Engineering Tv Nc 2004

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E N G I N EE R E DS Y S T E M S

Elastopipe / Engineering

Design basis:Drawings – Survey – Photo/VideoNorsok Technical Safety – NFPA

Design:Pipenet flow analysisSolidWorks / Routing - Bill of materialsSupport for Elastopipe – Design report

Verification:Function test – full scale

TVNC 2004 Agenda

PhotoModeler Software: Image-Based Engineering Measurement Software Page 1 of 2

http://www.photomodeler.com/app07.html 05.05.2003

Measuring and Modeling the Real World

PhotoModeler Pro software has many capabilities and features that support the requirements of plant and mechanical engineers. Our latest version, Pro 4.0, has added capabilities that are specifically designed to help create accurate 3D models and measurements of piping, process plant structures and mechanical parts.

T k th Pl t d M h i l E i i T d l h Ph t M d l i i d

With PhotoModeler Pro, you can

Generate as-built drawings Perform high-density surface models Measure and Model existing installations andequipment Do reverse-modeling of mechanical parts Model cylindrical objects such as pipes andvessels without pre-targeting Generate 3D models of existing plants and pipingstructures Assist in the design and maintenance of process,oil & gas and power plants Export models for use in CAD programs

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Generate as-built drawings

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Measure and Model existing installations and

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equipment

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Generate 3D models of existing plants and piping

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structures

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Export models for use in CAD programs

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TVNC 2004 Agenda

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Norsok Technical Safety – NFPA

Technical Safety S-001 Rev. 3, Jan. 2000

NORSOK standard Page 58 of 66

H.2 Fire Water Piping, Valves and Nozzles

General• It shall be possible to start the fire water pump system without delay and without causing

unacceptable pressure surges. A pressure surge study shall be performed. Means that may beconsidered for eliminating pressure surge problems are pressure vacuum valves, soft closingminimum flow valves, pressurised overhead tanks, etc.

• The deluge and monitor skid cabinets shall have doors with sufficient stopper arrangements toprevent a personnel risk associated with the cabinet doors in strong winds. The skids shallwithstand the applicable explosion loads.

• The deluge system shall comply with NFPA 16, Deluge Foam - Water System.• The sprinkler system shall comply with NFPA 13, Sprinkler Systems.• Deluge, monitor and sprinkler valves shall fail in last position upon loss of signal from F&G

logic.• The system design shall allow for complete system flushing in commissioning and operation.

Fire Water Piping• For general piping requirements, reference is made to NORSOK P-001, clause 8 and L-002 clause

4.7.• There shall be a minimum of two pressure transmitters in the Fire Water Ring main providing the

low-pressure start signal to the firewater pump diesels.• The FireWater Ring main shall be equipped with two points (min 6”) for connection to external

water supply for commissioning. (SOLAS international shore couplings should be used.)• The fire water piping system shall be fitted with sufficient number of high point vents to achieve

the following:• Efficient frost protection at all locations.• Efficient removal of all entrained air pockets in the water.• All low points in piping downstream deluge and monitor skids shall be equipped with 3 mm weep

wholes to prevent pockets of water to be entrained. The weep holes shall be considered in thefirewater demand calculations.

• Sprinkler systems shall have a test and flush connection in the far end of the piping system and atthe sprinkler valve(s). The connections shall be easy accessible from deck level and have onedrain box located below the connection.

• Adequate venting facilities with valves shall be provided for wet pipe sprinklers.

Valves• Sprinkler valves shall be provided with full capacity manual by-pass• The arrangement of the isolation valves shall be such that not more than 50% of the fire water to

water hoses and hydrants for one area, is effected if one segment of the fire water ring main istaken out of service.

• All valves (> 1") shall be painted red and provided with a car-sealing system.• Control valves for sprinkler and deluge systems shall be located outside the area they protect.• Deluge control valves shall be automatically activated by the F&G logic.• All deluge valves, monitors and sprinklers shall be fitted with a test line with 100 % capacity.• For manned installations resetting of deluge, monitor and sprinkler control valves shall only be

possible local to the valves.

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• The deluge system shall comply with NFPA 16, Deluge Foam - Water System. • The sprinkler system shall comply with NFPA 13, Sprinkler Systems.

Technical Safety S-001 Rev. 3, Jan. 2000

NORSOK standard Page 29 of 66

Fig. 10.1

Fig 10.1 Firewater system principles.

