Small scale boil off gas (BOG) re-liquefaction systems

Similar documents
DH Industries. Francesco Dioguardi

TECHNICAL SPECIFICATION. StirLNG-4 Maritime Stirling Cryogenics gas liquefier for LNG conditioning

Power Recovery in LNG Regasification Plants

LNG Systems for Marine Application. LNG Reliquefaction & LNG Regasification. Oil & Gas Systems

A new re-liquefaction system of MRS-F (Methane Refrigeration System Full re-liquefaction) for LNG Carriers

Cryogenic Expanders Operating on LNG-FPSO Vessels Hans E. Kimmel

NOVEL SCHEME FOR SMALL SCALE LNG PRODUCTION in POLAND. W.H. Isalski

LNG THE FUTURE IS TODAY ROYAL INSTITUTION OF NAVAL ARCHITECTS PETER KELLER NOVEMBER 19, 2015

Magnetically Coupled Submerged Cryogenic Pumps and Expanders for Ammonia Applications

ecosmrt LNG Reliquefaction INTERTANKO 2 nd May 2018

Low Carbon Technology for Marine Application. Hyundai Heavy Industries / Corporate Research Center Se-Young Oh, Sangmin Park Nov.

International Journal of Scientific & Engineering Research, Volume 5, Issue 7, July-2014 ISSN

Comparison of Spherical and Membrane Large LNG Carriers in Terms of Cargo Handling

Reliquification of Boil of Gas by using BOG Compressor

EBARA INTERNATIONAL CORPORATION Cryodynamics Division. Cryogenic Turbine Expanders. cryodynamics. Cryogenic Expanders for Liquefied Gas

Creating Optimal LNG Storage Solutions. 40 in detail

Estimation of Boil-off-Gas BOG from Refrigerated Vessels in Liquefied Natural Gas Plant

LNG study for MPSE project

Flammable Cryogenic Liquid Carriers

LNG as a marine bunker fuel

Modern Small-Scale LNG Plant Solutions

LCNG-LNG refuelling stations LNG AS A FUEL FOR VEHICLES.

Why LNG? LNG is mainly produced for transportation purposes. More economical to transport gas as LNG compared to pipelines over long distances

Transfer and Storage of Flammable Liquefied Hydrocarbon Gases

DEVELOPMENT OF DOWNHOLE PUMP FOR BINARY CYCLE POWER GENERATION USING GEOTHERMAL WATER

Equipment and Solutions LNG TRANSPORTATION, CARGO HANDLING AND FUELLING APPLICATIONS

DETERMINING THE MAXIMUM LNG PRODUCTION RATE BY PROCESS SIMULATION MODELLING OF LOW TEMPERATURE NATURAL GAS SEPARATION UNIT

LNG AS FUEL: THE TIPPING POINT?

Large scale hydrogen liquefaction in combination with LNG re-gasification

Research on a Magnetic Refrigeration Cycle for Hydrogen Liquefaction

The following sub-systems are provided and the integration of these is described below:

COMBINED HEAT AND POWER SYSTEMS IN LIQUEFIED NATURAL GAS (LNG) REGASIFICATION PROCESSES

Marine Facilities for LNG Carrier Transfer Alternatives

BOIL-OFF GAS MANAGEMENT LNG TERMINAL TECHNOLOGIES

CO 2. Recovery AND PRODUCTION

The World First Ever Very Large Ethane Carrier (VLEC)

LNG PUMPS FOR FLOATING STORAGE AND REGAS UNIT

DESIGN ANALYSIS OF A REFRIGERATED WAREHOUSE USING LNG COLD ENERGY

GTI Small-Scale Liquefier Technology. March 2013

2017 LPG Loading Master & Certification (3 Days)

Small Scale LNG From Concept to Reality. Chris Johnson, General Manager, LNG New Markets, Shell

Liquefaction of Bulk Cargoes

ENVIRONMENT-FRIENDLY ENERGY SOLUTIONS

LNG BUNKERING VESSELS AND CNG CARRIERS -Innovative solutions to improve sustainability- LNG/SHORE POWER Workshop TRIESTE 10 th of March 2016

Marine Tech SHIP OPERATIONS. Dr. Alok K. Verma Lean Institute - ODU

The general design of a LNG-terminal. Background

Study on a High-Power Stirling Cryocooler

Motorways of the Sea Forum. Brussels, 16 th of June 2017

Aim of BSR LNG Competence Center

Thermo-Fluid Modeling of a Full Scale Liquid Hydrogen Storage System with Integrated Refrigeration

Integrated ISRU for Human Exploration Propellant Production for the Moon and Beyond

R/V ZERO-V A ZERO-EMISSION HYDROGEN FUEL CELL RESEARCH VESSEL 29 AUGUST 2018 UNOLS GREEN BOATS AND PORTS CONFERENCE 2018

MARITIME LNG, REGULATION AND LOCAL DEVELOPMENT FRAMEWORK 25 November 2014 Andrew Morris, Director

LNG Terminal in Świnoujście. Mutual Joint Visit Workshop for Seveso Inspections 26 September 2017, Nicosia, Cyprus

A DUAL LOOP ORGANIC RANKINE CYCLE UTILIZING BOIL-OFF GAS IN LNG TANKS AND EXHAUST OF MARINE ENGINE. * Corresponding Author ABSTRACT 1.

