Heat recovery steam generation integration with high pressure feed gas processes for the production of liquefied natural gas

Patent metadata

Field	Value
Publication number	US-12281845-B2
Application number	US-202118005478-A
Country	US
Kind code	B2
Filing date	May 20, 2021
Priority date	Jul 17, 2020
Publication date	Apr 22, 2025
Grant date	Apr 22, 2025

Abstract

A method of producing LNG. According to the method, a natural gas stream is compressed using first and second compressors. A cooler cools the natural gas stream so that the second compressor produces a cooled, compressed natural gas stream, which is liquefied in a liquefaction process. The liquefaction process uses a refrigerant compressor configured to compress a stream of refrigerant used to chill, condense, or liquefy the cooled, compressed natural gas stream. Using a heat recovery steam generation (HRSG) system, heat is recovered from a power source of the refrigerant compressor. A stream of pressurized steam is generated from the recovered heat. At least one of the first and second compressors is powered using at least part of the stream of pressurized steam.

First claim

What we claim:

1. A method of producing liquefied natural gas (LNG), the method comprising:
providing a natural gas stream at a pressure of less than 8.27 MPa (1,200 psia) from a supply of natural gas;
compressing the natural gas stream to a pressure of at least 10.34 MPa (1,500 psia), wherein the compressing is performed using a first compressor and a second compressor;
between the first compressor and the second compressor, cooling the natural gas stream so that the second compressor produces a cooled, compressed natural gas stream;
liquefying the cooled, compressed natural gas stream in a liquefaction process, the liquefaction process using a refrigerant compressor configured to compress a stream of refrigerant used to chill, condense, or liquefy the cooled, compressed natural gas stream;
using a heat recovery steam generation (HRSG) system, recovering heat from a power source of the refrigerant compressor and generating a stream of pressurized steam from the recovered heat; and
powering at least one of the first and second compressors using at least part of the stream of pressurized steam.

2. The method of claim 1 , wherein cooling the compressed natural gas stream comprises cooling the compressed natural gas stream in at least one heat exchanger that exchanges heat with an environment.

3. The method of claim 2 , wherein the liquefaction process comprises a dual mixed refrigerant process using a combination of first and second refrigeration sub-processes to liquefy the natural gas stream, and wherein the refrigerant compressor is a compressor for one of the refrigeration sub-processes.

4. The method of claim 3 , further comprising a fourth compressor that provides compression for the second refrigeration cycle, wherein the HRSG system recovers heat generated by a power source of the fourth compressor to further generate the stream of pressurized steam.

5. The method of claim 1 , wherein the liquefaction process comprises a single mixed refrigerant process using a refrigeration sub-process cycle to liquefy the natural gas stream, and wherein the refrigerant compressor is a compressor for the refrigeration sub-process.

6. The method of claim 1 , wherein the liquefaction process comprises a high pressure expansion process with a cooling cycle and a sub-cooling cycle, and wherein the refrigerant compressor is a compressor for the cooling cycle or the sub-cooling cycle.

7. The method of claim 1 , wherein the first and second compressors compress the natural gas stream to a pressure greater than 20.68 MPa (3,000 psia).

8. The method of claim 1 , wherein the natural gas expander is a work producing expander that expands the cooled compressed natural gas stream to a pressure less than 13.79 MPa (2,000 psia).

9. The method of claim 1 , further comprising:
prior to the liquefying step, expanding, in at least one work producing natural gas expander, the cooled compressed natural gas stream to a pressure that is less than 13.79 MPa (2,000 psia) and no greater than the pressure to which the natural gas stream was compressed.

10. The method of claim 9 , wherein the natural gas expander is mechanically coupled to the first compressor or to the second compressor.

11. The method of claim 1 , wherein the liquefaction process comprises two or more liquefaction modules, wherein each of the two or more liquefaction modules have a HRSG system associated therewith, and wherein the first compressor is powered using at least part of streams of pressurized steam generated by the HRSG systems associated with the two or more liquefaction modules.

Assignees

• Exxonmobil Technology & Engineering Company

Inventors

• Vincentelli Jorge
• Liu Yijun
• Nagavarapu Ananda K
• Wright Xiaoli Y

Classifications

• F25J1/0022 Primary

  Hydrocarbons, e.g. natural gas · CPC title

• F01K15/00

  Adaptations of plants for special use {(F01K7/02 takes precedence)} · CPC title

• F25J1/0285

  Combination of different types of drivers mechanically coupled to the same refrigerant compressor, possibly split on multiple compressor casings · CPC title

• F25J2220/62

  Separating low boiling components, e.g. He, H2, N2, Air · CPC title

• F25J1/0042

  by liquid expansion with extraction of work · CPC title