10.7.2 Prime Mover and FireWater Pumps.Offshore installations shall be provided with two independent prime mover and firewater pumpsystems. Each pump system shall have the capacity to supply 100% of the largest fire water demand.The water application rates to the various areas and equipment shall be as follows:

- Wellhead area 20 l/min m2- Manifolds located on FPSO turrets 20 l/min m2- Area for circulation and treatment of mud 10 l/min m2- Processing area 10 l/min m2- Surface of pressure vessels and tanks containing combustibles 10 l/min m2

Other water application rates shall be according to ISO 13702 Annex H.It is recommended that each pump system consist of 2x50% pump units, unless other solutions areevaluated to present similar or increased safety level. Ref. clause 10.2.The following principles shall be the basis for prime mover and firewater pump system design:

- NFPA 20 shall be followed- Consideration shall be given to two separate modes, normal mode and maintenance mode- In normal mode the minimum capacity for the system is two separate and independentsystems, each with 100% capacity

- Measures to compensate for possible shut downs in the system due to maintenance shall bedefined and documented as a part of the design. Compensating measures in

DEDICATEDFIRE PUMPS

DISTRIBUTIONSYSTEM

AUTOMATICEQUIPMENT

F&G /

CONTROL

SYSTEM

DEDI-CATED

POWER

GENE-RATION

UNITS

DRAIN

MANUALEQUIPMENT

FIRE FIGHTING SYSTEM

OVER BOARDDUMP/TEST LINE

PRESSUREMAINTAINANCE

FOAM /PUMPDISTRIBUTION

SYSTEM

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- Wellhead area 20 l/min m2 - Manifolds located on FPSO turrets 20 l/min m2 - Area for circulation and treatment of mud 10 l/min m2 - Processing area 10 l/min m2 - Surface of pressure vessels and tanks containing combustibles 10 l/min m2

NFPA 15

Standard for Water Spray

Fixed Systems for Fire Protection

2001 Edition

NFPA, 1 Batterymarch Park, PO Box 9101, Quincy, MA 02269-9101 An International Codes and Standards Organization

NFPA License Agreement

This document is copyrighted by the National Fire Protection Association (NFPA), 1 Batterymarch Park, Quincy, MA 02269-9101 USA. All rights reserved.

NFPA grants you a license as follows: The right to download an electronic file of this NFPA document for temporary storage on one computer

for purposes of viewing and/or printing one copy of the NFPA document for individual use. Neither the electronic file nor the hard copy print may be reproduced in any way. In addition, the electronic file may not be distributed elsewhere over computer networks or otherwise. The

hard copy print may only be used personally or distributed to other employees for their internal use within your organization.

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TVNC 2004 Agenda

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Pipenet flow analysis

Oseberg A, Module M03 Main Deck, Run ID: PNET 114File: pnet 114.txt

PIPENET Schematic Page 1 of 1Tuesday, December 09, 2003

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34

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Page 4 PIPENET Spray/Sprinkler Module Technical ManualRev 5.04, December 1999

where: D is the internal diameter of the pipe.L is the pipe length.L

e is the equivalent length of any pipe fittings.

f is the Fanning friction factor.u is the fluid velocity.r is the fluid density.

The Fanning friction factor depends on Reynold�s number (Re=uDr/µ where µ isthe fluid viscosity) and the relative roughness of the pipe (pipe roughness/pipediameter). The standard values for f can be obtained from a graphical represen-tation known as the Moody diagram. This is represented in PIPENET by thefollowing empirical formulae (where r is the surface roughness of the pipe):

Laminar flow (Re < 2000):

f =16/Re

Transitional flow (2000<Re<3000):

f is found by interpolating between laminar value for Re=2000 and turbu-lent value at Re=3000.

Turbulent flow (Re >3000):

1/ Öf = -1.768ln(0.27 r / D + 1.252/Re Öf )

The Hazen-Williams Equation Method

The Hazen-Williams equation is an empirical formula which gives an explicitexpression for the frictional pressure loss:

where: L is the pipe length.L

e is the equivalent length of any pipe fittings.

Q is the (volumetric) fluid flowrate.D is the pipe diameter.C is the Hazen-Williams constant (or C-factor) for the pipe.

87.485.1

85.15 )(1005.6

DC

QLLP e

fric

+×=

Chapter 1 : Modelling Aspects Page 9

1.2 PIPES

Description

Pipes are viewed and edited via the View | Pipes menu option.

