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Method for producing liquefied natural gas by multi-component refrigerant double-stage compression

A technology for liquefied natural gas and refrigerants, applied in refrigeration and liquefaction, liquefaction, solidification, etc., can solve the problems of complex process, low unit energy consumption, and many equipment, and achieve the advantages of simple liquefaction process, wide application range, and high liquefaction efficiency Effect

Inactive Publication Date: 2013-03-06
李志远
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

Therefore, the disadvantages of the cascade liquefaction process are: many equipments, complex process, difficult control, poor operation flexibility, high initial investment cost, but its unit energy consumption is low
This process is simple and the number of equipment is small, but when the production scale reaches a large scale, the selection, manufacture and operation of the compressor will be very difficult
When using domestic compressors, this process can only be produced on a small scale, which is not conducive to the localization of this natural gas liquefaction process

Method used

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  • Method for producing liquefied natural gas by multi-component refrigerant double-stage compression

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Embodiment Construction

[0022] The present invention will be further described below in conjunction with specific implementation examples, but the present invention is not limited only to the examples described below.

[0023] figure 1 In the shown embodiment, the device used in the method of producing liquefied natural gas by two-stage compression of multi-component refrigerant includes a separation tank V-3, a pre-cooling compressor C-1, a cooler E-1, a buffer tank V- 5. Throttle valve J-1, separation tank V-1, separation tank V-4, cryogenic compressor C-2, cooler E-2, throttle valve J-2, separation tank V-2, separation tank VH, throttle valve J-3, cold box HEX-1.

[0024] The pretreated natural gas (or gas field gas, coal bed methane and gas rich in methane) of about 4.0MPaG enters the cold box HEX-1, and after heat exchange with the precooling refrigerant and cryogenic refrigerant, the temperature reaches about -60°C to become The gas-liquid is mixed, and then it goes out of the cold box HEX-1 ...

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Abstract

Provided is a method for producing liquefied natural gas by multi-component refrigerant two-stage compression. The method includes two multi-component refrigerant compression cycles, the refrigerant in a first cycle is called a pre-cooling refrigerant, the refrigerant in a second cycle is called a cryogenic refrigerant; the pre-cooling refrigerant returns to an ice chest after passing through a pre-cooling compressor, a cooler, a buffer tank, the ice chest, a throttle valve and a gas-liquid separation tank, and then returns to the pre-cooling compressor; the cryogenic refrigerant returns to the ice chest after passing through a cryogenic compressor, the cooler, the ice chest, the throttle valve and the gas-liquid separation tank, and then returns to the cryogenic compressor; and natural gas is cooled after heat transfer of the ice chest and the refrigerants and finally becomes the liquefied natural gas. The natural gas is liquefied by two independent multi-component refrigerant compression cycles, and composition and content of the two multi-component refrigerants are different, so that the method is wide in application range to raw material natural gas, high in operation flexibility and high in liquefying efficiency. Besides, the method is simple in liquefying process, low in investment cost, and is applicable to liquefied natural gas factories in various scales.

Description

technical field [0001] The invention relates to a method for producing liquefied natural gas, more specifically, the invention relates to a method for producing liquefied natural gas by using natural gas, coal bed methane or other methane-rich gases as raw materials. Background technique [0002] Natural gas is a clean, efficient and safe energy. In recent years, it has been paid more and more attention by various countries, and the trade volume of natural gas in the world has also increased rapidly. However, for cross-sea trade and remote distance transportation, it is neither economical nor convenient to transport gaseous natural gas. The raw material gas containing natural gas, such as: gas field gas, coal bed methane, methane-rich gas, etc., after deacidification, dehydration, mercury removal, heavy hydrocarbon removal, etc., is liquefied at low temperature to become liquefied natural gas. Natural gas is nearly 600 times smaller, which is convenient for storage and tran...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): F25J1/02
Inventor 不公告发明人
Owner 李志远
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