Uniflo Fog Reduction Module

Application for a recommendation on the use of membrane tanks for transport of liquefied natural gas on the tank vessel Argos-GL

MB 1 Contribute to the safe operation of a ship subject to IGF Code

CRYOGENICS OPTIONS FOR THE MMA. L. D'Addario, 97/09/20 REQUIREMENTS. We begin by assuming that the required cooling at each antenna

Transfer lines for liquefied natural gas for fast and safe offloading in rough seas and onshore

Typical projects of low-tonnage complexes for the production of LNG on GRS with a capacity from 1.5 to 5.0 t / hr

Cryobox-Bio. Biomethane upgrading and liquefaction nano station. & Virtual Pipeline

LNG as a Bunker Fuel - LNGF (3 Days)

2019 LNG as a Bunker Fuel - LNGF (3 Days)

Faculty of Engineering 2 nd year 2016 Mechanical Engineering Dep. Final-exam (code: M 1222)

Guidance for Structural Strength Assessment of Pump Tower of LNG Carriers

POWER RECOVERY IN FLOATING LNG REGASIFICATION PLANTS

LNG CARRIERS. Eniram Solutions for H I G H W I N D S O N T H E R O U T E - T R I M 2 3 C M B Y T H E B O W F O U L I N G I N C R E A S E D B Y 1 2

K-Sim Engine Diesel Electric Dual Fuel Cruise Ferry. Evy Kristine Sæter Product Advisor Engine Room Simulator

The Latest Progress of CCS Research on Springing & Whipping And Joint Industry Project with MARIN

Energy Efficiency and Recovery at Large Scale Cryogenic Plants: A Survey

Executive Summary. Engineering Report of the: Adaptation of jetties and LNG transfer facilities for loading of bunker vessels in Fos Tonkin

(12) Patent Application Publication (10) Pub. No.: US 2008/ A1

Submerged Motor LNG Pumps In Send-Out System Service. Unique pumps for unique duty...

OPERATIONS SEAFARER CERTIFICATION GUIDANCE NOTE SA MARITIME QUALIFICATIONS CODE. Ancillary Courses: Advanced Training Chemical Tankers

GUIDANCE ON LNG BoG MONITORING

MONITORING CRYOGENIC TURBINES USING NO-LOAD CHARACTERISTICS

Micro Motion Developments in HFO & LNG metering Per Stenhammar. Business Development Manager

(52) U.S. Cl. 60/643

Properties Of Membrane Tanks For Transportation Of LNG Cargo On Ships

The Separation and Liquefaction of Oxygenated CBM Yang Kejian and Zhang Wu

An Introduction to the Patented. VX TM Cycle. Small-Scale Production of LNG from Low-Pressure Gas by Methane Expansion

ENGINE TESTING OF BUS FUELLED WITH LNG

Braemar Technical Services

04 November LNG Ready Capabilities

FIBA Technologies, Inc. Company Overview and Introduction Grafton Road, Millbury, MA

HYSYS WORKBOOK By: Eng. Ahmed Deyab Fares.

LNG Carriers Ship Life Extension. Ed Waryas. Lloyd s Register North America, Inc.

LNG for IWT status / barriers / activities Train Workshop Go LNG / Interreg Baltic Sea Region

2019 LPG Loading Master & LPG Terminal Operations - 3 days

Guidance for. LNG Fuel Ready Ships

NATURAL GAS. photo credit: Tourism BC

On board LNG reliquefaction technology: a comparative study

Enabling safe and reliable offshore LNG transfer operations By Vincent Lagarrigue, Marketing & Project Manager within Trelleborg Industrial Solutions

Refrigerant Expanders Improve LNG Liquefaction Process

Evolution of an LNG Terminal: Senboku Terminal of Osaka Gas

VANDOR S EXPANSION CYCLE: The VX Cycle

LNG as fuel and Bunkering Disruptive innovations

THE CONCEPT OF INTEGRATED CRYOGENIC ENERGY STORAGE FOR LARGE SCALE ELECTRICITY GRID SERVICES. Finland *corresponding author

A Study on Re-liquefaction Process of Boil-off Gas of LCO 2 Transfer Ship

Transcription:

Small scale boil off gas (BOG) re-liquefaction systems As presented by Francesco Dioguardi at the 7 th Gas Fuelled Ships Conference, Hamburg, November 17, 2016 1

