CO2 capture system by chemical absorption
a capture system and chemical absorption technology, applied in liquid degasification, separation processes, dispersed particle separation, etc., can solve the problems of not being able to propose specific techniques to reduce energy and reduce and reuse waste heat, and achieve the effects of reducing cooling exhaust heat, increasing energy efficiency of the system, and reducing recovery energy inpu
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embodiment 1
[0027]A first embodiment of the CO2 capture system by chemical absorption according to the present invention will be described with reference to FIG. 1. In FIG. 1, an example will be described in which the outlet gas heat of the regenerator of the CO2 capture system by chemical absorption is recovered and reused for an inlet rich solvent of the regenerator.
[0028]FIG. 1 shows the system configuration of the regenerator and peripheral devices of the CO2 capture system by chemical absorption according to the first embodiment of the present invention.
[0029]The CO2 capture system by chemical absorption according to this embodiment comprises an absorber 1 for removing CO2 contained in exhaust gas by absorbing CO2 by a solvent, and a regenerator 2 for separating CO2 from the solvent that has absorbed CO2 and regenerating the solvent, wherein the solvent is circulated between the absorber 1 and the regenerator 2.
[0030]To explain the CO2 capture system by chemical absorption according to thi...
embodiment 2
[0051]Next, a second embodiment of the CO2 capture system by chemical absorption according to the present invention will be described with reference to FIG. 2.
[0052]Basic configuration of the CO2 capture system by chemical absorption according to this embodiment shown in FIG. 2 is the same as that of the CO2 capture system by chemical absorption according to the first embodiment shown in FIG. 1. Therefore, description of the configuration common to both systems is omitted and only different parts will be described below.
[0053]FIG. 2 shows an example of the CO2 capture system by chemical absorption that combines the configuration of the CO2 capture system by chemical absorption according to the first embodiment with the VR technique.
[0054]In the CO2 capture system by chemical absorption shown in FIG. 2, the rich solvent 5 that has absorbed CO2 contained in the exhaust gas in the absorber 1 is heated, through the liquid heat exchanger 12 installed along the path of the rich solvent su...
embodiment 3
[0070]Next, a third embodiment of the CO2 capture system by chemical absorption according to the present invention will be described with reference to FIG. 4.
[0071]Basic configuration of the CO2 capture system by chemical absorption according to this embodiment shown in FIG. 4 is the same as that of the CO2 capture system by chemical absorption according to the first embodiment shown in FIG. 1. Therefore, description of the configuration common to both systems is omitted and only different parts will be described below.
[0072]FIG. 4 shows an example of the CO2 capture system by chemical absorption that combines the configuration of the CO2 capture system by chemical absorption according to the first embodiment with the decompression operating method of the reboiler.
[0073]In the CO2 capture system by chemical absorption shown in FIG. 4, pressure of the reboiler 7 is decompressed to become lower than the pressure, 0.15 to 0.2 MPa, of the regenerator and operated. The lean solvent 8 fro...
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Abstract
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