Carbon dioxide separation apparatus
There is provided a moving bed type CO2 separation apparatus that is capable of achieving steady recovery of CO2, and that is energy-efficient. An adsorbent hopper that supplies a CO2 adsorbent of a moving bed to an adsorption tower that adsorbs CO2 from a treatment-target gas is provided. Below the adsorption tower, a moving bed-type regeneration tower for regenerating the CO2 adsorbent having adsorbed CO and a moving bed-type drying tower that dries the regenerated CO2 adsorbent are provided. Desorption-purpose steam generated from the drying tower is supplied to the regeneration tower. By allowing the desorption-purpose steam to be condensed on the CO2 adsorbent, CO2 is desorbed from the CO2 adsorbent. Thus, CO2 adsorbent forming a moving bed is used in a circulating manner through the CO2 separation apparatus, and the energy used for drying the condensed water contained in the CO2 adsorbent is used for desorbing CO2.
1. A carbon dioxide separation apparatus that separates carbon dioxide from a treatment-target gas containing carbon dioxide using a carbon dioxide adsorbent and that regenerates the carbon dioxide adsorbent having adsorbed the carbon dioxide, the carbon dioxide separation apparatus comprising:
a moving bed-type adsorption tower in which carbon dioxide is adsorbed from the treatment-target gas by the carbon dioxide adsorbent, the adsorption tower discharging the treatment-target gas having undergone adsorption, the adsorption tower discharging the carbon dioxide adsorbent having adsorbed the carbon dioxide;
a moving bed-type regeneration tower that receives the carbon dioxide adsorbent having adsorbed the carbon dioxide and discharged from the adsorption tower, the regeneration tower allowing desorption-purpose steam to be condensed on the carbon dioxide adsorbent such that the carbon dioxide is desorbed from the carbon dioxide adsorbent, the regeneration tower thereafter discharging the carbon dioxide adsorbent;
a moving bed-type drying tower that receives the carbon dioxide adsorbent discharged from the regeneration tower, the drying tower heating the carbon dioxide adsorbent such that condensed water contained in the carbon dioxide adsorbent is vaporized as steam and such that the carbon dioxide adsorbent is dried, the drying tower thereafter discharging the dried carbon dioxide adsorbent; and
a conveying mechanism that conveys the dried carbon dioxide adsorbent discharged from the drying tower to the adsorption tower, wherein
the steam generated by the heating in the drying tower from the condensed water contained in the carbon dioxide adsorbent is used as the desorption-purpose steam in the regeneration tower such that water is used in a circulating manner through the regeneration tower and the drying tower.
2. The carbon dioxide separation apparatus according to claim 1 , wherein
the drying of the condensed water contained in the carbon dioxide adsorbent in the drying tower is carried out by indirect heating, and
the steam generated from the condensed water is entirely used as the desorption-purpose steam.
3. The carbon dioxide separation apparatus according to claim 1 , wherein
the drying of the condensed water contained in the carbon dioxide adsorbent in the drying tower is carried out using superheated steam, and
mixed steam made up of the steam generated from the condensed water and steam derived from the superheated steam is partially used as the desorption-purpose steam.
4. The carbon dioxide separation apparatus according to claim 3 , further comprising:
an indirect heating device that again supplies superheated steam obtained by heating the mixed steam as the superheated steam in the drying tower; and
a circulating pump that allows the mixed steam and the superheated steam to circulate.
5. The carbon dioxide separation apparatus according to claim 1 , further comprising a recovery mechanism that recovers the carbon dioxide having been desorbed and discharged from the regeneration tower.
6. The carbon dioxide separation apparatus according to claim 1 , wherein the regeneration tower and the drying tower are integrally structured.
7. The carbon dioxide separation apparatus according to claim 1 , further comprising a gas stream leakage preventing mechanism that is provided immediately upstream from the regeneration tower and/or immediately downstream from the drying tower.
8. The carbon dioxide separation apparatus according to claim 1 , further comprising a cooling tower for cooling the carbon dioxide adsorbent discharged from the drying tower.