Design and Safety Considerations for existing LNG Peak ... · PDF fileDesign and Safety...

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Grossmann/Gastech2005 Revamping LNG Peak Shaving Plant 1 Design and Safety Considerations for existing LNG Peak Shaving Plants Hans Joachim Grossmann GOC Engineering GmbH Gastech 2005 March 13-17, Bilbao Spain

Transcript of Design and Safety Considerations for existing LNG Peak ... · PDF fileDesign and Safety...

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Design and Safety Considerations for existing LNG Peak Shaving Plants

Hans – Joachim GrossmannGOC Engineering GmbH

Gastech 2005 March 13-17, Bilbao Spain

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Design and Safety Considerations for existing LNG Peak Shaving Plants

-A Project Example-

The plantBrief plant

descriptionProject phasesPre-StudiesConformity studyCosting study

The projectDesign aspectsProject executionProject statusProject organizationSummary/conclusions

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The Plant

LNG Peak Shaving Plant Located at Dormagen

Nievenheim, Germany Part of ~ 4,000 km HP

Gas Pipeline Grid of RWE Energy

Mainly cavern storage

Start up in 1976 Built by CBI Germany Only two cryogenic LNG

installations in Germany

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Brief Plant Description

Gas Treatment and Liquefaction

Gas treatment with two adsorber systems

To remove moisture, aromatics, CO2

Liquefaction with MRL cycle

MRL Methane/Propane Liquefaction capacity

2,400 Nm³/h

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Brief Plant Description

LNG Storage

Double wall steel tank (API 620 Q)

Inner tank 9% nickel suspended deck

Outer tank CSBottom/shell

penetrationsGeo. V. 22,700 m³

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Brief Plant Description

BOG Handling (exist.)

Partly re-circulated back to tank

Partly send to pipeline

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Brief Plant Description

NG Send Out System Two HP Pumps , outside

tanks, 2 x 80m³/h LNG Two submerged

combustion vaporizers Send out rate: 2 x 50,000

Nm³/h Conditioning with LN2 Truck loading system

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Plant Views Submerged C. Vaporizer

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Plant Views Reg. Gas/MRL Compressor

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Pre- Studies

I. First Study to check the Compliance of the plant with actual rules &

regulations E.g. EN 1473/NFPA 59A Safety Study to review actual installed safety features Active & passive safety equipmentII. Target Life Extension of the plant Increased level of automation Alternative peak shaving concepts

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Plant Views

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Pre- Studies

III. Results EN 1473 allows no penetrations of the primary and

secondary container walls ( >> submerged tank pumps)

NFPA 59A allows penetrations, however the design spill shall be defined as the full liquids content of the tank ( >> with submerged pumps the design spill reduced to 10min. Nom. Pump capacity)

Entire revamping needed instrumentation & control system

Partly revamping needed for mechanical equipment

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Pre- Studies

IV. Costing study Costing of various alternatives Revamping of plant + submerged pumps Revamping of plant with additional safety

features ( water curtains, foam systems, thermal insulation of impoundment area )

Other alternatives such as close down of plant

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The Project Overview

Client decided to take out the plant for one winter season to:

Empty and warm up the LNG tank Install submerged pumps Install new instrumentation &control system Revamp partly mechanical equipment/ piping,

control building etc. Install new BOG handling system ( was added to

the project 2Q/2004) Project duration 1Q/04 – 4Q/05

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Design Aspects Process

Process simulation Change in gas composition Optimization due to input from operators E.g. gas treatment &liquefaction process Level of automation New BOG System

Safety Hazop Study SIL Allocation

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Design Aspects LNG Tank

Tank Decommissioning Data assessment after 30 years operation

Static calculations of existing tank Install new pumps/pump platform Recalculated the tank due to change in rules &

regulations Install additional outer shell stiffeners

Local authorities/ Environmental Change in Rules & Regulations Safety Report

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Design Aspects Tank Design

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Design Aspects Tank Design

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Design Aspects FE Calculations

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Project Execution

Decommissioning of tank starts at approx. 2,5 m liquid level ( April 2004)

Temporary connection between RT Loading pumps and HP send out pumps

Result : Tank more or less 100 % liquid emptied

Warming up Purging with nitrogen Purging with air Opening the tank

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Project Execution Temp. Send Out System

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Project Execution Tank Opening – Suspend. Deck

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Project Execution Tank Views

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Project Execution Tank Views

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Project Execution Plant Views

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Project Execution New Pump Platform

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Project Execution -Laser Scanning (Test Project)

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Project Execution -Laser Scanning (Test Project)

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Project Execution -Laser Scanning (Test Project)

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Project Execution -Laser Scanning (Test Project)

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Project Execution -Laser Scanning (Test Project)

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Project Organisation

Entire project execution with one Engineering company including:

pre studies basic, detailed engineering procurement assistance supervision and start up

Direct procurement of equipment

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Summary /Conclusions

Detailed Pre Studies required Close cooperation between Client/

Engineering company Detailed planning of activities Tailor made solutions required No critical findings after 30 years of use Findings/results can be used for other

projects too ( LNG/LEG)

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Summary /Conclusions

We hope that we can report during the next GASTECH venue the next important step in the project

The restart of the LNG Peak Shaving Plant

Thank you for your attention !

(* Pictures/Diagrams page 3-7 , source: RWE)