Absorption-type removal and concentration device
An absorption type carbon dioxide removal and concentration device can remove or concentrate a carbon dioxide throughout four seasons and can be manufactured with a relatively simple structure. The device includes a carbon dioxide removal rotor that holds a carbon dioxide absorbent. The rotor is divided into at least a treatment zone and a regeneration zone. Air to be treated is ventilated through the treatment zone, so that carbon dioxide contained in the air to be treated is absorbed by a holding absorbent of the rotor portion, so that the CO 2 can be separated and removed from the air to be treated. In the regeneration zone, regeneration air is ventilated, so that the carbon dioxide absorbed by the holding absorbent in the treatment zone is desorbed with the regeneration air to regenerate the holding absorbent. A total heat exchanger recovers latent heat and sensible heat from the regeneration exhaust.
1. An absorption removal and concentration device comprising:
a carbon dioxide removal rotor that holds a carbon dioxide absorbent, the carbon dioxide removal rotor being divided into at least a treatment zone and a regeneration zone, air to be treated being ventilated through the treatment zone, so that carbon dioxide contained in the air to be treated is absorbed by the carbon dioxide absorbent, to separate carbon dioxide from the air to be treated and thereby produce supply air that is supplied to a supply destination, regeneration air being passed through the regeneration zone to desorb carbon dioxide absorbed by the carbon dioxide absorbent in the treatment zone thereby regenerating the carbon dioxide absorbent for the treatment zone, the regeneration zone producing a regeneration exhaust;
a total heat exchanger to recover a latent heat and a sensible heat from the regeneration exhaust produced in the regeneration zone, the latent heat and sensible heat recovered from the regeneration exhaust being supplied to the regeneration air; and
a humidifying device on an outlet side of the treatment zone to humidify the supply air.
2. The absorption removal and concentration device according to claim 1 , further comprising at least one of:
a cooling device to cool the air to be treated; and
a heating device to heat the regeneration air.
3. The absorption removal and concentration device according to claim 1 , wherein
the total heat exchanger is a total heat exchange rotor or a static orthogonal flow heat exchanger.
4. The absorption removal and concentration device according to claim 1 , wherein
the total heat exchanger is a total heat exchange rotor, and
the total heat exchange rotor is rotated in a winter season and intermediate seasons, and is stationary in a summer season.
5. The absorption removal and concentration device according to claim 1 , wherein
the total heat exchanger is a total heat exchange rotor,
the total heat exchanger has a preheating zone and a precooling zone,
the regeneration exhaust produced in the regeneration zone of the carbon dioxide removal rotor is passed through the precooling zone before being exhausted,
the regeneration air is passed through the preheating zone before being sent to the regeneration zone, and
the absorption removal and concentration device further comprises at least one of:
a precooling bypass path to selectively bypass the precooling zone of the total heat exchange rotor, such that when activated, the regeneration exhaust is exhausted through the precooling bypass path without passing through the precooling zone; and
a preheating bypass path to selectively bypass the preheating zone of the total heat exchange rotor, such that when activated, the regeneration air is sent to the regeneration zone through the preheating bypass path without passing through the preheating zone.
6. The absorption removal and concentration device according to claim 1 , wherein
the total heat exchanger is a total heat exchange rotor,
the total heat exchanger has a preheating zone and a precooling zone,
the regeneration exhaust produced in the regeneration zone of the carbon dioxide removal rotor is passed through the precooling zone before being exhausted,
the regeneration air is passed through the preheating zone before being sent to the regeneration zone, and
the absorption removal and concentration device further comprises:
a precooling bypass path to selectively bypass the precooling zone of the total heat exchange rotor, such that when activated, the regeneration exhaust is exhausted through the precooling bypass path without passing through the precooling zone; and
a preheating bypass path to selectively bypass the preheating zone of the total heat exchange rotor, such that when activated, the regeneration air is sent to the regeneration zone through the preheating bypass path without passing through the preheating zone.
7. The absorption removal and concentration device according to claim 1 , further comprising:
an intake port to directly take in outside air, the intake port being provided between the total heat exchanger and the carbon dioxide removal rotor so that when activated, at least a portion of the regeneration air is not supplied with latent heat and sensible heat recovered from the regeneration exhaust; and
an exhaust port to directly exhaust the regeneration exhaust to outside the device so that when activated, at least a portion of the regeneration exhaust from the regeneration zone of the carbon dioxide removal rotor is exhausted to outside without having latent heat and sensible heat recovered by the total heat exchanger.
8. The absorption removal and concentration device according to claim 1 , wherein
a treatment circulation system path is provided to return a part of air emitted from the treatment zone of the carbon dioxide removal rotor to a front of the treatment zone.
9. The absorption removal and concentration device according to claim 1 , wherein
a regeneration circulation system path is provided to return a part of air emitted from the regeneration zone of the carbon dioxide removal rotor to a front of the regeneration zone.
10. An absorption removal and concentration device comprising:
a carbon dioxide removal rotor that holds a carbon dioxide absorbent, the carbon dioxide removal rotor being divided into at least a treatment zone and a regeneration zone, air to be treated being ventilated through the treatment zone, so that carbon dioxide contained in the air to be treated is absorbed by the carbon dioxide absorbent, to separate carbon dioxide from the air to be treated and thereby produce supply air that is supplied to a supply destination, regeneration air being passed through the regeneration zone to desorb carbon dioxide absorbed by the carbon dioxide absorbent in the treatment zone thereby regenerating the carbon dioxide absorbent for the treatment zone, the regeneration zone producing a regeneration exhaust;
a total heat exchanger to recover a latent heat and a sensible heat from the regeneration exhaust produced in the regeneration zone, the latent heat and sensible heat recovered from the regeneration exhaust being supplied to the regeneration air;
a cooling device to cool the air to be treated; and
a heating device to heat the regeneration air, wherein
the cooling device is an evaporator of a heat pump, and the heating device is a condenser of the heat pump.
