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Device and method for separating gases to be separated

A technology for separating gas and separating device, applied in the field of separating device, can solve the problem of high operating cost

Inactive Publication Date: 2012-05-09
MITSUI ENG & SHIPBUILD CO LTD
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

[0005] However, when generating CO 2 In the case of gas hydrates such as hydrates, processes such as pressurization and cooling are required, and in the case of decomposing (regasifying) gas hydrates in order to utilize the separated gas, due to the relatively low temperature Energy is required to raise the temperature, so the running cost tends to be relatively high

Method used

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  • Device and method for separating gases to be separated
  • Device and method for separating gases to be separated
  • Device and method for separating gases to be separated

Examples

Experimental program
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Effect test

Embodiment 1

[0052] The separation device 1 of the gas to be separated in this embodiment is provided with: a gas hydrate generating unit 2 for separating the gas G 0 A gas contained in the gas hydrate is hydrated to form a gas hydrate slurry; the dehydration unit 3 dehydrates the gas hydrate slurry; the gas hydrate decomposition unit 4 decomposes the dehydrated gas hydrate and regenerates it. gasification.

[0053] On the upstream side of the above-mentioned gas hydrate generating part 2, it is provided that the separated gas G 0 A compression device 5 such as a centrifugal compressor and a gas cooler 6 for hydrating the above-mentioned one gas at a predetermined pressure and temperature.

[0054] In addition, separated gas G such as combustion exhaust gas and production gas 0 It is usually at a high temperature of about 40°C to about 200°C, and contains a small amount of water (steam), oil, ash, dust and other discharges9. Therefore, take the following composition: in the gas G to be ...

Embodiment 2

[0072] according to figure 2 Another embodiment of the separation device of the gas to be separated according to the present invention will be described.

[0073] In the separation device 21 of the gas to be separated according to the present embodiment, the same members as in the first embodiment are given the same reference numerals, and their descriptions are omitted. In addition, as in Example 1, for the separated gas G 0 carbon dioxide (CO 2 ) is hydrated and separated.

[0074] In the above-mentioned gas hydrate generating part 2, CO is generated 2 Gas remaining after gas hydrate (unhydrated gas G 1 ) in the CO 2 Gas hydrate formation conditions, that is, a high pressure of 5 to 20 MPa, are discharged from the gas hydrate formation part 2 .

[0075] The separation device 21 of the separated gas of the present embodiment is constituted as follows: a power recovery unit 22 such as a known gas expander (axial flow turbine) is installed on the power shaft of the above...

Embodiment 3

[0078] according to image 3 Another embodiment of the separation device of the gas to be separated according to the present invention will be described.

[0079] In the separation device 31 of the gas to be separated according to this embodiment, the same members as those in Embodiments 1 and 2 are given the same reference numerals, and description thereof will be omitted. In addition, the same as in Example 1, for the gas G to be separated 0 carbon dioxide (CO 2 ) is hydrated and separated.

[0080] As shown in the description of Example 2, the high-pressure gas G discharged from the above-mentioned gas hydrate generating part 2 1 It is input to the power recovery part 22 provided in the above-mentioned compression device 5, returns to atmospheric pressure, and recovers the pressure energy. Here, the above-mentioned high-pressure gas G 1 At atmospheric pressure, cold energy is generated due to the expansion of the gas. The separator 31 of the gas to be separated accord...

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Abstract

A device and method for separating gases to be separated are provided with which the energy consumption for separating a certain gas, e.g., CO2, from gases to be separated, e.g., a combustion waste gas or process gas, can be reduced to attain a reduction in device operation cost. The device for separating gases to be separated is equipped with a gas hydrate formation section in which a gas contained in the gases to be separated, which are a mixture of a plurality of gas components, is hydrated to form a gas hydrate slurry, a dehydration section in which the gas hydrate slurry is dehydrated, and a gas hydrate decomposition section in which the gas hydrate obtained by the dehydration is decomposed to gasify the hydrate again, and is characterized in that the device has been configured so that the water removed from the gas hydrate slurry in the dehydration section is mixed with the water resulting from decomposition of the gas hydrate in the gas hydrate decomposition section and the resultant circulating water is introduced into the gas hydrate formation section.

Description

technical field [0001] The present invention relates to a separation device and method for separating certain gases contained in gases to be separated such as combustion waste gas and production gas. Background technique [0002] As a certain gas contained in the combustion waste gas and production gas of coal-fired thermal power generation and integrated gasification combined cycle power generation systems (IGCC), steel plants, cement plants, etc., such as carbon dioxide (CO 2 ) separation technology, the implementation of chemical absorption method, PSA method (physical adsorption method), membrane separation method, physical absorption method, oxygen combustion method, etc. [0003] The reagents used in the chemical absorption method and the physical absorption method are expensive, and the above-mentioned chemicals are highly toxic, and the leakage of the chemicals will cause a problem of environmental pollution. In the PSA method (physical adsorption method) and membra...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01D53/14B01D53/62C01B31/20C01B32/50
CPCB01D2257/504B01D2252/103Y02C10/04Y02C10/06B01D53/62B01D53/1475B01D2258/0283B01D53/78Y02C20/40
Inventor 宫川满松尾和芳樱井聪一郎酒井正和木户口晃
Owner MITSUI ENG & SHIPBUILD CO LTD
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