SOFREGAZ’s experience

Slides:



Advertisements
Similar presentations
SOFREGAZ COMPANY PROFILE
Advertisements

Petroleum Equipment Institute
LNG in-ground tank March 6 th, 2006 Kajima Corporation.
LAr1-ND Conceptual Design Review of Status June 25 Craig Thorn.
Gas Transmission Pipelines
1 Status of Hydrogen System Development MICE Collaboration Meeting, Frascati, June 26-29, 2005 Yury Ivanyushenkov, Tom Bradshaw, Elwyn Baynham, Mike Courthold,
LNG Hazards.
VARIOUS PROCESSES FOR REGASIFICATION
LNG Technology.
Objective : To understand the fabrication, design, installation welding, inspection and testing for new construction in oil and gas industry After followed.
Current status Arkadiy Klebaner November 21, 2012
Status of LBNE LAr and LAr1 at FNAL Bruce Baller - Fermilab.
04/10/2007CARTIGNY PRADURAT TEDELID1 Engineering school, Nancy, FRANCE 5 th and last year 1 year as ERASMUS students Project about Transportation of natural.
Cryogenic cavern in Asian site Conceptual design of the cryogenic system Layout of the cryogenic plant for site A & B New layout of the cryogenic system.
Global Design Effort - CFS for Asian Single Tunnel Configuration Design Progress Masanobu Miyahara KEK.
LBNE Reconfiguration Workshop – April 2012 FD Assumptions and Cost Estimate 1 Bruce Baller.
Logo L u c k y P e n n y The presentation will begin shortly…
23 rd World Gas Conference 5 – 9 June 2006 Amsterdam Full Scale Qualification Trials and Certification of the AMPLITUDE-LNG LOADING SYSTEM Phillip COX.
ICARUS Cold Vessels Thermal insulation Project progress report.
4/5/2005FLARE Cryogenics, RLSchmitt1 Argon Refrigeration Supply Purity.
Conceptual Design Study - Cryogenic Requirements How to decide the layout of ILC cryogenic system Conceptual design of cryogenic system Layout of cryogenic.
24 January 2014 LARP VTF Follow-up Meeting P. Kovach VTF 1 LARP Vertical Test Facility Vertical Dewar Design, Magnet Prep And Installation Paul Kovach.
Hydrogen system R&D. R&D programme – general points Hydrogen absorber system incorporates 2 novel aspects Hydrogen storage using a hydride bed Hydrogen.
The Application of Thermo-physical Properties of Foods. Air Products PLC.
HW Review 1.35 A tank of gas with a total pressure of 12.0 atm contains a mixture of oxygen, nitrogen and argon. If the partial pressure of nitrogen.
New compressor station Second stage of nitrogen system (N2 refrigerator, cryogenic tank, pipe lines) Cryogenic equipment required to run NICA Third stage.
LAr1 Plans at FNAL Bruce Baller - Fermilab. Outline LAGUNA Meeting - Mar  LBNE LAr detector overview  Prototyping plan  1 kton prototype.
Experience from large helium inventory management at CERN ILC Cryogenics and Helium inventory meeting CERN, Wed. 18 th of June 2014 D. Delikaris Technology.
Johan Bremer, 22th-26th September 2008 Cryogenics Operations 2008, CERN, Geneva, Switzerland 1 CRYOGENICS OPERATIONS 2008 Organized by CERN Safety aspects.
Iouri Ivaniouchenkov RAL Specifying the needs for MICE July 8, RAL MICE Collaboration Meeting 1.
For more information, please contact 14/12/2010 EN/CV/DC Technical specification IT-3684 by Elena Perez Rodriguez.
Installation of the T600 at Fermilab CSN2, September 22,
Cryogenics Fabrication Plans & Constraints David Montanari (on behalf of the CERN Neutrino Cryogenic Group) ProtoDUNEs Meeting Feb 23, 2016.
Long-Baseline Neutrino Facility LBNF Cryostats Systems Requirements on FSCF Marzio Nessi LBNF/DUNE DOE/SC CD-3a Director’s Review October 27-29, 2015.
SOFREGAZ LAGUNA-LBNO PROJECT LIQUID ARGON PRE-MEETING PROCESS FACILITIES (FILLING FACILITIES, BOG HANDLING, FILTRATION UNIT) Geneva – CERN – 22 nd February.
35ton and LAPD cryostats and future DUNE detector development.
Recondensation of excess boil-off gas by liquid nitrogen produced using LNG cold in a regasification terminal Prof. Kanchan Chowdhury Rohit Singla Jubil.
About company Kurgankhimmash is the leading Russian company manufacturing process equipment for oil & gas producing, oil & gas refining, chemical, energy,
SECONDARY BEAM HANDLING AND INFRASTRUCTURE DESIGN STATUS BRUNO FERAL (CERN/EN) DIAMANTO SMARGIANAKI (CERN/EN) Project Leader: I.Efthymiopoulos (Cern/EN)
SOFREGAZ LAGUNA-LBNO General Meeting PARIS March 2012 LIQUID ARGON HANDLING Jérôme Sialelli / Didier Fernique.
Cryogenic Energy Storage
Liquid natural gas LNG. Outline What is LNG? Well to customers.
Task # 3 Task # kW Target Station Layout proposal Presented by L.Bruno CERN AB Experimental Areas, Targets and Secondary Beams Group.
SOFREGAZ LAGUNA-LBNO GENERAL MEETING HANASAARI - 25 th /27 th August 2014 LIQUID ARGON HANDLING Jérôme Sialelli.
1 Cary Kendziora Fermi National Laboratory Cary Kendziora Fermi National Laboratory CEC-ICMC 2013 Anchorage Alaska – June, 2012.
Installation of the T600 at Fermilab Fermilab, February 15,
Neutrino Platform Proximity Cryogenics Functional Design M.Chalifour 14/04/2016 M. Chalifour - TE/CRG-CI 2.
ProtoDUNE Single Phase (NP-04) P&ID David Montanari (on behalf of Mark A, Johan B, Michel C, Joaquim C, Kevin H) CERN Neutrino Platform General Meeting.
European cryogenic days Membrane cryostats for large volume neutrino detectors June 9 th, GENEVA.
Sorbent Handling Plant by NHI-Design & Equipment Specifications
Gas Turbine Power Plant
Update on the PSB Cooling and Ventilation Systems
Installation of the T600 at Fermilab
Overview of the Long-Baseline Neutrino Facility Cryogenic System
LNG Transportation and Storage
IT-4189 Supply and installation of a cryogenic distribution system
SABRE PoP Fluid Handling
Proximity Cryogenics P&IDs meeting
Flow Equalization Jae K. (Jim) Park Dept. of Civil and Environmental Engineering University of Wisconsin-Madison.
Status of Cryogenics Facilities Design
EHN1 Neutrino Installation Plans
FlexfloTM Surge Relievers
Pinole-Hercules Water Pollution Control Plant Upgrade Project
Experimental study of helium liquefier
Overarching Commissioning Plan
Operator Training Requirements
Liquid Drainers for the Upstream, Mid-Stream, Down-Stream HPI
Module 4: Storage and Dispensing Locations
Chart Ferox, a.s. Děčín LNG Terminal Hamburg.
Gas Transmission Pipelines
Presentation transcript:

