Increasing efficiency in an LNG production system by pre-cooling a natural gas feed stream

Patent metadata

Field	Value
Publication number	US-11060791-B2
Application number	US-201615182050-A
Country	US
Kind code	B2
Filing date	Jun 14, 2016
Priority date	Jul 15, 2015
Publication date	Jul 13, 2021
Grant date	Jul 13, 2021

Abstract

Described herein are systems and processes to produce liquefied natural gas (LNG) using liquefied nitrogen (LIN) as the refrigerant. Greenhouse gas contaminants are removed from the LIN using a greenhouse gas removal unit. The LNG is compressed prior to being cooled by the LIN.

First claim

What is claimed is:

1. A liquefied natural gas production system, the system comprising:
a natural gas stream from a supply of natural gas;
a liquefied nitrogen stream from a refrigerant supply;
at least one heat exchanger that exchanges heat between the liquefied nitrogen stream and the natural gas stream to at least partially vaporize the liquefied nitrogen stream, to produce an at least partially vaporized nitrogen stream, and at least partially condense the natural gas stream;
a natural gas compressor that compresses the natural gas stream to a pressure of at least 135 bara to form a compressed natural gas stream;
a natural gas cooler that cools the compressed natural gas stream after being compressed by the natural gas compressor; and
a natural gas expander that expands the compressed natural gas to a pressure less than 200 bara, but no greater than the pressure to which the natural gas compressor compresses the natural gas stream, after being cooled by the natural gas cooler;
wherein the natural gas expander is connected to the at least one heat exchanger to supply natural gas thereto,
wherein the at least one heat exchanger comprises a first heat exchanger, and further comprising a second heat exchanger that cools the natural gas stream prior to the natural gas stream being compressed in the natural gas compressor, wherein the at least partially vaporized nitrogen stream is used to cool the natural gas stream in the second heat exchanger.

2. A liquefied natural gas production system, the system comprising:
a natural gas stream from a supply of natural gas;
a liquefied nitrogen stream from a refrigerant supply;
at least one heat exchanger that exchanges heat between the liquefied nitrogen stream and the natural gas stream to at least partially vaporize the liquefied nitrogen stream, to produce an at least partially vaporized nitrogen stream, and at least partially condense the natural gas stream;
a natural gas compressor that compresses the natural gas stream to a pressure of at least 135 bara to form a compressed natural gas stream;
a natural gas cooler that cools the compressed natural gas stream after being compressed by the natural gas compressor; and
a natural gas expander that expands the compressed natural gas to a pressure less than 200 bara, but no greater than the pressure to which the natural gas compressor compresses the natural gas stream, after being cooled by the natural gas cooler;
wherein the natural gas expander is connected to the at least one heat exchanger to supply natural gas thereto,
wherein the at least one heat exchanger comprises a first heat exchanger, and further comprising a second heat exchanger that cools the compressed natural gas stream prior to the compressed natural gas stream being cooled in the natural gas cooler, wherein the at least partially vaporized nitrogen stream is used to cool the natural gas stream in the second heat exchanger.

3. A method of producing liquefied natural gas (LNG), the method comprising:
providing a natural gas stream from a supply of natural gas;
providing a liquefied nitrogen stream from a refrigerant supply;
passing the natural gas stream and the liquefied nitrogen stream through a first heat exchanger that exchanges heat between the liquefied nitrogen stream and the natural gas stream to at least partially vaporize the liquefied nitrogen stream, to produce an at least partially vaporized nitrogen stream, and at least partially condense the natural gas stream;
compressing the natural gas stream in a natural gas compressor to a pressure of at least 135 bara to form a compressed natural gas stream;
cooling, in a natural gas cooler, the compressed natural gas stream after being compressed by the natural gas compressor;
expanding, in a natural gas expander, the compressed natural gas stream to a pressure less than 200 bara, but no greater than the pressure to which the natural gas compressor compresses the natural gas stream, after being cooled by the natural gas cooler; and supplying natural gas from the natural gas cooler to the at least one heat exchanger to be at least partially condensed therein,
wherein the at least one heat exchanger comprises a first heat exchanger, the method further comprising cooling, in a second heat exchanger, the natural gas stream prior to compressing the natural gas stream in the natural gas compressor, wherein the at least partially vaporized nitrogen stream is used to cool the natural gas stream in the second heat exchanger.

4. A method of producing liquefied natural gas (LNG), the method comprising:
providing a natural gas stream from a supply of natural gas;
providing a liquefied nitrogen stream from a refrigerant supply;
passing the natural gas stream and the liquefied nitrogen stream through a first heat exchanger that exchanges heat between the liquefied nitrogen stream and the natural gas stream to at least partially vaporize the liquefied nitrogen stream, to produce an at least partially vaporized nitrogen stream, and at least partially condense the natural gas stream;
compressing the natural gas stream in a natural gas compressor to a pressure of at least 135 bara to form a compressed natural gas stream;
cooling, in a natural gas cooler, the compressed natural gas stream after being compressed by the natural gas compressor;
expanding, in a natural gas expander, the compressed natural gas stream to a pressure less than 200 bara, but no greater than the pressure to which the natural gas compressor compresses the natural gas stream, after being cooled by the natural gas cooler; and supplying natural gas from the natural gas cooler to the at least one heat exchanger to be at least partially condensed therein,
wherein the at least one heat exchanger comprises a first heat exchanger, the method further comprising cooling, in a second heat exchanger, the compressed natural gas stream prior to cooling the compressed natural gas stream being cooled in the natural gas cooler, wherein the at least partially vaporized nitrogen stream is used to cool the natural gas stream in the second heat exchanger.

Assignees

• Pierre Jr Fritz
• Gupte Parag A
• Huntington Richard A
• Denton Robert D
• Exxonmobil Upstream Res Co

Inventors

• Pierre Jr Fritz
• Gupte Parag A
• Huntington Richard A
• Denton Robert D

Classifications

• F25J3/08 Primary

  Separating gaseous impurities from gases or gaseous mixtures {or from liquefied gases or liquefied gaseous mixtures}(cold traps B01D8/00) · CPC title

• F25J3/0257

  separation of nitrogen (from air F25J3/04, production of nitrogen in general C01B21/00) · CPC title

• F25J3/0233

  separation of CnHm with 1 carbon atom or more · CPC title

• F25J1/025

  Details related to the refrigerant production or treatment, e.g. make-up supply from feed gas itself · CPC title

• F25J1/023

  for the combustion as fuels, i.e. integration with the fuel gas system · CPC title