DH Industries BV Based in Eindhoven, The Netherlands Successor of Philips Cryogenics, in business since 1955 Main product brands: Stirling Cryogenics: Several types of Cryogenerators to produce on site cooling power CryoZone: Several types of pumps and circulators for cryogenic gases and liquids Nordic Biogas Conference

StirLNG-4

CONDITIONING OF LNG

Why conditioning of LNG? To prevent (a) LNG storage (cargo or fuel) from venting (pressure control): Safety, environmental & economic Keep LNG cold = value To maintain the composition of the LNG (mixture) Conditioning can be done by: or Re-liquefying the (excess) boil off gas Cooling the liquid Both methods will decrease the tank pressure

Conditioning of LNG GAS LIQUID Liquefaction temperature of LNG increases with increasing pressure Reducing the pressure of a system will cool down the liquid & reducing liquid temperature will reduce pressure (as gas and liquid want to stay in equilibrium)

THE STIRLING CYCLE to create cryogenic cooling power

Stirling thermodynamic cycle Stirling Cryogenerator interior

Stirling thermodynamic cycle Step 1: Compression Helium gas is compressed Gas temperature rises Step 2: Cooling Compression heat is removed; The helium gas is pre-cooled in the regenerator before expansion starts Step 3: Expansion By expansion, energy is extracted from the gas and thereby the temperature goes down thus cooling the cold head Step 4: Displacement Gas is displaced back to the compression space; the cold from the helium gas is stored in the regenerator during displacement to step 1 Regenerator

Cooling capacity StirLNG-4

EASY PROCESS INTEGRATION

Easy process integration Internal cold generation by He gas: methane is not part of process Simple integration: at the LNG process side, the Stirling Cryogenerator is only a heat-exchanger. Small enough & efficient to fit maritime BOG size reliquefaction Capacity range 0.25 to > 10 ton/day.

Easy process integration The liquefier works as a simple heat exchanger either for gas or liquid No compression of LNG No contamination of LNG High efficiency Scalable, flexible and redundant liquid out gas in Nordic Biogas Conference

Conditioning by re-liquefaction of BOG Cold boil-off gas, directly from the tank, is fed to the Cryogenerator Gas is re-liquefied and fed back to main storage vessel No pumping required Driving force is pressure difference and gravity T of liquid will decrease with lower head pressure

Conditioning by liquid sub-cooling Liquid from the tank is pumped through the HX of the liquefier, decreasing its temperature Colder liquid re-enters the tank reducing overall T and pressure

ADAPTATIONS FOR MARITIME USE

Adaptation for Maritime usage Modifications made for maritime application: To assure functionality during roll and pitching Allow static inclination during (un)loading Vertical motion due to waves Vibrations Corrosion Remote operating Modifications to meet regulations (ABS, USCG, UL etc.)

Adaptation for Maritime usage Corrosion prevention for maritime circumstances Lubrication system and LNG outlets of StirLNG-4 adapted for 22,5 o dynamic roll and pitch, refer to videos Static tilting up to 15 o each direction Free directional positioning on ship For USCG: separation of Cryogenerator and motor by bulk head with rotating seal ABS Certified, other notified bodies upon request

ABS Type Approval Amongst others 22,5 Roll & pitch test Link to roll test clip Link to pitch test clip Note: Units are in operation during these tests to proof their full functionality

Adaptation for Maritime usage USCG requirement: Bulk head seal Motors in safe area

FIRST MARITIME PROJECT DESIGN AND PRODUCTION

2200 M 3 LNG Bunker Barge Based on conceptual design developed by GTT Single cargo tank of Mark III Flex technology with BOR 0.38%/day Cold LNG delivery ensured by 6 Stirling StirLNG-4 cryocooler units

StirLNG on board LNG Barge

StirLNG on board LNG Barge Design Parameters 6 x StirLNG-4 units: Capacity: 6 x ~ 900 kg /day = ~5,400 kg/day @ 0 barg and 0.5% N2 Power consumption: 6 x ~38 kw = ~ 228kW (+ water chillers) Operations: Each StirLNG-4 has its own controller and can start and stop on its own Dimensions and weight: lxbxh = 7,850 x 3,000 x 1,700mm (25.8 x 10 x 5.6 ) ~ 8,500 kg (18,800 lbs)

Re-liquefaction concept Boil off gas Liquid return LNG

Factory Acceptance Test

Factory Acceptance Test Each StirLNG-4 was tested for: Capacity: With LN2 at 4.8 barg (same liquefaction T as the expected BOG) Vibrations: at 5 points per unit, in 3 directions Temperatures: at 5 points per unit Error test: Each individual unit was error tested by simulating or initiating fault conditions. Result: All units successfully passed.

FIRST MARITIME PROJECT INSTALLATION

Installation at Conrad

Installation at Conrad

Installation at Conrad

For further information, please visit our Maritime website http://www.stirlingcryogenics.com/en/markets/maritime