SOFREGAZ’s experience GLA2011 WORSHOP SOFREGAZ’s experience in tank building and process  JYVÄSKYLÄ – June 7th 2011 Jérôme Sialelli

FEW WORDS ABOUT SOFREGAZ

ACTIVITIES AND SERVICES LNG RECEIVING TERMINAL BILBAO SPAIN Engineering company specialized in natural gas. ■ Feasibility studies ■ Basic & Detailed Engineering ■ Project Management Consulting ■ Procurement / sourcing ■ Construction Supervision ■ Commissioning & start-up

ALL THROUGH THE “NATURAL GAS CHAIN” LNG RECEIVING TERMINAL HAZIRA INDIA Gas treatment (Gas gathering system, Gas Oil Separation Plant, Sweetening, Drying, Extraction, separation and storage of C2+, …) LNG Peak shaving Small Scale Natural Gas Liquefaction LNG import terminals Transmission systems – Pipelines and pumping and compression stations GAS TREATMENT WAFA LIBYA COMPRESSION STATION S3-S6 IRAN

LNG CHAIN

EXPERIENCE IN LARGE LNG STORAGE In the last 10 years SOFREGAZ has successfully completed as Joint Venture member 8 EPC contracts including 11 LNG tanks with a cumulated capacity of 1,450,000 m3. PROJECT Storage Qty Unit Vol (m3) Total Vol (m 3) Year of completion SHANGHAI Peak Shaving (China) 1 (Full cont. above ground) 20,000 2000 BILBAO Rec. Ter. (Spain) 2 (Full cont. above ground) 150,000 300,000 2004 HAZIRA Rec. Ter. (india) 160,000 320,000 2005 GUANGDONG Rec. Ter.(China) 3 480,000 2006/2007 FOS CAVAOU Rec. Ter. (France) 110,000 330,000 2009

OVERVIEW ON PROVEN TECHNOLOGIES ON LARGE CAPACITY CRYOGENIC STORAGE (> 60,000 m3)

LNG TANK TYPE

TYPICAL LNG FULL CONTAINMENT TANK

LNG STORAGE: IN GROUND TECHNOLOGY

LNG STORAGE: MEMBRANE TECHNOLOGY Stainless Steel corrugated membrane Plywood Reinforced polyurethane foam Secondary barrier Reinforced polyurethane foam Plywood Typical GTS membrane (GTT license) Mastic Pre-stressed concrete wall

