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29/11/2016 1 Energoil Consulting Liquefaction Processes Lecture 11 LNG Import Terminals Slide 1 © Dr. Richard J Barnes 2013 Energoil Consulting Liquefaction Processes Types of Terminal Slide 2 © Dr. Richard J Barnes 2013

Lecture 11 LNG Import Terminals R2 - FIT Staffwebstaff.fit.ac.cy/eng.ap/FALL2016/MOE506/Lecture 11 LNG Import... · • FSRU -Floating Storage and ... ... Lecture 11 LNG Import Terminals

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Page 1: Lecture 11 LNG Import Terminals R2 - FIT Staffwebstaff.fit.ac.cy/eng.ap/FALL2016/MOE506/Lecture 11 LNG Import... · • FSRU -Floating Storage and ... ... Lecture 11 LNG Import Terminals

29/11/2016

1

Energoil

Consulting

Liquefaction Processes

Lecture 11

LNG Import Terminals

Slide 1© Dr. Richard J Barnes 2013

Energoil

Consulting

Liquefaction Processes

Types of Terminal

Slide 2© Dr. Richard J Barnes 2013

Page 2: Lecture 11 LNG Import Terminals R2 - FIT Staffwebstaff.fit.ac.cy/eng.ap/FALL2016/MOE506/Lecture 11 LNG Import... · • FSRU -Floating Storage and ... ... Lecture 11 LNG Import Terminals

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Energoil

Consulting

Existing LNG Terminals

Operational in 2008

Japan 32 Brazil 2

USA 12 Chile 2

China 8 Italy 2

Spain 7 Taiwan 2

UK 5 Turkey 2

India 4 Belgium 1

South Korea 4 Greece 1

France 3 Canada 1

Mexico 3 Puerto Rica 1

Portugal 1

Total 93

Slide 3© Dr. Richard J Barnes 2013

Energoil

ConsultingTerminal Location

Terminal may be located:

• On the mainland (most common).

• On an island.

• On a platform.

• On a dedicated vessel.

Slide 4© Dr. Richard J Barnes 2013

Page 3: Lecture 11 LNG Import Terminals R2 - FIT Staffwebstaff.fit.ac.cy/eng.ap/FALL2016/MOE506/Lecture 11 LNG Import... · • FSRU -Floating Storage and ... ... Lecture 11 LNG Import Terminals

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Energoil

ConsultingMainland Terminal

• Requires deep water port.

• Easy access to export trunkline.

• Construction cost relatively low.

• Can be difficult to get planning approval -locals may object.

Source: www.ch-IV.com

Slide 5© Dr. Richard J Barnes 2013

Energoil

ConsultingIsland Terminal

• Requires deep water port.

• Access to export trunkline includes subsea link.

• Construction cost relatively low.

• Can be easier to get planning approval.

Source: tritonsa.gr

Slide 6© Dr. Richard J Barnes 2013

Page 4: Lecture 11 LNG Import Terminals R2 - FIT Staffwebstaff.fit.ac.cy/eng.ap/FALL2016/MOE506/Lecture 11 LNG Import... · • FSRU -Floating Storage and ... ... Lecture 11 LNG Import Terminals

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Energoil

ConsultingPlatform Terminal

• Deep water alongside.

• Could use old oil platform.

• Less planning problems.

• Requires subsea connector to land.Source: fiesta.bren.ucsb.edu

Slide 7© Dr. Richard J Barnes 2013

Energoil

ConsultingDedicated Vessel

• FSRU - Floating Storage and Regasification Unit.

• Same benefits as offshore platform terminal.

• Provides storage.

• LNG tanker is not delayed in turnaround.

Source: fiesta.bren.ucsb.edu

Source: http://www.excelerateenergy.com/downloads/Excelerate_teesside_08.pdf

Slide 8© Dr. Richard J Barnes 2013

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Energoil

Consulting

Liquefaction Processes

Marine Facilities

Slide 9© Dr. Richard J Barnes 2013

Energoil

ConsultingMarine Facilities

• Deep water channel required, typically about 17 m minimum.

• Adequate manoeuvring space, typically twice vessel length.

• Adequate tug support.

• Potential to close port whilst LNG tanker is in port.

