P-sr-007r1.pdf

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NORSOK STANDARD

SYSTEM REQUIREMENTS

FLARE, VENT AND BLOWDOWN SYSTEM NO. 43

P-SR-007 Rev. 1, December 1994

Flare, Vent and Blowdown

P-SR-007 Rev. 1, December 1994

CONTENTS 1. FOREWORD 2. SCOPE 3. NORMATIVE REFERENCES 4. DEFINITIONS AND ABBREVIATIONS 4.1 Definitions 4.2 Abbreviations 5. FUNCTIONAL REQUIREMENTS 5.1 General 5.2 Products/Services 5.3 Equipment/Schematic 5.4 Performance 5.5 Regularity 5.6 Process/Ambient Conditions 5.7 Operational Requirements 5.8 Maintenance Requirements 5.9 Isolation and Sectioning 5.10 Layout Requirements 5.11 Interface Requirements 5.12 Commissioning Requirements

NORSOK Standard

2 2 2 2 2 2 2 2 2 3 3 3 4 4 4 5 5 5 6

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Flare, Vent and Blowdown

1.

P-SR-007 Rev. 1, December 1994

FOREWORD This standard has been developed by the NORSOK Standardisation Work Group.

2.

SCOPE

3.

NORMATIVE REFERENCES NORSOK Standard P-CR-001 S-DP-001

Process Design Technical Safety.

4.

DEFINITIONS AND ABBREVIATIONS

4.1

Definitions

4.2

Abbreviations

5.

FUNCTIONAL REQUIREMENTS

5.1

General Discharge and disposal of gases and liquids during emergency depressurization, process upsets, system and equipment failure, depressurization for maintenance and operation and purging of tanks and vessels.

5.2

Products/Services Not Applicable.

NORSOK Standard

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Flare, Vent and Blowdown

5.3

P-SR-007 Rev. 1, December 1994

Equipment/Schematic

Flare tips

HP-flare HP-flare K.O. drum LP-flare LP-flare K.O. drum Vent Vent K.O. drum

5.4

Performance HP System Capacity Source discharge pressure (barg) Knock-out drum pressure (barg) Knock-out droplet size (micron) *)

5.5

LP

: : : :

Vent ATM

<400 *)

<300

ATM <300

For subsonic flare, 300 micron shall be used.

Regularity

5.5.1 Regularity 99 %. 5.5.2 Sparing HP, LP and Vent, as required. No Sparing.

NORSOK Standard

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5.6

P-SR-007 Rev. 1, December 1994

Process/Ambient Conditions Not Applicable.

5.7

Operational Requirements

5.7.1 Control and Monitoring System performance shall be controlled and monitored from CCR as shown below: OS/VDU Functions

P

T

L

Knock-out Vessel

M

M1)

C1)

Flare Meter Flare Tip Pilots

F

A X1)

X

Other 1)

Low temperature and liquid level DAS

X2)

Pilots extinguished

P = Pressure, T = Temperature, L = Level, F = Flow, A = Alarm, M = Monitoring, C = Control, X=Alarm available as required 5.7.2 Measurements Systems shall be equipped with flow devices located downstream knock-out drums continuously measuring the rates of fluids being flared. The rates shall be available on above OS VDU picture and as input to Data Acquisition System (DAS). 5.7.3 Pilot Ignition Generators Functionality shall be proven under all operating conditions. 5.8

Maintenance Requirements

5.8.1 Access All instrumentation shall be located and available for testing, repair and replacement without production shutdown, except instrumentation at flare tip. Ladders and platform for access to flare tips shall be provided.

NORSOK Standard

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Flare, Vent and Blowdown

5.9

P-SR-007 Rev. 1, December 1994

Isolation and Sectioning

5.9.1 Valves Block valves shall be installed downstream blowdown valves and upstream and downstream safety relief valves. 5.10

Layout Requirements

5.10.1 Piping To slope towards knock-out drums and no pocket allowed. 5.10.2 Insulation Not required on knock-out vessel 5.11

Interface Requirements

5.11.1 Power Vessels shall be fitted with heaters to prevent liquids from freezing. 5.11.2 Nitrogen Each system shall be continuously purged with nitrogen supplied upstream in headers and sub-headers. 5.11.3 Pilots Each flare tip shall be equipped with pilot burners. Alternative backup source provided. Provision shall be made for use of propane bottles. 5.11.4 Methanol Shall be considered to prevent blockage by hydrates.

NORSOK Standard

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5.12

P-SR-007 Rev. 1, December 1994

Commissioning Requirements Spectacle blinds shall be provided as required to perform leak testing of system, excluding flare stack piping from knock-out drum outlets.

NORSOK Standard

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