subsea equipment codes.
4.1
This section has been revised for the incorporation of identification system for transmission lines and flowlines.
4.2
Renumbered sub-sections 4.2.1, 4.2.2, 4.2.3, 4.2.4, 4.2.5, 4.2.6 as 4.2.2, 4.2.3, 4.2.4, 4.2.5, 4.2.6 and 4.2.7.
4.2.2
Incorporated size in US customary / SI units.
4.2.3
Table 2 has been updated to include additional fluid codes.
4.3
Table 3 has been aligned with DEP 30.46.00.31-Gen and also added additional insulation tags.
4.4
Updated insulation codes in examples.
4.5
Incorporated new section on examples of line numbers in US customary units.
5
Incorporated new section on pipeline/flowline numbering.
6
Incorporated new section on identification of special pipe supports.
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1.6
COMMENTS ON THIS DEP Comments on this DEP may be submitted to the Administrator using one of the following options: Shell DEPs Online
(Users with access to Shell DEPs Online)
Enter the Shell DEPs Online system at https://www.shelldeps.com Select a DEP and then go to the details screen for that DEP. Click on the “Give feedback” link, fill in the online form and submit.
DEP Feedback System
(Users with access to Shell Wide Web)
Enter comments directly in the DEP Feedback System which is accessible from the Technical Standards Portal http://sww.shell.com/standards. Select “Submit DEP Feedback”, fill in the online form and submit.
DEP Standard Form
(Other users)
Use DEP Standard Form 00.00.05.80-Gen. to record feedback and email the form to the Administrator at
[email protected].
Feedback that has been registered in the DEP Feedback System by using one of the above options will be reviewed by the D EP Custodian for potential improvements to the DEP. 1.7
DUAL UNITS This DEP contains both the International System (SI) units, as well as the corresponding US Customary (USC) units, which are given following the SI units in brackets. When agreed by the Principal, the indicated USC values/units may be used.
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GENERAL
Mechanical symbols in PFSs, UFSs, PEFSs and UEFSs shall be in accordance with Standard Drawing S 02.002. These symbols may also be used in other documents where required. Standard Drawing S 02.002 is produced so that the symbols can easily be copied in electronic form. For equipment symbols not shown in this DEP, a simple outline should be drawn, together with a short description of its function. For very complicated equipment hook-ups a rectangle (dot-and-dash line) should be drawn with a reference to a separate scheme. Certain basic symbols have been included for use only in PFSs. The other symbols may be applied in all documents mentioned above. If a symbol is not adequate to indicate the type or function of a piece of equipment, additional notes should be located next to the symbol. For symbols not shown in Standard Drawing S 02.002, the symbols in BS 1553-1 shall be used. For coal handling and preparation plants, the symbols in ISO 561 shall be used. For instrument symbols and identification, and valve actuating methods, reference is made to DEP 32.10.03.10-Gen. and Standard Drawing S 37.000. For electrical symbols, reference is made to IEC 60617 and Standard Drawing S 64.000.
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IDENTIFICATION OF EQUIPMENT
3.1
GENERAL All equipment shall be identified by a tag number of the format: (N-) AA -xxxYYz,
in which “ N”
is an optional train number in case of repetitive trains with identical process units; see (3.2)
" AA " is a one or two-letter code identifying the equipment function in accordance with Table 1; see (3.3); "XXX" is a one, two-digit or three-digit number used to ident ify the process unit; see (3. 4); "YY" is a two-digit sequence number; see (3.5) and "Z" NOTE:
3.2
is a one-letter code applied only to denote identical equipment items used for the same purpose. See (3.6). Refer to (3.8) for the equipment numbering of parallel trains.
TRAIN NUMBER "N" (OPTIONAL) Identical equipment of identical parallel trains shall be given identical equipment numbers, except for the train identifier. The number before the equipment function code indicates the number of the train. Examples:
3.3
for common facilities (e.g., utilities)
N is 0
for train - 1
N is 1
For train -2
N is 2
EQUIPMENT FUNCTION CODE " AA " The equipment function code shall be arranged as follows:
3.4
a.
The first letter shall indicate the equipment type, in accordance with column 1 of Table 1;
b.
The optional second letter shall indicate the supporting function in accordance with column 2 of Table 1.
PROCESS UNIT NUMBER "XXX" Examples:
3.5
for unit
100,
X is 1
for unit
7400,
XX is 74
for unit
15200
XXX is 152
SEQUENCE NUMBER "YY" Sequence numbers shall run consecutively from 01 for each group of equipment in accordance with Table 1, unless flexibility for the addition of future equipment within the same sequence is required.