Appearance

Chapter 2 : Built-In Data Page 17

Equivalent Lengths (metres) of Fittings for NFPA Rules

NOTES:

1. Equivalent lengths are taken from NFPA 15 (1990), except for fittingtypes 7 and 8 which are manufacturers� data.

2. The above values are used only with a Hazen-Williams C factor of120. For other values of C factor the equivalent lengths are scaled inaccordance with NFPA 15 Table A-7-2 (g).

3. The equivalent length of a 90mm butterfly valve is assumed thesame as the 100mm valve.

4. For NFPA 1996 rules the above values only apply to internal diam-eters identical to the Schedule 40 steel pipe. For other internal diam-eters the equivalent lengths are scaled in accordance with NFPA1996 rules, Table 5.-5.2.1 (Note 2).

edoC epyTgnittiF

eziSepiPlanimoN

mmni

0.050.2

0.565.2

0.080.3

0.095.3

0.0010.4

1°54dradnatS

woblE6906.0 4419.0 4419.0 4419.0 2912.1

2°09dradnatS

woblE425.1 8828.1 6331.2 4834.2 840.3

3 woblEsuidargnoL 4419.0 2912.1 425.1 425.1 8828.1

4wolF(ssorCroeeT

)°09denrut840.3 6756.3 275.4 6181.5 690.6

5 evlaVetaG 8403.0 8403.0 8403.0 8403.0 6906.0

6 evlaVkcehCgniwS 8253.3 2762.4 8678.4 2197.5 6507.6

7 evlaVnruter-noN 3.4 2.5 1.6 9.6 7.7

8 evlaVllaB 47.2 56.2 95.2 0.3 5.3

9 evlaVylfrettuB 8828.1 6331.2 840.3 6756.3 6756.3

Chapter 1 : Modelling Aspects Page 31

1.11 NOZZLES

Description

Nozzles are added to the network via the View | Nozzles menu option. Via thisoption a user can specify the characteristics of an individual nozzle in terms of itsproperties, or select from a list of nozzle types in the library.

Appearance

User Input Parameters

Enter the nozzle label, input node and either the required flowrate or the flow den-sity and the area to be covered by the nozzle in the spaces provided. Default valueof flowrate or flow density and area can be set using the menu option Init | DefaultValues.

The list box on the left hand side lists all the nozzle types which have been de-fined using the Library menu (or read in using the File menu), together with theoption �user defined�. One of the nozzle types in this list must be chosen by click-ing on it.

If a nozzle type from the PDF is chosen then its properties are shown for informa-tion purposes on the right hand side. If the �user defined� nozzle type is chosenthen the user must enter the K factor and minimum and maximum operatingpressures in the spaces provided on the right hand side.

Presentation of Pipenet calculation

Appendix Page 1 of 3

vlookup "TITL" file2, 1,( )

"Oseberg B - CD0 - temporary deluge 02"

"Temporary deluge 12 noszzles"

"Module CD0 (C30)"

"Project nr: 89176"

=

Number of pipes :.....................

Number of nozzles:...................

Pressure at deluge valve [barG].......

Flow at deluge valve [lit/min).........

npipe 190=

nnoz1 134=

press 8.129=

flow 12234=

0 20 40 60 80 100 120 140 160 1802

4

6

8

10Pipe: pressure in and out [barG]

Pipe #

file 4⟨ ⟩( )ipipe

100000


100000

ipipe

file

0 20 40 60 80 100 120 140 160 1800

0.5

1

1.5

2Pipe: Friction Loss [bar/m]

Pipe #


100000

ipipe

12.02.2004 results.mcd



file21 1, "Oseberg B - CD0 - temporary deluge 02"=

0 20 40 60 80 100 120 140 160 1800

5

10

15Pipe: Velocity [m/s]

Pipe #


ipipe

0 20 40 60 80 100 120 140 160 1800

5

10

15Pipe: Flow rate [m^3/min]

Pipe #


60 1−

ipipe




file21 1, "Oseberg B - CD0 - temporary deluge 02"=

0 20 40 60 80 100 1202

4

6

8Nozzle, Pressure In [bar G]

Nozle #

file 3⟨ ⟩( )inoz1

100000

inoz1 npipe−

0 20 40 60 80 100 12040

60

80

100

120Nozzle, Flow rate [lit/min] / Req. flow

Nozle #


60000 1−


60000 1−

inoz1 npipe−

0 20 40 60 80 100 1200

50

100Nozzle, Deviation [%]