11. The absorption removal and concentration device according to claim 10 , wherein
the total heat exchanger is a total heat exchange rotor or a static orthogonal flow heat exchanger.
12. The absorption removal and concentration device according to claim 10 , wherein
the total heat exchanger is a total heat exchange rotor, and
the total heat exchange rotor is rotated in a winter season and intermediate seasons, and is stationary in a summer season.
13. The absorption removal and concentration device according to claim 10 , wherein
the total heat exchanger is a total heat exchange rotor,
the total heat exchanger has a preheating zone and a precooling zone,
the regeneration exhaust produced in the regeneration zone of the carbon dioxide removal rotor is passed through the precooling zone before being exhausted,
the regeneration air is passed through the preheating zone before being sent to the regeneration zone, and
the absorption removal and concentration device further comprises at least one of:
a precooling bypass path to selectively bypass the precooling zone of the total heat exchange rotor, such that when activated, the regeneration exhaust is exhausted through the precooling bypass path without passing through the precooling zone; and
a preheating bypass path to selectively bypass the preheating zone of the total heat exchange rotor, such that when activated, the regeneration air is sent to the regeneration zone through the preheating bypass path without passing through the preheating zone.
14. The absorption removal and concentration device according to claim 10 , further comprising:
an intake port to directly take in outside air, the intake port being provided between the total heat exchanger and the carbon dioxide removal rotor so that when activated, at least a portion of the regeneration air is not supplied with latent heat and sensible heat recovered from the regeneration exhaust; and
an exhaust port to directly exhaust the regeneration exhaust to outside the device so that when activated, at least a portion of the regeneration exhaust from the regeneration zone of the carbon dioxide removal rotor is exhausted to outside without having latent heat and sensible heat recovered by the total heat exchanger.
15. The absorption removal and concentration device according to claim 10 , wherein
a treatment circulation system path is provided to return a part of air emitted from the treatment zone of the carbon dioxide removal rotor to a front of the treatment zone.
16. The absorption removal and concentration device according to claim 10 , wherein
a regeneration circulation system path is provided to return a part of air emitted from the regeneration zone of the carbon dioxide removal rotor to a front of the regeneration zone.
17. An absorption removal and concentration device comprising:
a carbon dioxide removal rotor that holds a carbon dioxide absorbent, the carbon dioxide removal rotor being divided into at least a treatment zone and a regeneration zone, air to be treated being ventilated through the treatment zone, so that carbon dioxide contained in the air to be treated is absorbed by the carbon dioxide absorbent, to separate carbon dioxide from the air to be treated and thereby produce supply air that is supplied to a supply destination, regeneration air being passed through the regeneration zone to desorb carbon dioxide absorbed by the carbon dioxide absorbent in the treatment zone thereby regenerating the carbon dioxide absorbent for the treatment zone, the regeneration zone producing a regeneration exhaust; and
a total heat exchanger to recover a latent heat and a sensible heat from the regeneration exhaust produced in the regeneration zone, the latent heat and sensible heat recovered from the regeneration exhaust being supplied to the regeneration air, wherein
the total heat exchanger is a total heat exchange rotor, and
the total heat exchange rotor is rotated in a winter season and intermediate seasons, and is stationary in a summer season.
18. The absorption removal and concentration device according to claim 17 , further comprising at least one of:
a cooling device to cool the air to be treated; and
a heating device to heat the regeneration air.
19. The absorption removal and concentration device according to claim 17 , wherein
the total heat exchanger is a total heat exchange rotor,
the total heat exchanger has a preheating zone and a precooling zone,
the regeneration exhaust produced in the regeneration zone of the carbon dioxide removal rotor is passed through the precooling zone before being exhausted,
the regeneration air is passed through the preheating zone before being sent to the regeneration zone, and
the absorption removal and concentration device further comprises at least one of:
a precooling bypass path to selectively bypass the precooling zone of the total heat exchange rotor, such that when activated, the regeneration exhaust is exhausted through the precooling bypass path without passing through the precooling zone; and
a preheating bypass path to selectively bypass the preheating zone of the total heat exchange rotor, such that when activated, the regeneration air is sent to the regeneration zone through the preheating bypass path without passing through the preheating zone.
20. The absorption removal and concentration device according to claim 17 , further comprising:
an intake port to directly take in outside air, the intake port being provided between the total heat exchanger and the carbon dioxide removal rotor so that when activated, at least a portion of the regeneration air is not supplied with latent heat and sensible heat recovered from the regeneration exhaust; and
an exhaust port to directly exhaust the regeneration exhaust to outside the device so that when activated, at least a portion of the regeneration exhaust from the regeneration zone of the carbon dioxide removal rotor is exhausted to outside without having latent heat and sensible heat recovered by the total heat exchanger.
21. The absorption removal and concentration device according to claim 17 , wherein
a treatment circulation system path is provided to return a part of air emitted from the treatment zone of the carbon dioxide removal rotor to a front of the treatment zone.
22. The absorption removal and concentration device according to claim 17 , wherein
a regeneration circulation system path is provided to return a part of air emitted from the regeneration zone of the carbon dioxide removal rotor to a front of the regeneration zone.