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IDENTICAL EQUIPMENT CODE "Z" This code is used to denote identical equipment items used for the same purpose, and shall be one of the letters: "A", "B", "C", "D", etc. The letter "S" shall be used with common spare equipment.
3.7
EXAMPLES OF EQUIPMENT NUMBERS Example 1: P-106A, P-106B, P-108S, in which P
equipment function code of a pump
1
process unit 100
6
equipment sequence number of pump 6
A and B
the letters indicating two identical pumps (either working in parallel or in series or equipment with single spare)
S
common spare (e.g., for P-108 and P-109)
Example 2: P-7004A, P-7004B, P-7008S, in which P
equipment function code of a pump
70
process unit 7000
4
equipment sequence number of pump 4
A and B
the letters indicating two identical pumps (either working in parallel or in series or equipment with single spare)
S
common spare (e.g., for P-7008 and P-7009)
Example 3: K-15210A, K-15210B,K-15220S, in which K
equipment function letter code of a compressor
152
process unit 15200
10
equipment sequence number of compressor 10
A and B
the letters indicating two identical compressors (either working in parallel or in series or compressor with single spare)
S
common spare (e.g., for K-15220 and K-15221)
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Table 1 Letter
Equipment funct ion codes
Column 1 (Equipment type)
Column 2 (Supporting function)
A
Packaged units and miscellaneous equipment, e.g., extruders, crushers, cutters, kneaders, crystallisers, pelletisers
Aerial, Air Motor
B
Buildings, rooms, enclosures, containers
C
Columns : tray columns packed columns rotating disc contactors
Chamber
D
Drying equipment
Diesel engine, Damper
E
Unfired heat transfer equipment: heat exchangers condensers air-cooled heat exchangers reboilers
• • • •
F
Fired equipments, furnaces, heaters, steam boilers, flare tip
Fan
G
Generator
Gearbox
H
Heaters; electrical
Hydraulic motor
I
See Note 2
J
Jets (ejectors, injectors and eductors)
K
Compressors, blowers, fans, turboexpanders
L
Pig Launchers
M
Mixers, stirrers, mixing nozzles, blenders, steam desuperheaters, agitators, piping manifolds
Electric motor
N
Not assigned
Natural gas engine
O
See Note 2
P
Pumps (centrifugal, reciprocating, rotary), PLET (pipeline end termination)
Q
Not assigned
R
Pig Receivers
S
Gravity and mechanical separators, e.g., thickeners, cyclones, expellers, centrifuges, filters, dust collectors, sieves, hydrocyclones
Shell, Fan Silencer
T
Atmospheric storage tanks, interceptors, neutralising pits
Turbine (steam or gas), Tube
U
Umbilical, incl. distribution equipment
V
Vessels, incl. pressure storage vessels, silos and hoppers
W
Weighing equipment, wellheads
X
Stationary transport equipment, material handling equipment, cranes, hoists
Y
Special piping item
Z
Bulk loading arms, offloading buoys
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DEP 31.10.03.10-Gen. February 2013 Page 11 NOTES:
1. Where a choice has to be made between two or more letters, the most important function of the equipment shall prevail. If, for example, a jet is used for mixing purposes, M is preferred to J. 2. The letters I and O should not be used to avoid confusion with the numbers 1 and 0.
3.8
3.9
EXAMPLES OF THE LETTER CODES OF TABLE 1 EG
Gearbox of heat transfer equipment (e.g., fin-fans)
GT
Turbine of generator
KT
Turbine of compressor
PD
Diesel engine of pump
PG
Gearbox of pump
PM
Electric motor of pump
EM
Electric motor of air-cooled heat exchanger
EQUIPMENT NUMBERING OF PACKAGE UNITS The package unit shall be given a number as described above. The first digit of the sequence number "YY" should be allocated so that this digit is identical for all equipment in the package unit. Equipment inside a package unit shall be numbered using an equipment identifier, of which the first number(s) is (are) identical to the package-unit identifier. Example: Process unit 15000 Package unit number: A-15100 E-15101 P-15101 etc.
3.10
SPECIAL PIPING ITEMS Piping components not typically specified in piping classes, like certain types of blowdown valves, non-slam check valves, injection quills and non standard thermowell or branch devices shall be defined as special piping items. Example: Y-106, in which Y
special piping item
1
process unit 100
6
equipment sequence number of special piping item is 6
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DEP 31.10.03.10-Gen. February 2013 Page 12 4.