Nozle #


inoz1 npipe−


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TVNC 2004 Agenda

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SolidWorks / Routing - Bill of materials

6 7

811

10

12 13 14

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1

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2

4

5

ITEM NO. QTY. PART NO. PART NO. (row:D) DESCRIPTION CUT LENGTH1 1 routeAssy2

2 WNeck Flange 150-NPS4 WNeck Flange 150-NPS41 4 in, Schedule 40, 5 Pipe 4 in, Sch 40 16.56cm1 Tee Inch 4 Sch40 Tee Inch 4 Sch402 90L LR Inch 4 Sch40 90L LR Inch 4 Sch401 4 in, Schedule 40, 6 Pipe 4 in, Sch 40 34.3cm1 4 in, Schedule 40, 7 Pipe 4 in, Sch 40 12.74cm1 4 in, Schedule 40, 8 Pipe 4 in, Sch 40 105cm1 4 in, Schedule 40, 9 Pipe 4 in, Sch 40 7.56cm

2 1 routeAssy32 WNeck Flange 150-NPS4 WNeck Flange 150-NPS43 90L LR Inch 4 Sch40 90L LR Inch 4 Sch401 4 in, Schedule 40 Pipe 4 in, Sch 40 238.46cm1 4 in, Schedule 40, 1 Pipe 4 in, Sch 40 97.92cm1 4 in, Schedule 40, 2 Pipe 4 in, Sch 40 9.52cm1 4 in, Schedule 40, 3 Pipe 4 in, Sch 40 7.56cm


4 1 routeAssy62 WNeck Flange 150-NPS4 WNeck Flange 150-NPS41 90L LR Inch 4 Sch40 90L LR Inch 4 Sch401 4 in, Schedule 40 Pipe 4 in, Sch 40 3910mm1 4 in, Schedule 40, 1 Pipe 4 in, Sch 40 142mm1 4 in, Schedule 40, 2 Pipe 4 in, Sch 40 823mm1 4 in, Schedule 40, 3 Pipe 4 in, Sch 40 76mm1 90deg LR Inch Elbow_Local4 90L LR Inch 4 Sch401 90deg LR Inch Elbow_Local5 90L LR Inch 4 Sch40


6 1 routeAssy82 WNeck Flange 150-NPS4 WNeck Flange 150-NPS41 4 in, Schedule 40 Pipe 4 in, Sch 40 580cm

7 1 routeAssy92 WNeck Flange 150-NPS4 WNeck Flange 150-NPS41 4 in, Schedule 40 Pipe 4 in, Sch 40 580cm

8 1 routeAssy102 WNeck Flange 150-NPS4 WNeck Flange 150-NPS41 90L LR Inch 4 Sch40 90L LR Inch 4 Sch401 90deg LR Inch Elbow_Local1 90L LR Inch 4 Sch401 4 in, Schedule 40 Pipe 4 in, Sch 40 97.36cm1 4 in, Schedule 40, 1 Pipe 4 in, Sch 40 12.87cm1 4 in, Schedule 40, 2 Pipe 4 in, Sch 40 189.91cm

9 1 routeAssy112 WNeck Flange 150-NPS4 WNeck Flange 150-NPS41 90L LR Inch 4 Sch40 90L LR Inch 4 Sch401 90deg LR Inch Elbow_Local2 90L LR Inch 4 Sch401 90deg LR Inch Elbow_Local3 90L LR Inch 4 Sch401 4 in, Schedule 40 Pipe 4 in, Sch 40 7.56cm1 4 in, Schedule 40, 1 Pipe 4 in, Sch 40 313.1cm1 4 in, Schedule 40, 2 Pipe 4 in, Sch 40 37.08cm1 4 in, Schedule 40, 3 Pipe 4 in, Sch 40 9.54cm

10 1 routeAssy122 WNeck Flange 150-NPS4 WNeck Flange 150-NPS42 90L LR Inch 4 Sch40 90L LR Inch 4 Sch401 4 in, Schedule 40 Pipe 4 in, Sch 40 7.56cm1 4 in, Schedule 40, 1 Pipe 4 in, Sch 40 268.32cm1 4 in, Schedule 40, 2 Pipe 4 in, Sch 40 89.66cm

6

D

C

B

A

E

F

G

H

E

A

B

C

D

F

54321 7 8 9 10 11 12

1 2 3 4 5 6 7 8

G

L09842WEIGHT:

A2

SHEET 1 OF 1SCALE:1:250

DWG NO.