Slide 10© Dr. Richard J Barnes 2013

Page 6: Lecture 11 LNG Import Terminals R2 - FIT Staffwebstaff.fit.ac.cy/eng.ap/FALL2016/MOE506/Lecture 11 LNG Import... · • FSRU -Floating Storage and ... ... Lecture 11 LNG Import Terminals

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Energoil

ConsultingLNG Tanker Manoeuvring

Slide 11© Dr. Richard J Barnes 2013

Source: http://www.porttechnology.org/images/sized/images/uploads/news/LNG_Tanker-600x0.jpg

Source: http://www.asianews.it/files/img/russia-LNG-tanker.preview.jpg

Source: http://dmn.wpengine.netdna-cdn.com/wp-content/uploads/2011/11/CG-security-escort-for-tanker-Matthew.jpg

Energoil

Consulting

Liquefaction Processes

Offloading Rate

Slide 12© Dr. Richard J Barnes 2013

Page 7: Lecture 11 LNG Import Terminals R2 - FIT Staffwebstaff.fit.ac.cy/eng.ap/FALL2016/MOE506/Lecture 11 LNG Import... · • FSRU -Floating Storage and ... ... Lecture 11 LNG Import Terminals

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Energoil

Consulting

• LNG tankers are normally loaded and offloaded in 24 hours.

• Cargo size is between 75,000 m3 and 160,000 m3.

• Offloading rate must be 6,700 m3/hr.

© Dr. Richard J Barnes 2013 Slide 13

Offloading Rate

Energoil

Consulting

Liquefaction Processes

Loading/Offloading Arms

Slide 14© Dr. Richard J Barnes 2013

Page 8: Lecture 11 LNG Import Terminals R2 - FIT Staffwebstaff.fit.ac.cy/eng.ap/FALL2016/MOE506/Lecture 11 LNG Import... · • FSRU -Floating Storage and ... ... Lecture 11 LNG Import Terminals

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Energoil

Consulting

• Typical installation is:

– 2 or 3 liquid loading arms;

– 1 vapour return;

– 1 liquid/vapour spare.

• Each arm has a 5,000 m3/hr rate.

© Dr. Richard J Barnes 2013 Slide 15

Loading Arms

Source: http://maritime-connector.com/ships_uploads/hilli-7382720-lng_tanker-port_-_dry_dock-566.jpg

Energoil

Consulting

• Each arm consists of:

– A riser pipe;

– An inboard arm;

– An outboard arm.

• Each section is vacuum insulated.

• Inner pipe is 16 to 24” diameter.

• Outer pipe is 20 to 28”.© Dr. Richard J Barnes 2013 Slide 16

Loading Arm Detail

Page 9: Lecture 11 LNG Import Terminals R2 - FIT Staffwebstaff.fit.ac.cy/eng.ap/FALL2016/MOE506/Lecture 11 LNG Import... · • FSRU -Floating Storage and ... ... Lecture 11 LNG Import Terminals

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Energoil

Consulting

• Each arm section is about 9 m long.

• Design allows for ship movement due to tide, wind and cargo discharge.

© Dr. Richard J Barnes 2013 Slide 17

Arm Flexibility

Source: Design and Construction SpecificationFor MARINE LOADING ARMS, (Third Edition –1999), OCIMF

Energoil

Consulting

• Each arm is fitted with safety devices.

• Quick connect/disconnect couplers (QCDC)

• Emergency release systems (ESRs).

• Position monitoring.

© Dr. Richard J Barnes 2013 Slide 18

Arm Safety

Source: http://www.fmctechnologies.com/en/LoadingSystems/Technologies/ChiksanMarineLoadingSystems/~/media/LoadingSystems/Images/440_ChiksanMLA_LNGservice-280x240.ashx?bc=White&as=1&w=280

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Energoil

Consulting

• Provides easy positioning and quick connection to ship’s manifold.

• Hydraulic power supplied by marine arm.

• Operator can connect from a distance.

© Dr. Richard J Barnes 2013 Slide 19

Quick Connect/Disconnect Couplers

Source: http://www.niigata-ls.co.jp/jp/products/loading_arm/marine/options/images/qcdc/img01_001.jpg

Energoil

Consulting

• Disconnects loading arm in case of fire, sudden tanker movement or other event.

• Two valves close and tanker is decoupled.

• Interlock prevents spillage.

© Dr. Richard J Barnes 2013 Slide 20

Emergency Release Systems

Source: http://www.niigata-ls.co.jp/jp/products/loading_arm/marine/options/images/ers/img01_001.jpg

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Energoil

Consulting

• Provides real-time data on loading arm position.

• Monitors position of tanker and arms.

• Movement of tanker.

• Displays operating envelope and gives alarm on excursions.