IDENTIFICATION OF PIPING SYSTEMS
4.1
GENERAL All piping systems with piping classes in PEFSs, UEFSs and piping drawings shall be identified by a line number consisting of the following components (see 4.2), This form of identification should be applied to all plant piping where piping classes are developed to effectively manage piping selection, design and procurement of bulk items. The alternative identification format specified in (5) shall be applied only with approval of the Principal and only to transmission pipelines and flowlines that are typically custom engineered for the service and fall outside the scope of plant piping codes such as ASME B31,3, Line number example based on SI units: (1-)100-P3001 - 31011- 4EN
1
100
P
3
001
31011
3HH
Train number 1 (optional)
Size Nominal Diameter (DN)
Fluid
Process Unit Number 300
Sequence number
Piping class identification in accordance with
Insulation code see (4.3)
Code
DEP 31.38.01.12-Gen. and DEP 31.38.01.15-Gen.
Line numbering – See (4.2) Line number example based on US customar y units: (1-)4”-P3001 - 31011- 4EN 1
4”
P
3
001
31011
3HH
Train number 1 (optional)
Size Nominal Pipe Size (NPS)
Fluid
Process Unit Number 300
Sequence number
Piping class identification in accordance with
Insulation code see (4.3)
Code
DEP 31.38.01.12-Gen. and DEP 31.38.01.15-Gen.
Line numbering – See (4.2) NOTE:
On offshore platforms, a location code may be inserted between the piping class identification and the insulation code. If so applied, t he Principal shall define the location codes.
4.2
LINE NUMBERING
4.2.1
Train number "N" (optional)
Examples:
4.2.2
for common facilities (e.g., utilities)
N is 0
for train - 1
N is 1
For train -2
N is 2
Size
Size of piping system is nominal pipe size. Pipe size shall be designated as DN number for SI units and as NPS for US customary units.
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Fluid cod e
To indicate the type of fluid, the codes in Table 2 shall be used. Table 2
4.2.4
Process
P
Inert gas
G
Steam/condensate
S
Water
W
Air
A
Drain
D
Fuel
F
Refrigeration
R
Blowdown and relief
B
Corrosion Inhibitor
C
Methanol
H
Low Dosage Hydrate Inhibitor (LDHI)
L
Paraffin (wax) Inhibitor
X
Scale Inhibitor
E
Spare
Z
Asphaltene Solvent
V
Asphaltene Inhibitor
N
Chemical (other)
Q
Fluid codes The letter P may be replaced, if desired, by: M for slurry lines T for very toxic material
Typically used for undesignated subsea umbilical lines
Process unit numb ers
The process unit numbers correspond to those assigned to the associated equipment as described in (3.4). 4.2.5
Line sequence numb ers
The sequence number for the line shall be a three-digit number from 001 to 999. 4.2.6
Assig ning line identific ations
Process and utility lines shall be numbered from equipment to equipment. Where there is a considerable change in the pressure, volume or temperature, the numbering shall also be changed. This normally occurs at piping class/fluid service changes or major branches. Parallel lines shall be numbered separately. In order to facilitate assignment of line sections to (construction) modules, the Principal may allocate specific module codes to the sequence number of the line identification. Piping passing from one unit to another, either directly or indirectly via a pipe bridge, pipe track or other interconnecting system, shall be given line numbers corresponding to the unit of origin, seen in the direction of flow. Lines entering a unit from other sources and not included in any other identification system shall be given line numbers corresponding to the unit they enter.
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DEP 31.10.03.10-Gen. February 2013 Page 14 Utility headers on common pipe bridges or tracks not entering a specific unit shall be given a line number corresponding to the unit of origin, seen in the direction of flow. Utility lines from utility headers entering a processing unit shall be given number(s) of that unit. 4.3
INSULATION CODES The insulation code to designate insulation systems shall be a two- or three-letter code, as follows: a.
The first number shall indicate the temperature operating window (TOW) in accordance with Table 3.
b.
The second letter shall indicate the primary insulation function in accordance with Table 3.
c.
The third letter shall indicate the secondary insulation function in accordance with Table 3. 1)
The applicable codes are provided in Table 3 . NOTE:
1. Insulation codes derived from (2.2.2), DEP 30.46.00.31-Gen. Possible codes are provided in Appendix I, DEP 30.46.00.31-Gen.
