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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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