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
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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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