Table 3
TOW
Tagging system for thermal and acoustic insul ation on PFS and PEFs for line identification Temperature indication
Process temperature
CUI Category
1
Cold or cryogenic
All process temperatures < –5 ºC (25 °F)
Low Cold
2
Ambient (+/-)
Process temperatures between –5 ºC and 50 ºC (25 and 121 °F)
Medium
3
Hot
Process temperatures between 50 ºC and 175 ºC (122 and 347 °F)
High
4
Very hot
All process temperatures > 175 ºC (347 °F)
Low Hot
5
Variable or cycling
Cycling or dual process temperatures between –20 ºC and 320 ºC ( -4 and 608 °F) (or lower)
Extreme
Primary Insulation Function
Description pr imary insulation function
A
Acoustic (or noise control) insulation system: reducing/controlling noise in piping, valves. (see DEP 31.46.00.31-Gen)
C
Cold insulation system: to minimize cold/energy loss and mitigate condensation by keeping surface temperature above the dew point of surrounding air.
F
Freeze protection (winterisation): minimizing energy required for heat tracing systems and/or extending the time to freezing i n the event of system failure.
H
Hot insulation system. Always energy conservation: minimizing unwanted heat loss/gain from piping and equipment, as well as preserving natural and financial resources (reducing CO2)
N
Not Required where it may be expected (e.g., piping/equipment only used for start up or venting etc.)
P
Personnel protection: controlling surface temperatures to avoid contact burns (hot or cold)
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Primary Insulation Function
Description pr imary insulation function
S
Fire safety: provide passive fire protection of critical products in piping and/or equipment.
T
Temperature control: temperature control of processes or products, to avoid, e.g., solidification or changing of viscosities.
V
Insulation system for dual, cycling or variable operating temperatures
”Blank”
Not insulated (e.g., ambient rundown lines to tank farm)
Secondary Insulation Function
Description secondary insulation fu nction
A
Acoustic insulation system Class A
B
Acoustic insulation system Class B
C
Acoustic insulation system Class C
D
Acoustic insulation system Class D
E
Insulation system for electrically heat traced pipe
G
Guards by means of metal screens for personnel protection
H
Heat gain and energy conservation (including CO2 reduction)
I
Ignition prevention
J
Jacketed (pipe-in-pipe)
O
Insulation system for hot oil heat traced pipe
S
Insulation system for steam traced pipe
U
Buried
W
Avoiding condensation and water dripping of cold insulation systems
X
Avoiding condensation and water dripping of cold insulation systems and reducing of heat gain.
”Blank”
Function not required or unknown.
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4.4
EXAMPLES OF LINE NUMBERS IN SI UNITS Example 1
Example 2
1-100-P6002-31011-3HH
100-S43005-91011-4TS
in which:
in which:
1 100 P 6
002
31011 3HH
= train 1 = nominal pipe diameter (DN) = fluid code for process, see (4.2) = unit identifier for process unit 600, see (3.4) = line sequence number = piping class; ASME rating class 300 Process temperatures between 50 °C and 175 °C. Hot insulation system for heat conservation
100
= nominal pipe diameter (DN)
S
= fluid code for steam, see (4.2) = unit identifier for process unit 4300, see (3.4) = line sequence number
43
005
91011 4TS
= piping class; ASME rating class 900 All process temperatures > 175 °C. Insulation system for temperature control for process purposes (avoiding inside condensation, solidification, etc.) by means of steam tracing.
Example 3
Example 4
100-G152125-61011-A in which:
100-W8003-17061 in which:
100
= nominal pipe diameter (DN)
100
= nominal pipe diameter (DN)
G
= fluid code for gas, see (4.2)
W
=
152
= unit identifier for process unit 15200, see (3.4)
8
= unit identifier unit 600, see (3.4)
125
= line sequence number
003
= line sub-number
G150125
= line number
W8003
=
61011
= piping class; ASME rating class 600
17320
= piping class, glass fibre reinforced epoxy
A
water, see (4.2)
line number
No insulation required for process temperature reasons Acoustic insulation system Class A
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DEP 31.10.03.10-Gen. February 2013 Page 17 4.5
EXAMPLES OF LINE NUMBERS IN US CUSTOMARY UNITS Example 1
Example 2
1-4”-P6002-31011-3HH
4”-S43005-91011-4TS
in which:
in which:
1 4” P 6
002
31011 3HH
= train 1 = nominal pipe size (NPS) = fluid code for process, see (4.2) = unit identifier for process unit 600, see (3.4) = line sequence number = piping class; ASME rating class 300 Process temperatures between 120 °F and 350 °F. Hot insulation system for heat conservation
4”
= nominal pipe size (NPS)
S
= fluid code for steam, see (4.2) = unit identifier for process unit 4300, see (3.4) = line sequence number
43
005
91011 4TS
= piping class; ASME rating class 900 All process temperatures > 350 °F. Insulation system for temperature control for process purposes (avoiding inside condensation, solidification, etc.) by means of steam tracing.
