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Design and Safety Considerations for<br />

existing LNG Peak Shaving Plants<br />

Hans – Joachim Grossmann<br />

<strong>GOC</strong> <strong>Engineering</strong> GmbH<br />

Gastech 2005<br />

March 13-17, Bilbao Spain<br />

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Design and Safety Considerations for existing<br />

LNG Peak Shaving Plants<br />

-A Project Example-<br />

The plant<br />

Brief plant<br />

description<br />

Project phases<br />

Pre-Studies<br />

Conformity study<br />

Costing study<br />

The project<br />

Design aspects<br />

Project execution<br />

Project status<br />

Project organization<br />

Summary/conclusions<br />

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The Plant<br />

LNG Peak Shaving Plant<br />

Located at Dormagen<br />

Nievenheim, Germany<br />

Part of ~ 4,000 km HP<br />

Gas Pipeline Grid of<br />

RWE Energy<br />

Mainly cavern storage<br />

Start up in 1976<br />

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Built by CBI Germany<br />

Only two cryogenic LNG<br />

installations in Germany


Brief Plant Description<br />

Gas Treatment and<br />

Liquefaction<br />

Gas treatment with two<br />

adsorber systems<br />

To remove moisture,<br />

aromatics, CO2<br />

Liquefaction with MRL<br />

cycle<br />

MRL Methane/Propane<br />

Liquefaction capacity<br />

2,400 Nm³/h<br />

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Brief Plant Description<br />

LNG Storage<br />

Double wall steel<br />

tank (API 620 Q)<br />

Inner tank 9% nickel<br />

suspended deck<br />

Outer tank CS<br />

Bottom/shell<br />

penetrations<br />

Geo. V. 22,700 m³<br />

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Brief Plant Description<br />

BOG Handling<br />

(exist.)<br />

Partly re-circulated back<br />

to tank<br />

Partly send to pipeline<br />

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Brief Plant Description<br />

NG Send Out System<br />

Two HP Pumps , outside<br />

tanks, 2 x 80m³/h LNG<br />

Two submerged<br />

combustion vaporizers<br />

Send out rate: 2 x 50,000<br />

Nm³/h<br />

Conditioning with LN2<br />

Truck loading system<br />

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Plant Views Submerged C. Vaporizer<br />

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Plant Views Reg. Gas/MRL Compressor<br />

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Pre- Studies<br />

I. First Study to check the<br />

Compliance of the plant with actual rules &<br />

regulations<br />

E.g. EN 1473/NFPA 59A<br />

Safety Study to review actual installed safety features<br />

Active & passive safety equipment<br />

II. Target<br />

Life Extension of the plant<br />

Increased level of automation<br />

Alternative peak shaving concepts<br />

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Plant Views<br />

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Pre- Studies<br />

III. Results<br />

EN 1473 allows no penetrations of the primary and<br />

secondary container walls ( >> submerged tank<br />

pumps)<br />

NFPA 59A allows penetrations, however the design<br />

spill shall be defined as the full liquids content of<br />

the tank ( >> with submerged pumps the design<br />

spill reduced to 10min. Nom. Pump capacity)<br />

Entire revamping needed instrumentation &<br />

control system<br />

Partly revamping needed for mechanical equipment<br />

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Pre- Studies<br />

IV. Costing study<br />

Costing of various alternatives<br />

Revamping of plant + submerged pumps<br />

Revamping of plant with additional safety<br />

features ( water curtains, foam systems,<br />

thermal insulation of impoundment area )<br />

Other alternatives such as close down<br />

of plant<br />

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The Project Overview<br />

Client decided to take out the plant for one<br />

winter season to:<br />

Empty and warm up the LNG tank<br />

Install submerged pumps<br />

Install new instrumentation &control system<br />

Revamp partly mechanical equipment/ piping,<br />

control building etc.<br />

Install new BOG handling system ( was added to<br />

the project 2Q/2004)<br />

Project duration 1Q/04 – 4Q/05<br />

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Design Aspects Process<br />

Process simulation<br />

Change in gas composition<br />

Optimization due to input from operators<br />

E.g. gas treatment &liquefaction process<br />

Level of automation<br />

New BOG System<br />

Safety<br />

Hazop Study<br />

SIL Allocation<br />

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Design Aspects LNG Tank<br />

Tank Decommissioning<br />

Data assessment after 30 years operation<br />

Static calculations of existing tank<br />

Install new pumps/pump platform<br />

Recalculated the tank due to change in rules &<br />

regulations<br />

Install additional outer shell stiffeners<br />

Local authorities/ Environmental<br />

Change in Rules & Regulations<br />

Safety Report<br />

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Design Aspects Tank Design<br />

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Design Aspects Tank Design<br />

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Design Aspects FE Calculations<br />

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Project Execution<br />

Decommissioning of tank starts at approx.<br />

2,5 m liquid level ( April 2004)<br />

Temporary connection between RT Loading<br />

pumps and HP send out pumps<br />

Result : Tank more or less 100 % liquid<br />

emptied<br />

Warming up<br />

Purging with nitrogen<br />

Purging with air<br />

Opening the tank<br />

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Project Execution Temp. Send Out System<br />

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Project Execution Tank Opening – Suspend. Deck<br />

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Project Execution Tank Views<br />

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Project Execution Tank Views<br />

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Project Execution Plant Views<br />

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Project Execution New Pump Platform<br />

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Project Execution -Laser Scanning (Test Project)<br />

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Project Execution -Laser Scanning (Test Project)<br />

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Project Execution -Laser Scanning (Test Project)<br />

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Project Execution -Laser Scanning (Test Project)<br />

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Project Execution -Laser Scanning (Test Project)<br />

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Project Organisation<br />

Entire project execution with<br />

one <strong>Engineering</strong> company including:<br />

pre studies<br />

basic, detailed engineering<br />

procurement assistance<br />

supervision and start up<br />

Direct procurement of equipment<br />

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Summary /Conclusions<br />

Detailed Pre Studies required<br />

Close cooperation between Client/<br />

<strong>Engineering</strong> company<br />

Detailed planning of activities<br />

Tailor made solutions required<br />

No critical findings after 30 years of use<br />

Findings/results can be used for other<br />

projects too ( LNG/LEG)<br />

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Summary /Conclusions<br />

We hope that we can report during the next GASTECH<br />

venue the next important step in the project<br />

The restart of the LNG Peak Shaving Plant<br />

Thank you for your attention !<br />

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

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