A CO 2 recovery system includes an absorption tower that brings gas containing CO 2 into contact with a CO 2 absorption solution to remove CO 2 from the CO 2 -containing gas; a regeneration tower that regenerates a CO 2 -absorbed rich solution; and a compression device that re-uses a lean solution, from which CO 2 has been removed in the regeneration tower, in the absorption tower and compresses CO 2 in gas emitted from the regeneration tower, wherein the rich solution has a high pressure, the high-pressure rich solution is subjected to gas-liquid separation by a flash drum, the rich solution as a liquid component separated in the flash drum is introduced into the regeneration tower, and high-pressure CO 2 gas as a gas component separated in the flash drum is introduced into a compression device having a predetermined compression pressure.
1. A CO 2 recovery system comprising:
an absorption tower that brings gas containing CO 2 into contact with a CO 2 absorption solution to generate a rich solution which is the CO 2 absorption solution absorbing CO 2 by removing CO 2 from the CO 2 -containing gas;
a booster unit that is provided at a downstream side of the absorption tower in a flow of the rich solution and pressurizes the rich solution from the absorption tower;
a flash drum that is provided at a downstream side of the booster unit in a flow of the rich solution and partially flashes the rich solution pressurized by the booster unit to separate into CO 2 and a rich absorption solution,
a pressure reducing valve that is provided at a downstream side of the flash drum in a flow of the rich absorption solution and decreases a pressure of the rich absorption solution from the flash drum,
a regeneration tower that is provided at a downstream side of the pressure reducing valve in a flow of the rich absorption solution and heats the rich absorption solution of which pressure is decreased, by a reboiler using a provided steam and regenerates the rich absorption solution by emitting a CO 2 , which pressure is lower than the pressure of the CO 2 separated by the flash drum, by the generated steam, and
a compression device, into which the CO 2 emitted from the drum and the regeneration tower is introduced, that compresses the CO 2 emitted from the regeneration tower, wherein
the booster unit is provided between the absorption tower and the flash drum in the flow of the rich solution, and the pressure reducing valve is provided between the flash drum and the regeneration tower in the flow of the rich absorption solution, and
the compression device includes:
a first compressor into which the CO 2 emitted by the regeneration tower is introduced, and configured to compress the introduced CO 2 ; and
a second compressor into which the CO 2 emitted from the flash drum and the CO 2 compressed by the first compressor are introduced, and configured to compress the introduced CO 2 with higher pressure than the first compressor.
2. The CO 2 recovery system according to claim 1 ,
wherein
an assist pressure reducing valve and an assist flash drum are provided between the flash drum and the regeneration tower, and
the compression device includes a third compressor,
wherein
the assist pressure reducing valve decreases a pressure of the rich absorption solution from the flash drum,
the assist flash drum partially flashes the rich absorption solution of which pressure is decreased by the assist pressure reducing valve to separate a CO 2 , which pressure is lower than the pressure of the CO 2 from the flash drum and higher than the pressure of the CO 2 from the regeneration tower, and the rich absorption solution,
the pressure reducing valve decreases the pressure of the rich absorption solution from the assist flash drum,
the third compressor into which the CO 2 emitted by the assist flash drum and the CO 2 compressed by the first compressor are introduced, and is configured to compress the introduced CO 2 with higher pressure than the first and with lower pressure than the second compressor, and
the second compressor into which the CO 2 emitted from the flash drum and the CO 2 compressed by the third compressor are introduced, and configured to compress the introduced CO 2 .
3. The CO 2 recovery system according to claim 2 ,
wherein a heat exchanger which heats the rich solution is provided between the absorption tower and the flash drum.
4. The CO 2 recovery system according to claim 2 ,
wherein an inert gas separator, which separates inert gas, and an inert gas introduction line, which introduces the separated inert gas into the absorption tower, are provided between the absorption tower and the flash drum.
5. The CO 2 recovery system according to claim 1 ,
wherein when the gas introduced into the absorption tower is normal-pressure gas which is near atmospheric pressure, a normal-pressure absorption tower is used as the absorption tower,
a booster pump that pressurizes the rich solution emitted from the normal-pressure absorption tower is provided, and
the pressurized rich solution is subjected to gas-liquid separation by a gas-liquid separator.
6. The CO 2 recovery system according to claim 1 ,
wherein when the gas introduced into the absorption tower is high-pressure gas which pressure is higher than an atmospheric pressure in certain value, a pressurization absorption tower is used as the absorption tower, and
the pressurized rich solution emitted from the pressurization absorption tower is subjected to gas-liquid separation by a gas-liquid separator.
7. The CO 2 recovery system according to claim 1 , wherein
the booster unit pressurizes the rich solution at higher pressure than a compression pressure of the second compressor.