Example 3
Example 4
4”-G152125-61011-A in which:
4”-W8003-17320 in which:
4”
= nominal pipe size (NPS)
4”
= nominal pipe size (NPS)
G
= fluid code for gas, see (4.2)
W
=
152
= unit identifier for process unit 15200, see (3.4)
8
= unit identifier unit 600, see (3.4)
125
= line sequence number
003
= line sub-number
G150125
= line number
W8003
=
61011
= piping class; ASME rating class 600
17320
= piping class, glass fibre reinforced epoxy
A
water, see (4.2)
line number
No insulation required for process temperature reasons Acoustic insulation system Class A
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DEP 31.10.03.10-Gen. February 2013 Page 18 5.
IDENTIFICATION OF TRANSMISSION PIPELINES AND FLOWLINES
5.1
GENERAL The application of this format shall be subject to approval by Principal and shall only be applied, by exception to (4), to pipelines and flowline systems, including subsea, that fall outside the scope of plant and facility piping and associated piping classes, and are typically designed and constructed to pipeline codes. It shall not be construed as an alternate to identification through piping class as specified in (4) for piping systems that are subject to piping class identification. Pipeline/flowline number example based on SI units: 273 - P8001 – 25-X65- N
273
P
8
001
25
X65
N
Actual Line OD mm
Fluid
Process Unit Number 800
Sequence number
Wall Thickness in mm
Material (Grade or Yield Strength)
Insulation code see (4.3)
Code
Line numbering – See (5.2) Pipeline/flowline number example based on US customar y units: 10.750” - P8001 – 1.000-X65- N
10.750”
P
8
001
1.000
X65
N
Actual Line OD inches
Fluid
Process Unit Number 800
Sequence number
Wall Thickness in inches
Material (Grade or Yield Strength)
Insulation code see (4.3)
Code
Line numbering – See (5.2) NOTE:
On offshore platforms, a location code may be inserted between the piping class identification and the insulation code. If so applied, t he Principal shall define the location codes.
5.2
PIPELINE/FLOWLINE NUMBERING
5.2.1
Act ual Lin e OD
The Actual Line OD is the measured pipe outer diameter in accordance with ISO 3183. 5.2.2
Fluid cod e
See Table 2 in (4.2.3). 5.2.3
Process unit numb ers
The process unit numbers correspond to those assigned to the associated equipment as described in (3.4). 5.2.4
Line sequence numb ers
The sequence number for the line shall be a three-digit number from 001 to 999. 5.2.5
Wall Thick ness
The Wall Thickness is the specified wall thickness of the pipe. 5.2.6
Material (grade or yield strength )
Material is used to specify the chemical makeup of the piping.
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DEP 31.10.03.10-Gen. February 2013 Page 19 5.2.7
Assig ning line identific ations
Process and utility lines shall be numbered from apparatus to apparatus. Where there is a change in the pipeline/flowline specifications (i.e., Actual Line OD, wall thickness, material, or insulation), the numbering shall also be changed. Parallel lines shall be numbered separately. Flowlines passing from one unit to another shall be given line numbers corresponding to the unit of origin, seen in the direction of flow. Flowlines entering a unit from other sources and not included in any other identification system shall be given line numbers corresponding to the unit they enter. 5.3
INSULATION CODES See Table 3 in (4.3)
5.4
EXAMPLES OF PIPELINE/FLOWLINE NUMBERS IN SI UNITS Example 1
Example 2
273- P8001 – 25-X65- 5HH
219- P8001 – 20-X70-5HJ
in which:
in which:
273 P
= Actual Line OD = fluid code for process, see (4.2) = unit identifier for process unit 800, see (3.4) = line sequence number
219 P
25
= wall thickness
20
= wall thickness
X65
= material (grade or strength)
X70
= material (grade or strength)
5HH
Cycling or dual process temperatures between -20 °C and 320 °C. Thermal conservation of equipment and piping. Contact insulation (wet-insulated subsea piping)
5HJ
Cycling or dual process temperatures between -20 °C and 320 °C. Thermal conservation of equipment and piping. Pipe-in-Pipe insulation.