TITLE:

REVISIONDO NOT SCALE DRAWING

MATERIAL:

DATESIGNATURENAME

DEBUR AND BREAK SHARP EDGES

FINISH:UNLESS OTHERWISE SPECIFIED:DIMENSIONS ARE IN MILLIMETERSSURFACE FINISH:TOLERANCES: LINEAR: ANGULAR:

Q.A

MFG

APPV'D

CHK'D

DRAWN

Oseberg A, M-03 (Nedre Del!) Side 1 av 2 12.02.2004

Item Type Navn Prefab Dyse Dyseforlenger(Titan) 100mm

Item 001 T-stykke 1" x 3/4"NPT x 3/4"NPT m/plugg Prefab DN 20 HV NozzleItem 002 T-stykke 1 1/2" x 3/4"NPT x 1" Prefab DN 20 HV NozzleItem 003 T-stykke 1 1/2" x 3/4"NPT x 1 1/2" Ikke Prefab DN 20 HV NozzleItem 004 T-stykke 1 1/2" x 1 1/2" x 1 1/2" Ikke PrefabItem 005 T-stykke 1 1/2" x 1 1/2" x 5/4" m/plugg Ikke PrefabItem 006 T-stykke 1 1/2" x 3/4"NPT x 1" Prefab DN 20 HV NozzleItem 007 T-stykke 1" x 3/4"NPT x 3/4"NPT m/plugg Prefab DN 20 HV NozzleItem 008 T-stykke 1" x 3/4"NPT x 3/4"NPT m/plugg Ikke Prefab DN 20 HV NozzleItem 009 T-stykke 1 1/2" x 3/4"NPT x 1" Ikke Prefab DN 20 HV Nozzle 1550Item 010 T-stykke 1 1/2" x 3/4"NPT x 1 1/2" Ikke Prefab DN 20 HV Nozzle 1265Item 011 Kryss 2" x 1 1/2" x 2 x 1 1/2" Ikke PrefabItem 012 Endeavslutning 1" x 3/4NPT

Item 013 T-stykke 1 1/2" x 3/4"NPT x 1" Prefab DN 20 HV NozzleItem 014 T-stykke 1" x 3/4"NPT x 3/4"NPT m/plugg Prefab DN 20 HV NozzleItem 015 T-stykke 1" x 3/4"NPT x 3/4"NPT m/plugg Ikke Prefab DN 20 HV NozzleItem 016 T-stykke 1 1/2" x 3/4"NPT x 1" Ikke Prefab DN 20 HV Nozzle 1157 2Item 017 T-stykke 1 1/2" x 3/4"NPT x 1 1/2" Ikke Prefab DN 20 HV Nozzle 1157 1Item 018 Kryss 3" x 1 1/2" x 2 x 1 1/2" Ikke PrefabItem 019 Endeavslutning 1" x 3/4"NPTItem 020 T-stykke 1 1/2" x 3/4"NPT x 1" Prefab DN 20 HV NozzleItem 021 T-stykke 1" x 3/4"NPT x 3/4"NPT m/plugg Prefab DN 20 HV NozzleItem 022 T-stykke 1" x 3/4"NPT x 3/4"NPT m/plugg Ikke Prefab DN 20 HV NozzleItem 023 T-stykke 1 1/2" x 3/4"NPT x 1" Ikke Prefab DN 20 HV Nozzle 1157 1Item 024 T-stykke 1 1/2" x 3/4"NPT x 1 1/2" Ikke Prefab DN 20 HV Nozzle 1157 1Item 025 Kryss 3" x 1 1/2" x 3 x 1 1/2" Ikke PrefabItem 026 Endeavslutning 1" x 3/4"NPTItem 027 T-stykke 1 1/2" x 3/4"NPT x 1" Prefab DN 20 HV NozzleItem 028 T-stykke 1" x 3/4"NPT x 3/4"NPT m/plugg Prefab DN 20 HV NozzleItem 029 T-stykke 1" x 3/4"NPT x 3/4"NPT m/plugg Ikke Prefab DN 20 HV NozzleItem 030 T-stykke 1 1/2" x 3/4"NPT x 1 1/2" Ikke Prefab DN 20 HV Nozzle 1157 1Item 031 Kryss 3" x 1 1/2" x 3 x 1 1/2" Ikke PrefabItem 032 Endeavslutning 1" x 3/4"NPTItem 033 T-stykke 1 1/2" x 3/4"NPT x 1 1/2" Ikke Prefab DN 20 HV Nozzle 1157 1Item 034 T-stykke 1 1/2" x 3/4"NPT x 1" Prefab DN 20 HV Nozzle

