Process for the production of a subcooled liquefied natural gas stream from a natural gas feed stream, and associated installation

Patent metadata

Field	Value
Publication number	US-9506690-B2
Application number	US-62458709-A
Country	US
Kind code	B2
Filing date	Nov 24, 2009
Priority date	Nov 25, 2008
Publication date	Nov 29, 2016
Grant date	Nov 29, 2016

Abstract

A process for the production of a subcooled liquefied natural gas stream from a natural gas feed stream. Passing a first natural gas feed stream through a first heat exchanger for precooling by heat exchange with a first stream of gaseous refrigerant produced in a first refrigeration cycle comprising a first dynamic expansion turbine. Passing the precooled feed stream through a second heat exchanger for liquefying by heat exchange with a second stream of gaseous refrigerant produced in a second refrigeration cycle comprising a second dynamic expansion turbine. Passing the liquefied natural gas stream through a third heat exchanger for subcooling the liquefied gas by heat exchange with a third refrigerant stream produced in a third refrigeration cycle comprising a third dynamic expansion turbine separate from the first turbine and the second turbine. An installation includes devices for conveying the natural gas stream, the heat exchangers and the turbines and compression devices cooling the refrigerants for the heat exchangers.

First claim

The invention claimed is:

1. A process for the production of a subcooled liquefied natural gas stream from a natural gas feed stream, the method comprising the following steps:
precooling the natural gas feed stream by passing the natural gas feed stream through a first heat exchanger for obtaining a feed stream precooled to a temperature below −20° C.;
liquefying the precooled feed stream by passing the precooled feed stream through a second heat exchanger for obtaining at least one liquefied natural gas stream at a temperature below −80° C.;
subcooling the liquefied natural gas stream by passing the liquefied natural gas stream through a third heat exchanger for obtaining a liquefied natural gas stream subcooled to a temperature below −120° C.;
during the precooling, placing the natural gas feed stream in a heat exchange relationship in the first heat exchanger with a first stream of substantially gaseous refrigerant and producing the substantially gaseous refrigerant in a first refrigeration cycle from a first gaseous stream of expanded refrigerant fluid issuing from a first dynamic gas expansion turbine;
during the liquefying, placing the precooled feed stream in a heat exchange relationship in the second heat exchanger with a second stream of gaseous refrigerant circulating in a second refrigeration cycle, producing the second gaseous refrigerant stream from a second gaseous stream of expanded fluid issuing from a second dynamic gas expansion turbine separate from the first dynamic gas expansion turbine;
during the subcooling, placing the liquefied natural gas stream in a heat exchange relationship in the third heat exchanger with a third refrigerant stream circulating in a third refrigeration cycle, producing the third refrigerant stream at least partly from a third gaseous stream of expanded fluid issuing from a third dynamic expansion turbine separate from the first and the second dynamic gas expansion turbines;
conveying a first stream of heated refrigerant obtained at an outlet of the first heat exchanger to a first compression device without passing the first stream of heated refrigerant through the second or the third heat exchangers;
conveying a second stream of heated refrigerant issuing from the second heat exchanger to a second compression device without passing the second stream of heated refrigerant through the first or the third heat exchangers; and
conveying a third stream of heated refrigerant issuing from the third heat exchanger to a third compression device without passing the third stream of heated refrigerant through the first or the second heat exchangers.

2. The process according to claim 1 , further comprising:
separating the first gaseous stream of expanded refrigerant fluid into a first gaseous refrigerant stream and a first auxiliary cooling stream;
placing the first auxiliary cooling stream in a heat exchange relationship in a second cycle thermal exchanger with compressed refrigerant stream issuing from the second compression device for forming a second cooled compressed refrigerant stream,
conveying the second cooled compressed refrigerant stream to the second expansion turbine for forming the second gaseous stream of expanded refrigerant fluid,
wherein the first auxiliary stream is a gaseous stream.