8
001
8
001
= Actual Line OD = fluid code for process, see (4.2) = unit identifier for process unit 800, see (3.4) = line sequence number
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DEP 31.10.03.10-Gen. February 2013 Page 20
5.5
EXAMPLES OF PIPELINE/FLOWLINE NUMBERS IN US CUSTOMARY UNITS Example 1
Example 2
10.750”- P8001 – 1.000-X65- 5HH
8.625”- P8001 – 0.75-X70-5HJ
in which:
in which:
10.750” P
= Actual Line OD = fluid code for process, see (4.2) = unit identifier for process unit 800, see (3.4) = line sequence number
8.625” P
1.000
= wall thickness
0.75
= wall thickness
X65
= material (grade or strength)
X70
= material (grade or strength)
5HH
Cycling or dual process temperatures between -4 °F and 600 °F. Thermal conservation of equipment and piping. Contact insulation (wet-insulated subsea piping)
5HJ
Cycling or dual process temperatures between -4 °F and 600 °F. Thermal conservation of equipment and piping. Pipe-in-Pipe insulation.
8
001
8
001
= Actual Line OD = fluid code for process, see (4.2) = unit identifier for process unit 800, see (3.4) = line sequence number
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DEP 31.10.03.10-Gen. February 2013 Page 21 6.
IDENTIFICATION OF SPECIAL PIPE SUPPORTS
6.1
GENERAL Definition of special pipe support is contained in DEP 31.38.01.29-Gen. All special pipe supports shall be identified by a tag number of the format: SPS-xxx-YYY,
in which "XXX" is a one, two-digit or three-digit number used to identify the process unit; see (6.2); "YYY" is a three-digit sequence number; see (6.3) 6.2
PROCESS UNIT NUMBER "XXX" The process unit numbers correspond to those assigned to the associated equipment as described in (3.4).
6.3
SEQUENCE NUMBER "YYY" The sequence number for the pipe support shall be a three-digit number from 001 to 999.
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DEP 31.10.03.10-Gen. February 2013 Page 22 7.
REFERENCES
In this DEP, reference is made to the following publications: NOTES:
1. Unless specifically designated by date, the latest edition of each publication shall be used, together with any amendments/supplements/revisions thereto. 2. The DEPs and most referenced external standards are available to Shell staff on the SWW (Shell Wide Web) at http://sww.shell.com/standards/.
SHELL STANDARDS
DEP feedback form
DEP 00.00.05.80-Gen.
Definition of temperature, pressure and toxicity levels
DEP 01.00.01.30-Gen.
Thermal insulation
DEP 30.46.00.31-Gen.
Piping classes – Refining and chemicals
DEP 31.38.01.12-Gen.
Piping classes – Exploration and production
DEP 31.38.01.15-Gen.
Pipe supports
DEP 31.38.01.29-Gen.
Acoustic insulation for piping (amendments/supplements to ISO 15665)
DEP 31.46.00.31-Gen.
Instrumentation symbols and identification on process engineering flow schemes
DEP 32.10.03.10-Gen.
STANDARD DRAWINGS
Mechanical symbols for use on flow schemes: sheet 1
pipe symbols and pipe indicators
sheet 2
general and valves
sheet 3
vessels and tanks
sheet 4
columns and internals
sheet 5
pumps, compressors, blowers and fans
sheet 6
separators and filters
sheet 7
mixers
sheet 8
heat transfer equipment
sheet 9
drying equipment
sheet 10
furnaces
sheet 11
miscellaneous equipment
sheet 12
data identification (SI units)
sheet 13
data identification (US Customary units)
S 02.002
PEFS legend for instrument symbols and identification – based on ISO: sheets 1 - 5
S 37.000
Electrical symbols in addition to IEC 617
S 64.000
BRITISH STANDARD
Specification for graphical symbols for general engineering – Part 1: Piping systems and plant
BS 1553-1
INTERNATIONAL STANDARDS
Graphical symbols for diagrams
IEC 60617
Coal preparation plant – Graphical symbols
ISO 561
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DEP 31.10.03.10-Gen. February 2013 Page 23
Petroleum and natural gas industries — Steel pipe for pipeline transportation systems
ISO 3183
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