This document outlines the key steps in the liquefied natural gas (LNG) production process. It begins with extracting natural gas from the ground, then treating the gas to remove impurities. The treated gas is then condensed into a liquid by cooling it to -260°F through a multi-stage liquefaction process. The LNG is stored and transported in specialized cryogenic tanks on ships or trucks, then regasified back into gas form before being distributed through pipelines. The document provides details on each stage of the LNG value chain from production to regasification and discusses related technologies like compressed natural gas.
2. Outline Lecture
What is LNG?
LNG Production Process
Production of LNG
Basic Facts
LNG industry and Technology(or LNG Value Chain)
1)Production
2)Liquefaction :Train Size; Compressor Drive Efficiency
3)Transportation
3.1)Pipe
3.2) Shipping
3.3) Tanker
Major Natural Gas Trade Movements
4) Regasification
5) Storage
How much does LNG cost?
Conclusion
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5. General LNG Production Process
Heat
Exchangers
Gas
Treatment
Refrigerant
Compression
LNG
Ships
Pipeline
Feed Gas
-260oF
LNG Storage
Pentanes and heavier
Condensates
Impurities:
Carbon Dioxide (CO2)
Mercury (Hg)
Hydrogen Sulfide (H2S)
Water (H2O)
Nitrogen (N2)
Heat expelled
to water or air
Source: Cheniere
LNG manufacture uses the real gas law.
A mixed refrigerant system chills methane until it reaches changes its state from a gas to a liquid.
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6. Typical Sour Gas Plant with NGL Recovery
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24. Modified Stertford® process flow diagram to Direct conversion
of H2S to sulfur (Joule Processing, 2012)
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25.
26. Gas Sweetening Processes
• There is a great number of existing and economically viable gas sweetening
processes, and some of them are listed below according to chemical and
physical principles used (Arnold & Stewart, 1999):
1) Solid bed absorption:
Iron Sponge
SulfaTreat® (Licensor: The SulfaTreat Company)
Zinc Oxide
Molecular Sieves (Licensor: Union Carbide Corporation)
2) Chemical solvents:
Monoethanol amine (MEA)
Diethanol amine (DEA)
Methyldiethanol amine (MDEA)
Diglycol amine (DGA)
Diisopropanol amine (DIPA)
Hot potassium carbonate
Proprietary potassium systems
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3) Physical solvents:
Fluor Flexsorb® (Licensor: Fluor Daniel Corporation)
Shell Sulfinol®
Selexol® (Licensor: Norton Co., Chemical Process Products)
Rectisol® (Licensor: Lurg, Kohle & Mineraloltechnik GmbH
& Linde A.G.)
4) Direct conversion of H2S to sulfur
Claus
LOCAT® (Licensor: ARI Technologies)
Strertford® (Licensor: Ralph M. Parsons Co.)
IFP (Licensor: Institute Francais du Petrole)
Sulfa-check® (Licensor: Exxon Chemical Co.)
5) Hydrogen sulfide scavengers
6) Distillation
Amine-aldehyde condensates
7) Gas permeation
30. Melkøya LNG Plant with LNG Carrier Arctic Princess Photo: Statoil
The LNG feedstock comes from a gas plant as outlined above. It must satisfy
sales gas specifications. Ethane, propane and butane all have freezing points
of less than -180°C and can be part of the LNG, but the concentration of
methane is generally above 90%. Some NGLs are also needed as refrigerant
for the cryogenic process.
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36. • At the receiving terminal, LNG is stored in local
cryogenic tanks. It is regasified to ambient temperature
on demand, commonly in a sea water heat exchanger,
and then injected into the gas pipeline system.
Cove point LNG terminal
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41. Transportation of the gas
90% of the investment involved is in shipping of the gas.
Loading and unloading is possible and easy with small facilities.
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Opportunities for CNG Marine Transport
VOTRANS™ Shifts CNG Paradigm
RATE,mmscfd
1,000
500
1,500
RATE,mmscfd
1,000
500
1,500
Pipelines LNG
Hydrates
3,0002,0001,0000
Transport Distance, nm
3,0002,0001,0000
Transport Distance, nm
CNG
3,0002,0001,0000
Transport Distance, nm
43,0002,0001,0000
Transport Distance, nm
43,0002,0001,0000
Transport Distance, nm
4
VOTRANSTM
42. CNG Cargo Containment System
For distances up to 2500 miles, CNG appears more attractive than LNG
Major advantage in terms of market entry
Much less capital deployed in country
Up to 2 Bcf on a ship
Ideal for limited supply, limited consuming markets
CNG Application
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50. Existing and Emerging Technologies
Company Syngas Fischer-Tropsch Catalyst
Plant Size
(bpd)
Sasol (SPD) ATR(O2)
Slurry phase
180-250oC, 10-45 atm Fe, Co 50,000
Shell (SMDS) POX(O2)
Fixed bed (Non-catalytic)
180-250oC, 10-45 atm
Co 50,000
ExxonMobil
AGC-21
ATR(O2)
Slurry phase
(Fluidized bed)
180-250oC, 10- 45 atm (“RIM”)
Co >50,000
BP SMR Fixed bed Co
Syntroleum ATR(air)
Fixed bed
180-250oC, 10-45 atm
Co <10,000
Rentech SR Fixed bed, slurry Fe <5,000
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