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TVNC 2004 Agenda

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Support for Elastopipe – Design report

Trelleborg Viking AS Page: 1 of 15 Rev. C

TRELLEBORG VIKING AS, 3052 Mjøndalen Doc. Nr.: 89106-085 Support for Elastopipe rev C.doc

ENGINEERED SYSTEMS Title:

SUPPORT FOR ELASTOPIPE

Project

ELASTOPIPE SUPPORT DEVELOPMENT

Client: Internal Address:

Contact person: Ole Bjørn Rasmussen

Contract no.:

Document no.: 89106-085

Classification: Open

Page 1 of 15

Doc. responsible: Gunnar Jul Sand

Summary:

This report document the calculation and design of a general support for Elastopipe Rev. C incorporate the use of double UNO-profile for 1", 1 1/2", 2", 3" and 4" Elastopipe

C Reissued for construction 06.02.03 GJS sign

TJ sign

OBR sign

B Issued for construction 07.01.03 GJS TJ OBR

A Issued for DC 28.08.02 GJS TJ OBR

Rev. Reason for issue Date Prepared Controlled Approved Released

Von Mises

thin-support-02-case 10 :: Static Nodal StressUnits : N/mm^2 (MPa)

Trelleborg Viking AS Page: 13 of 15 Rev. C

TRELLEBORG VIKING AS, 3052 Mjøndalen Doc. Nr.: 89106-085 Support for Elastopipe rev C.doc

6.2 St 37

Based on use of St 37 the following max span length table apply: (blast = 0.25 bar) Max span for UNO-profile - St 37 [mm]

Pipe dimension UNO profile Fixed-fixed Hinged-Fixed Hinged-Hinged Fixed-Free

(cantilever)

1" U-41-1-P 7400 4300 2400 600 1,5" U-41-1-P 6300 3700 2100 500 2" U-41-1-P 5800 3400 1900 400 3" U-41-1-P 4800 2800 1600 400 4" U-41-1-P 4100 2400 1300 300 1" U-41-2-P 9500 5600 3100 700

1,5" U-41-2-P 8600 5100 2800 700 2" U-41-2-P 8000 4700 2600 600 3" U-41-2-P 6900 4100 2300 500 4" U-41-2-P 6100 3600 2000 500 5" U-41-2-P 5500 3200 1800 400 6" U-41-2-P 4800 2800 1600 400 8" U-41-2-P 4100 2400 1300 300

Table 9 Max span for single UNO-profile - St 37

Example: A 2" Elastopipe clamped to a single UNO-profile in SS can in this situation be max 3100 mm. If used a St37 for same purpose max l = 3400 mm

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TVNC 2004 Agenda

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Function test – full scale



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TRELLEBORG VIKING AS, Kallosjegata 15, N-3055 Krokstadelva Doc. No.: 89163-001 Function Test Certificate - Ekofisk 2 4 C rev A

ENGINEERED SYSTEMS Title:

FUNCTION TEST CERTIFICATE

Project: 89163 Ekofisk 2/4 C Lower Wellhead

Document no.: 89163-001 Function Test Certificate – Ekofisk 2 4 C

Page 1 of 3

Comments: Full scale test performed on 2/4 C Lower Wellhead 14. November 2003 Results: Calculated Test

Total flow, liter/min 3188 3237 => 1,5% deviation. OK

Most remote nozzle, barg 3,129 3,12 OK

Pressure downstream skid barg 5.67 5,73 => 1,06% deviation OK

A Issued for information 28.11.03 GJS

Rev. Reason for issue Date Prepared

Controlled

Approved

Released

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Calculated Test Total flow, liter/min 3188 3237 => 1,5% deviation. OK Most remote nozzle, barg 3,129 3,12 OK Pressure downstream skid barg 5.67 5,73 => 1,06% deviation OK

Documents

Engineering Tv Nc 2004