© Dr. Richard J Barnes 2013 Slide 21

Position Monitoring System

Source: http://www.niigata-ls.co.jp/jp/products/loading_arm/marine/options/images/pms/img01_001.jpg

Energoil

Consulting

Liquefaction Processes

Terminal Process Scheme

Slide 22© Dr. Richard J Barnes 2013

Page 12: Lecture 11 LNG Import Terminals R2 - FIT Staffwebstaff.fit.ac.cy/eng.ap/FALL2016/MOE506/Lecture 11 LNG Import... · • FSRU -Floating Storage and ... ... Lecture 11 LNG Import Terminals

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Energoil

ConsultingTerminal Flow Scheme

Boil OffCompressor

VapourReturn Blower

VapourReturn Line

LNG Unloading Lines

LNG StorageTanks

First StageSendout Pumps

Second StageSendout Pumps

Recondenser

Vapouriser

Natural GasTrunk line

Slide 23© Dr. Richard J Barnes 2013

Energoil

Consulting

Liquefaction Processes

Terminal Storage

Slide 24© Dr. Richard J Barnes 2013

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Energoil

Consulting

• Tank can be 80-90 m diameter and 50 m high.

• Typical volume is 160,000 m3 up to 250,000 m3.

• Normally a minimum of two tanks at a terminal.

© Dr. Richard J Barnes 2013 Slide 25

Terminal Tank Size

Source: http://s0.geograph.org.uk/geophotos/01/02/54/1025438_82c70921.jpg

Energoil

ConsultingLNG Storage Tanks

• Single containment.

• Double containment.

• Full containment.

• Membrane.

• In-ground storage.

• Standard tank size is now 160,000 m3.

Slide 26© Dr. Richard J Barnes 2013

Page 14: Lecture 11 LNG Import Terminals R2 - FIT Staffwebstaff.fit.ac.cy/eng.ap/FALL2016/MOE506/Lecture 11 LNG Import... · • FSRU -Floating Storage and ... ... Lecture 11 LNG Import Terminals

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Energoil

ConsultingTank Choice

• Full containment more expensive than single containment.

• Extra area of single containment tanks may be too expensive or not available.

• Single containment tanks require larger fire fighting and vapour compression.

• Concrete full containment tanks provide increased protection against external events.

• In-ground tanks claimed to be better in seismically active areas (Japan has 76 in-ground tanks). Slide 27© Dr. Richard J Barnes 2013

Energoil

Consulting

• Receiving terminals built for winter period supply.

• Require sufficient tanks that one can be delivering to pipeline, whilst other is being filled.

• More tanks may be built to meet strategic demand and provide buffer storage.

© Dr. Richard J Barnes 2013 Slide 28

Terminal Storage Capacity

Page 15: Lecture 11 LNG Import Terminals R2 - FIT Staffwebstaff.fit.ac.cy/eng.ap/FALL2016/MOE506/Lecture 11 LNG Import... · • FSRU -Floating Storage and ... ... Lecture 11 LNG Import Terminals

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Energoil

Consulting

Liquefaction Processes

Types of Vaporiser

Slide 29© Dr. Richard J Barnes 2013

Energoil

ConsultingVapouriser Types

• Open Rack.

• Submerged Combustion.

• Shell and tube.

• Cold utilisation.

Slide 30© Dr. Richard J Barnes 2013

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Energoil

ConsultingOpen Rack Vaporiser

• Takes heat from seawater to vaporise LNG.

• Environmental restrictions on seawater return temperature.

• Biocide added to seawater to inhibit marine growth.

• Seawater can create corrosion problems.

Source: http://www.spp.co.jp/English/jigyou/ekika-e.html

Slide 31© Dr. Richard J Barnes 2013

Energoil

Consulting

Submerged Combustion

Vaporiser

• Heat is supplied by burning natural gas.

• Flame is submerged for direct heat transfer to the water heating medium.

• Water becomes corrosive because CO2 dissolves in it.

• No flame impingement or hot spots.

Source: http://www.spp.co.jp/English/jigyou/ekika-e.html

Slide 32© Dr. Richard J Barnes 2013

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Energoil

ConsultingShell and Tube

• Several different configurations;

• Seawater cooled indirectly by propane;

• Reduces risk of seawater freezing

• Also suitable for temperature recovery.Slide 33© Dr. Richard J Barnes 2013

Source: .kobelco.co.jp/english/machinery/products/ecmachinery/lng/ifv.html

Energoil

Consulting“Cold” Recovery

Low temperature used in other process:

• Cool air intake of CCGTG;

• Pre-cooling in air separation;

• Cold storage of frozen food;

• Refrigeration and industrial use;

• Production of CO2 and dry ice;

• Ethane and propane extraction and recovery.

