IP Library Granted Patent US 10,443,926
Granted Patent B2
US 10,443,926 · App. 14/924,788 · Granted Oct 15, 2019

System and method for liquefied natural gas production

Inventors: Daniel Ohart (Waverly, NY); Greg Yonker (Lawrenceville, GA); Jason M. Kerth (Houston, TX)
Assignee: DRESSER-RAND COMPANY
F25J1/0022F25J1/004F25J1/005F25J1/0045F25J1/0052F25J1/0087F25J1/023F25J1/0208F25J1/0227F25J1/0264F25J1/0265F25J1/0268F25J1/0284F25J1/0288F25J2210/06F25J2230/30F25J2270/12F25J2270/60F25J2270/90F25J2270/906
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Quick Facts
Patent No.
US 10,443,926
App. No.
14/924,788
Granted
Oct 15, 2019
Kind
B2
Abstract

A system and method for producing liquefied natural gas from a natural gas source is provided. The method may include feeding natural gas provided by the natural gas source to a liquefaction module. The method may also include flowing the natural gas through a product stream of the liquefaction module. The method may further include flowing a process fluid through a liquefaction stream of the liquefaction module to cool at least a portion of the natural gas flowing through the product stream to produce the liquefied natural gas.

Claims (29)

1. A method for producing liquefied natural gas from a natural gas source, comprising:

feeding natural gas provided by the natural gas source to a precompression module;

controlling the precompression module to increase or decrease an amount of the liquefied natural gas to be produced by the method based at least in part on a level of pressure imparted by the precompression module to the natural gas fed into the precompression module;

directing the natural gas from the precompression module to a product stream of the liquefaction module,

wherein the directing of the natural gas to the product stream of the liquefaction module comprises:

cooling the natural gas in a pre-cooling heat exchanger of a cooling assembly;

further cooling the cooled natural gas from the cooling assembly in a first heat exchanger of a pair of heat exchangers downstream from the cooling assembly;

expanding the further cooled natural gas from the first heat exchanger of the pair of heat exchangers downstream from the cooling assembly in an expansion valve to produce a two-phase fluid including liquefied natural gas and a vapor phase; and

separating the liquefied natural gas from the vapor phase in a liquid separator of the liquefaction module; and

directing a process fluid to a liquefaction stream of the liquefaction module to cool at least a portion of the natural gas directed to the product stream,

wherein the directing of the process fluid to the liquefaction stream of the liquefaction module comprises:

compressing the process fluid in a compression assembly;

cooling the compressed process fluid in another heat exchanger of the cooling assembly;

further cooling the cooled, compressed process fluid in a second heat exchanger of the pair of heat exchangers;

at least partially separating natural gas liquids from the further cooled, compressed process fluid from the second heat exchanger of the pair of heat exchangers in a liquid separator to form at least a further cooled, compressed process vapor;

expanding the further cooled, compressed process vapor in a turbine of a turbomachinery to generate a refrigeration stream; and

cooling the at least a portion of the natural gas directed to the product stream with the refrigeration stream.

2. The method of claim 1 , further comprising storing the liquefied natural gas in a storage tank fluidly coupled with the liquefaction module.

3. The method of claim 2 , further comprising:

feeding the vapor phase from the liquid separator of the liquefaction module to a flash recovery module fluidly coupled with the liquefaction module; and

cooling at least a portion of natural gas from the precompression module in the flash recovery module with the vapor phase.

4. The method of claim 2 , wherein the directing of the process fluid to the liquefaction stream of the liquefaction module further comprises:

compressing the refrigeration stream in a compressor of the turbomachinery to produce a recycle stream; and

compressing the recycle stream in the compression assembly.

5. The method of claim 2 , further comprising:

generating electrical energy in a power generation module;

delivering the electrical energy from the power generation module to the liquefaction module; and

driving the compression assembly of the liquefaction module with the electrical energy.

6. The method of claim 1 , further comprising removing at least a portion of a non-hydrocarbon from the natural gas provided from the natural gas source in a conditioning module before feeding the natural gas provided from the natural gas source to the liquefaction module.

Assignments (3)
MERGER Recorded Mar 8, 2023
From: DRESSER-RAND COMPANY
To: SIEMENS ENERGY, INC.
Reel/Frame 062916/0264 →
MERGER Recorded Mar 8, 2023
From: DRESSER-RAND COMPANY
To: SIEMENS ENERGY, INC.
Reel/Frame 062916/0825 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Apr 12, 2016
From: OHART, DANIEL; YONKER, GREG; KERTH, JASON M.
To: DRESSER-RAND COMPANY
Reel/Frame 038251/0602 →
Continuity (3)
Provisional Application 62081799 · Nov 19, 2014
Provisional Application 62246171 · Oct 26, 2015
Related Publication 20160138861A1 · May 19, 2016