System and process for liquefying natural gas

Patent metadata

Field	Value
Publication number	US-9791209-B2
Application number	US-201514681255-A
Country	US
Kind code	B2
Filing date	Apr 8, 2015
Priority date	Apr 16, 2014
Publication date	Oct 17, 2017
Grant date	Oct 17, 2017

Abstract

A process of liquefying a natural gas stream in a liquefied natural gas facility is provided. The process includes cooling the natural gas stream in a first refrigeration cycle to produce a cooled natural gas stream. The process also includes cooling the cooled natural gas stream in a first chiller of a second refrigeration cycle, the cooled natural gas stream exiting the first chiller at a first pressure. The process further includes cooling the cooled natural gas stream in a first core of a second chiller of the second refrigeration cycle. The process yet further includes cooling a refrigerant of a refrigerant recycle stream separate from the cooled natural gas stream in a second core of the second chiller of the second refrigeration cycle, wherein the refrigerant recycle stream enters the second chiller at a second pressure that is lower than the first pressure of the cooled natural gas stream.

First claim

What is claimed is:

1. A process of liquefying a natural gas stream in a liquefied natural gas (LNG) facility, the process comprising:
cooling the natural gas stream in a first refrigeration cycle to produce a cooled natural gas stream;
cooling the cooled natural gas stream in a first chiller of a second refrigeration cycle, the cooled natural gas stream exiting the first chiller at a first pressure;
cooling the cooled natural gas stream in a first core of a second chiller of the second refrigeration cycle; and
cooling a refrigerant of a refrigerant recycle stream separate from the cooled natural gas stream in a second core of the second chiller of the second refrigeration cycle, wherein the refrigerant recycle stream enters the second chiller at a second pressure that is lower than the first pressure of the cooled natural gas stream; routing the cooled natural gas stream from the second refrigerant cycle to a heat exchanger for cooling therein; reducing the pressure of the cooled natural gas stream in a first expansion component disposed downstream of the heat exchanger; routing the cooled natural gas stream to a first flash drum configured to separate the cooled natural gas stream into a natural gas vapor portion and a natural gas liquid portion; routing the natural gas vapor portion to the heat exchanger for heating therein; routing the natural gas vapor portion from the heat exchanger to an inlet port of a compressor; routing the refrigerant recycle stream from the second chiller of the second refrigeration cycle to a methane recycle flash drum configured to separate the refrigerant recycle stream into a refrigerant vapor portion and a refrigerant liquid portion; routing the refrigerant liquid portion to the heat exchanger for cooling therein; reducing the pressure of the refrigerant liquid portion in a second expansion component disposed downstream of the heat exchanger; and routing the refrigerant liquid portion to a second flash drum configured to separate the refrigerant liquid portion into a refrigeration recycle vapor portion and a refrigeration recycle liquid portion.

2. The process of claim 1 , further comprising:
compressing the refrigerant in the compressor;
cooling the refrigerant downstream of the compressor;
cooling the refrigerant in the heat exchanger; and
routing the refrigerant out of the heat exchanger to produce the refrigerant recycle stream that is configured to be cooled downstream of the heat exchanger in the second core of the second chiller of the second refrigeration cycle.

3. The process of claim 2 , wherein cooling the refrigerant downstream of the compressor comprises cooling the refrigerant in a refrigerant cooler.

4. The process of claim 3 , wherein cooling the refrigerant downstream of the compressor further comprises cooling the refrigerant in the first refrigeration cycle.

5. The process of claim 2 , wherein the refrigerant comprises a methane-rich stream.

6. The process of claim 1 , further comprising routing the refrigerant vapor portion to the heat exchanger for heating therein and providing the refrigerant vapor portion to a fuel gas supply.

7. The process of claim 1 , further comprising routing the refrigerant recycle vapor portion to a nitrogen rejection unit.

8. The process of claim 7 , wherein the refrigerant recycle vapor portion is heated in the heat exchanger prior to being routed to the nitrogen rejection unit.

9. The process of claim 7 , further comprising routing a portion of the refrigerant recycle vapor portion to an inlet port of a compressor.

10. The process of claim 1 , further comprising mixing the refrigerant recycle liquid portion with the natural gas liquid portion exiting the first flash drum.

Assignees

• Conocophillips Co

Inventors

• Gandhi Satish L
• Rockwell Jim L
• Herzog Karl L
• Vogel David C

Classifications

• F25J1/0087

  Propane; Propylene · CPC title

• F25J1/0208

  in combination with an internal quasi-closed refrigeration loop, e.g. with deep flash recycle loop (F25J1/021 takes precedence) · CPC title

• F25J1/0219

  in combination with an internal quasi-closed refrigeration loop, e.g. using a deep flash recycle loop · CPC title

• F25J1/0082

  Methane · CPC title

• F25J1/0209

  as at least a three level refrigeration cascade · CPC title