3. The process according to claim 2 , further comprising:
separating the second gaseous stream of expanded refrigerant fluid into the second gaseous refrigerant stream and a second auxiliary cooling stream, and
placing the second auxiliary cooling stream in a heat exchange relationship in a third cycle exchanger with compressed refrigerant issuing from the third compression device for forming a third cooled compressed refrigerant stream, and
conveying the third cooled compressed refrigerant stream to the third expansion turbine for forming the third gaseous stream of expanded refrigerant fluid.

4. The process according to claim 1 , wherein the refrigerant streams comprise respective refrigerant fluids circulating in the first refrigeration cycle, in the second refrigeration cycle and in the third refrigeration cycle and the fluids are kept completely separate, the first heated refrigerant stream issuing from the first heat exchanger, the second heated refrigerant stream issuing from the second heat exchanger, and the third heated refrigerant stream issuing from the third heat exchanger being respectively conveyed to respectively separate compressors of the respective ones of first compression device, the second compression device and the third compression device, respectively for compressing each of the refrigerant streams separately from one another.

5. The process according to claim 1 , further comprising:
forming at least one mixed stream from at least two of the first heated refrigerant stream, the second heated refrigerant stream and the third heated refrigerant stream,
compressing each mixed stream in a compressor common to at least two of the first, second and third compression devices.

6. The process according to 1 , wherein the third refrigerant stream is substantially gaseous before being introduced into the third heat exchanger.

7. The process according to claim 1 , further comprising:
separating the compressed refrigerant stream issuing from the third compression device into a forming stream for forming the third refrigerant stream and into a gaseous cooling stream for refrigeration of the forming stream,
conveying the gaseous cooling stream to the third expansion turbine, and placing the expanded gaseous cooling stream issuing from the third expansion turbine in a heat exchange relationship with the forming stream for liquefying the forming stream,
conveying the liquefied forming stream to a hydraulic expansion turbine for forming the third refrigerant stream in substantially liquid form, and
placing the third refrigerant stream in substantially liquid form in a heat exchange relationship with the liquefied natural gas stream in the third heat exchanger.

8. Process according to claim 1 , further comprising:
dividing the precooled feed stream issuing from the first heat exchanger into a main precooled feed stream and an auxiliary expansion stream,
expanding the auxiliary expansion stream to a low pressure that is at least 5 bar below the pressure of the main precooled feed stream, and
passing the stream derived from the auxiliary expansion stream through the second heat exchanger and through the third heat exchanger in succession for delivering a stream of subcooled liquefied natural gas at low pressure.

9. The process according to claim 1 , wherein a molar nitrogen content of each of the first, second and third refrigerant streams is greater than 90%.

10. The process according to claim 1 , wherein the first refrigerant stream is based on natural gas having a molar methane content greater than 70%.

11. The process according to claim 10 , wherein the second refrigerant stream has a molar methane content greater than 90%.

12. The process according to claim 10 , wherein the first refrigerant stream has a molar carbon dioxide content greater than 5%.

13. The process according to claim 1 , wherein a pressure at an outlet of the first compression device is greater than 50 bar, and a pressure at an inlet of the first compression device is greater than 10 bar.

14. The process according to claim 1 , wherein each of the first, second and third heat exchangers contains only two fluids.

15. The process according to claim 1 , further comprising forming a second stream of compressed refrigerant at an outlet of the second compression device, cooling the second str

Assignees

• Paradowski Henri
• Vovard Sylvain
• Technip France

Inventors

• Paradowski Henri
• Vovard Sylvain

Classifications

• F25J1/0278

  Unit being stationary, e.g. on floating barge or fixed platform · CPC title

• F25J1/0263

  using different types of heat exchangers · CPC title

• F25J1/0217

  as at least a three level refrigeration cascade with at least one MCR cycle · CPC title

• F25J1/0215

  with one SCR cycle · CPC title

• F25J1/0022

  Hydrocarbons, e.g. natural gas · CPC title