Slide 34© Dr. Richard J Barnes 2013

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Energoil

Consulting

Liquefaction Processes

LNG Pumps

Slide 35© Dr. Richard J Barnes 2013

Energoil

Consulting

• Pumps in each storage tank deliver the LNG at about 7 barg.

• The pumps are installed from the top of the tank, so that no aperture is cut into the tank below liquid level.

• Several pumps are installed to give adequate spares.

• LNG is pumped around the loading lines to keep them cold.

© Dr. Richard J Barnes 2013 Slide 36

In-tank Pumps

Source: http://www.nikkiso.com/products/pump/submerged/img/c04-1.jpg

Page 19: Lecture 11 LNG Import Terminals R2 - FIT Staffwebstaff.fit.ac.cy/eng.ap/FALL2016/MOE506/Lecture 11 LNG Import... · • FSRU -Floating Storage and ... ... Lecture 11 LNG Import Terminals

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Energoil

Consulting

• Send-out pumps boost the LNG to pipeline pressure before the vaporiser.

• Due to the high head normally required, multi-stage, canned pumps are used.

© Dr. Richard J Barnes 2013 Slide 37

Send-out Pumps

Source: http://www.lngexpress.com/lngl/Pres/TommyStone.pdf

Energoil

Consulting

Liquefaction Processes

Boil Off Gas

Slide 38© Dr. Richard J Barnes 2013

Page 20: Lecture 11 LNG Import Terminals R2 - FIT Staffwebstaff.fit.ac.cy/eng.ap/FALL2016/MOE506/Lecture 11 LNG Import... · • FSRU -Floating Storage and ... ... Lecture 11 LNG Import Terminals

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Energoil

ConsultingVapour Disposal

• Vapour sent to tanker when unloading.

• Compressed, recondensed and fed to Second Stage Sendout Pumps.

• Compress and send direct to natural gas pipeline;

• Flare or vent.

Slide 39© Dr. Richard J Barnes 2013

Energoil

Consulting

© Dr. Richard J Barnes 2013 Slide 40

BOG Liquefaction Schematic

From BOGCompression

Liquid ReturnTo Tank

HP BOG toPipeline

Compressor-Expander

After-Cooler

CompressorAfter-Cooler

TC

PC

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Energoil

Consulting

Liquefaction Processes

Meeting Gas Specification

Slide 41© Dr. Richard J Barnes 2013

Energoil

ConsultingGas Higher Heating Values

Slide 42© Dr. Richard J Barnes 2013

Gas BTU/SCF MJ/m3

Methane 1,010.0 37.708

Ethane 1,769.6 66.065

Propane 2,516.1 93.936

Nitrogen 0.0 0.0

Page 22: Lecture 11 LNG Import Terminals R2 - FIT Staffwebstaff.fit.ac.cy/eng.ap/FALL2016/MOE506/Lecture 11 LNG Import... · • FSRU -Floating Storage and ... ... Lecture 11 LNG Import Terminals

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Energoil

ConsultingEffect of Ethane and Propane

• 20% ethane or 10% propane could be added to gas and still meet the CV specification.

• Wobbe specification limits addition to 5% ethane and 4% propane.

Slide 43© Dr. Richard J Barnes 2013

Energoil

ConsultingAddition of 5% Nitrogen

• Addition of inert gas decreases both CV and Wobbe.

• Up to 15% ethane can be added or 10% propane and still meet both specifications.

Slide 44© Dr. Richard J Barnes 2013

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Energoil

Consulting

Liquefaction Processes

Import Terminal

Cost Breakdown

Slide 45© Dr. Richard J Barnes 2013

Energoil

ConsultingTypical Cost Breakdown

Jetty 11%

Tanks 45%

Process 24%

Utilities 16%

General Facilities 4%

Total 100%

Slide 46© Dr. Richard J Barnes 2013

Page 24: Lecture 11 LNG Import Terminals R2 - FIT Staffwebstaff.fit.ac.cy/eng.ap/FALL2016/MOE506/Lecture 11 LNG Import... · • FSRU -Floating Storage and ... ... Lecture 11 LNG Import Terminals

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Energoil

ConsultingCAPEX Estimate

• Dependent on soil conditions;

• Jetty length and need for dredging;

• Cost of land and area required;

• $70 - 150 / tpa capacity.

(Source: BG Group)

Slide 47© Dr. Richard J Barnes 2013

Energoil

Consulting

Liquefaction Processes

End of Presentation

Slide 48© Dr. Richard J Barnes 2013