Looking for breakthrough ideas for innovation challenges? Try Patsnap Eureka!

Cascade type natural gas pressurized liquefaction process with sublimation removal of CO2

A technology of natural gas and CO2, which is applied in liquefaction, refrigeration, liquefaction, solidification, etc., can solve the problems that are not involved in natural gas liquefaction process, cannot guarantee that natural gas will not precipitate, and are difficult to popularize and apply, so as to save equipment investment and reduce floor space , the effect of energy consumption reduction

Inactive Publication Date: 2012-08-01
SHANGHAI JIAO TONG UNIV
View PDF9 Cites 9 Cited by
  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

However, the material of the cooler in this patent needs to be one of metal oxide, ceramics, single crystal or sapphire, which is too special and expensive to be popularized and applied; and the solid phase as the core of the patent is in the center of the container rather than on the wall Formed technology, it is difficult to realize in engineering practice
The patent number is 5819555, and the title is "Removal of CO from feed stream through gas-solid separation 2 A method” of the U.S. Patent, which proposes the related desublimation to remove CO 2 technology, but it does not involve the natural gas liquefaction process, and cannot guarantee that the natural gas will not precipitate solid CO in the subsequent liquefaction process 2

Method used

the structure of the environmentally friendly knitted fabric provided by the present invention; figure 2 Flow chart of the yarn wrapping machine for environmentally friendly knitted fabrics and storage devices; image 3 Is the parameter map of the yarn covering machine
View more

Image

Smart Image Click on the blue labels to locate them in the text.
Viewing Examples
Smart Image
  • Cascade type natural gas pressurized liquefaction process with sublimation removal of CO2
  • Cascade type natural gas pressurized liquefaction process with sublimation removal of CO2

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0033] A CO removal with desublimation 2 The cascaded natural gas liquefaction process under pressure, the implementation scheme is as follows figure 1 shown. Propane is used as a high-temperature refrigerant with a flow rate of 0.772kmol / h; ethylene is used as a low-temperature refrigerant with a flow rate of 0.884kmol / h; the molar composition of raw natural gas is 0.5% CO 2 +99.5%CH 4 , pressure 1.5MPa, temperature 35°C, flow rate 1kmol / h, CO removal with desublimation 2 The specific steps of the cascaded natural gas liquefaction process under pressure are as follows:

[0034] 1. Since the raw natural gas is within the pressure range of 1.4-1.6MPa, the pressure regulating device 1 is omitted. The raw material gas is introduced into the precooler 2, absorbs cooling energy from the refrigerant propane and ethylene, flows out of the precooler 2, and the temperature drops to -37°C;

[0035] 2. The natural gas pre-cooled in step 1 is introduced into the crystallizer 3, and t...

Embodiment 2

[0042] A CO removal with desublimation 2 The cascaded natural gas liquefaction process with pressure, in the process of natural gas liquefaction, desublimation removes CO 2 , and then produce LNG products under pressure, and the innovative design of the process cancels the CO 2 Pretreatment device, and ensure no CO in the subsequent liquefaction process 2 Crystal precipitation; at the same time, a two-stage cascade refrigeration system is used to provide cooling capacity for the natural gas liquefaction process. Compared with the traditional three-stage cascade refrigeration cycle, the primary refrigeration system is omitted, which simplifies the process and reduces equipment investment.

[0043] Propane is used as a high-temperature refrigerant with a flow rate of 0.844 kmol / h; ethylene is used as a low-temperature refrigerant with a flow rate of 1.012 kmol / h; the molar composition of raw natural gas is 10% CO 2 +90%CH 4 , pressure 1.5MPa, temperature 35°C, flow rate 1kmol...

Embodiment 3

[0052] A CO removal with desublimation 2 The cascaded natural gas liquefaction process with pressure, in the process of natural gas liquefaction, desublimation removes CO 2 , and then produce LNG products under pressure, and the innovative design of the process cancels the CO 2 Pretreatment device, and ensure no CO in the subsequent liquefaction process 2 Crystal precipitation; at the same time, a two-stage cascade refrigeration system is used to provide cooling capacity for the natural gas liquefaction process. Compared with the traditional three-stage cascade refrigeration cycle, the primary refrigeration system is omitted, which simplifies the process and reduces equipment investment.

[0053] Propane is used as a high-temperature refrigerant with a flow rate of 1.054 kmol / h; ethylene is used as a low-temperature refrigerant with a flow rate of 1.141 kmol / h; the molar composition of raw natural gas is 30% CO 2 +70%CH 4 , pressure 1.5MPa, temperature 35°C, flow rate 1kmol...

the structure of the environmentally friendly knitted fabric provided by the present invention; figure 2 Flow chart of the yarn wrapping machine for environmentally friendly knitted fabrics and storage devices; image 3 Is the parameter map of the yarn covering machine
Login to View More

PUM

No PUM Login to View More

Abstract

The invention relates to a cascade type natural gas pressurized liquefaction process with sublimation removal of CO2. Natural gas is kept at a gas state and precooled in a precooler, and is fed into a crystallizer and kept on cooling, so that solid dry ice can be separated out by sublimation and the CO2 content is reduced to 0.5%; and then, natural gas is fed into a cryogenic compressor for pressurization, fed into a liquefier for liquefaction under a high pressure, and fed into a storage tank for storage. The cold quantity required by a liquefaction process is provided by an independent two-stage cascade refrigerating cycle. Compared with the prior art, the process provided by the utility model not only dispenses with CO2 pretreatment equipment which occupies a large area in the conventional natural gas liquefaction process, but also simplifies the traditional three-stage cascade refrigerating cycle to two-stage refrigerating cycle, so as to greatly reduce the cost of investment for natural gas liquefaction on an offshore platform which has high manufacturing cost. Meanwhile, the natural gas liquefaction at a high temperature also reduces the energy consumption of the refrigerating cycle.

Description

technical field [0001] The invention relates to a purification and liquefaction process of natural gas, which is a liquefaction process for removing carbon dioxide at low temperature in the natural gas liquefaction process, in particular a liquefaction process for desublimation and removal of carbon dioxide in the cascade natural gas liquefaction process under pressure. It belongs to the field of chemical industry and low temperature technology. Background technique [0002] Exploration practice has proved that there are abundant oil and gas resources in many sedimentary basins in China's sea area, and the proven offshore natural gas reserves are about 1 / 3 of the national natural gas reserves. The development and utilization of offshore natural gas can not only provide a clean energy with high calorific value, but also reduce the dependence on oil resources, which has important environmental protection and energy strategic security significance. In order to facilitate the t...

Claims

the structure of the environmentally friendly knitted fabric provided by the present invention; figure 2 Flow chart of the yarn wrapping machine for environmentally friendly knitted fabrics and storage devices; image 3 Is the parameter map of the yarn covering machine
Login to View More

Application Information

Patent Timeline
no application Login to View More
Patent Type & Authority Applications(China)
IPC IPC(8): F25J3/08F25J1/02
CPCF25J1/0022F25J1/0052F25J1/0085F25J1/0087F25J1/0205F25J1/0254F25J2205/20F25J2220/66F25J2230/08F25J2230/30
Inventor 林文胜熊晓俊
Owner SHANGHAI JIAO TONG UNIV
Who we serve
  • R&D Engineer
  • R&D Manager
  • IP Professional
Why Patsnap Eureka
  • Industry Leading Data Capabilities
  • Powerful AI technology
  • Patent DNA Extraction
Social media
Patsnap Eureka Blog
Learn More
PatSnap group products