LNG TANK TYPE : REFERENCES & TRENDS

LNG STORAGE: DIRECT LNG STORAGE IN MINED CAVERN Technology developed by GEOSTOCK - SAIPEM Pilot Plant in Pyongtaek in South Korea tested with liquid N2 No industrial plant

LIQUID ARGON STORAGE FOR LAGUNA PROJECT PRELIMINARY SCHEME OF LARGE BELOW GROUND LIQUID ARGON STORAGE FOR LAGUNA PROJECT

LAGUNA PROJECT SPECIFIC ASPECTS OF A LARGE LIQUID ARGON STORAGE (100 kt) STORED PRODUCT: ARGON compared to LNG INTERNAL WALL SURFACE TREATMENT CONSTRUCTION IN A CONFINED IN AN UNDERGROUND CAVITY DRYING, FIRST COOLING AND FILLING OPERATION BOIL OFF GAS HANDLING PURIFICATION & FILTRATION INSTALLATION & MAINTENANCE OF INTERNAL INSTRUMENTATION ARGON LNG Boiling point at 1 atm (°C) minus 186 Around minus 160 Liquid density (kg/m3) 1,400 Around 450 Product purity High purity < 1 ppb Mixture of N2 (<3% vol), C1 (>90% vol), C2+, CO2 (< 50 ppm) Operation One single filling Cycle of filling and emptying Safety Inert gas Flamable

PRELIMINARY BLOCK DIAGRAM ABOVE GROUND FIRST FILLING FACILITIES EMERGENCY EMPTYING LIQUID ARGON Ground BOG RELIQUEFACTION BELOW GROUND LIQUID ARGON STORAGE PURIFICATION UNIT

ABOVE GROUND FILLING FACILITIES Liquid Argon Purification Unit Purified Liquid Argon (PLA)vacuum insulated buffer storage Raw Liquid Argon (RLA) vacuum insulated buffer storage (contaminants content: 5 to 10 ppm mainly oxygen) Truck unloading station 30 m3/h On spec liquid argon to the mine Based on 6 months filling period 20 trucks/day 1 week storage: 3,000 m3 1,000 m3

TRANSFER LINE FROM GROUND TO BOTTOM Pipe in Pipe Technology: Invar pipes PiP PiPiP Vertical shaft Main issue: Vertical hanging

METALLIC (Stainless Steel) SELF SUPPORTING PRE-STRESSED CONCRETE LNG STORAGE IN THE CASE OF FULL CONTAINMENT LIQUID ARGON TANK: CHOICE OF OUTER TANK DESIGN: CHOICE OF MAIN CONTAINMENT TYPE: METTALIC SELF SUPPORTING (Conventional) MEMBRANES METALLIC (Stainless Steel) SELF SUPPORTING PRE-STRESSED CONCRETE Concept not used for LNG for large storage. Common concept for large LNG storage Limitation is size of plates (length) From where concrete will be coming; Inside => location of batching plant Outside => How to transport More flexible for stop & go problems Need to be more continuous (jumping or sliding forms) Vertical shaft

ARGON BOIL-OFF GAS RELIQUEFACTION & PURIFICATION: SCHEME 1 Argon BOG compressor LIQUID ARGON STORAGE NITROGEN CLOSED LOOP LIQUID ARGON ULTRA PURIFICATION Cooler (Air ?) Nitrogen compressor

ARGON BOIL-OFF GAS RELIQUEFACTION & PURIFICATION: SCHEME 2 Argon BOG compressor Cooler (Air ?) LIQUID ARGON STORAGE ARGON OPEN LOOP LIQUID ARGON ULTRA PURIFICATION

LARGE LIQUID ARGON STORAGE: Auxiliaries Buffer Storage Buffer Storage Truck unloading facilities Primary Filtration facilities Impounding basin PiP¨ High purity Filtration BOG re-liquefaction In-tank pump HP pump

MAIN CONSTRAINSTS COMPARED WITH A CONVENTIONAL ABOVE GROUND TANK CONSTRUCTION MAIN CONSTRAINSTS COMPARED WITH A CONVENTIONAL ABOVE GROUND TANK LIMITATION MAXIMUM ACCESS SIZE & WEIGTH FOR MATERIAL FEW SPACE FOR STORAGE OF MATERIAL AND LIMITED CONSTRUCTION AREA FEW SPACE FOR CRANES VENTILATION & HSE ASPECTS

CONSTRUCTION SEQUENCE EXCAVATION LNG TANK AUXILIARIES UNITS INSTRUMENTATION Excavation for tank & construction area Tank Design Tank Procurement Procurement of Instrumentation ? Tank Construction & tests Construction of above ground & below ground facilities Installation of instrumentation? Tank Mechanical completion First Raw Liquid Argon truck Cool down & first fill operation Last Raw Liquid Argon truck READY FOR OPERATION

THANK YOU FOR YOUR ATTENTION