Design and Safety Considerations for existing LNG Peak ... · PDF fileDesign and Safety...
Transcript of Design and Safety Considerations for existing LNG Peak ... · PDF fileDesign and Safety...
Grossmann/Gastech2005 Revamping LNG Peak Shaving Plant 1
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)