Carbon dioxide separation recovery system and method

Patent metadata

Field	Value
Publication number	US-2021229032-A1
Application number	US-201917268533-A
Country	US
Kind code	A1
Filing date	Oct 29, 2019
Priority date	Oct 30, 2018
Publication date	Jul 29, 2021
Grant date	—

Abstract

A carbon dioxide separation recovery method includes: bringing a particulate carbon dioxide adsorbent and a treatment target gas containing carbon dioxide into contact with each other to make the carbon dioxide adsorbent adsorb the carbon dioxide contained in the treatment target gas; and bringing the carbon dioxide adsorbent which has adsorbed the carbon dioxide and superheated steam into contact with each other to desorb the carbon dioxide from the carbon dioxide adsorbent and thereby regenerate the carbon dioxide adsorbent, and recovering the desorbed carbon dioxide. A saturation temperature of the superheated steam which is brought into contact with the carbon dioxide adsorbent is not more than a temperature of the carbon dioxide adsorbent which contacts the superheated steam. The regenerated carbon dioxide adsorbent is utilized for adsorption of the carbon dioxide again without being subjected to a drying step.

First claim

1 . A carbon dioxide separation recovery system comprising:
an adsorption reactor into which a particulate carbon dioxide adsorbent flows; a treatment target gas supply line configured to supply a treatment target gas containing carbon dioxide to the adsorption reactor; a treated gas discharge line configured to discharge from the adsorption reactor the treatment target gas from which the carbon dioxide has been adsorbed and removed by contact with the carbon dioxide adsorbent; a desorption reactor into which the carbon dioxide adsorbent which has adsorbed the carbon dioxide in the adsorption reactor flows; a superheated steam supply line configured to supply superheated steam to the desorption reactor; a carbon dioxide recovery line configured to discharge a recovery gas from the desorption reactor, the recovery gas containing the superheated steam which has contacted the carbon dioxide adsorbent and the carbon dioxide which has been desorbed from the carbon dioxide adsorbent; and a transfer apparatus configured to transfer to the adsorption reactor the carbon dioxide adsorbent from which the carbon dioxide has been desorbed in the desorption reactor, wherein pressure of the superheated steam in the desorption reactor is predetermined pressure that is not more than saturated steam pressure at a temperature of the carbon dioxide adsorbent which contacts the superheated steam.

2 . A carbon dioxide separation recovery system comprising:
a treatment reactor filled with a particulate carbon dioxide adsorbent; a treatment target gas supply line configured to supply a treatment target gas containing carbon dioxide to the treatment reactor; a treated gas discharge line configured to discharge from the treatment reactor the treatment target gas from which the carbon dioxide has been adsorbed and removed by contact with the carbon dioxide adsorbent; a superheated steam supply line configured to supply superheated steam to the treatment reactor; a carbon dioxide recovery line configured to discharge a recovery gas from the treatment reactor, the recovery gas containing the superheated steam which has contacted the carbon dioxide adsorbent and the carbon dioxide which has been desorbed from the carbon dioxide adsorbent; and a switching apparatus configured to switch between a state where the treatment target gas supply line and the treated gas discharge line are connected to the treatment reactor and a state where the superheated steam supply line and the carbon dioxide recovery line are connected to the treatment reactor, wherein pressure of the superheated steam in the treatment reactor is predetermined pressure that is not more than saturated steam pressure at a temperature of the carbon dioxide adsorbent which contacts the superheated steam.

3 . The carbon dioxide separation recovery system according to claim 1 , wherein the carbon dioxide recovery line includes a condenser configured to condense moisture contained in the recovery gas.

4 . The carbon dioxide separation recovery system according to claim 1 , wherein:
the carbon dioxide recovery line includes
a compression pump configured to compress the recovery gas and
a carbon dioxide holder configured to store the compressed recovery gas; and
the compression pump performs forced air suction with respect to the adsorption reactor or the treatment reactor such that pressure in the adsorption reactor or the treatment reactor becomes the predetermined pressure.

5 . The carbon dioxide separation recovery system according to claim 1 , wherein a temperature of the superheated steam is higher than the temperature of the carbon dioxide adsorbent which contacts the superheated steam.

6 . A carbon dioxide separation recovery method comprising:
bringing a particulate carbon dioxide adsorbent and a treatment target gas containing carbon dioxide into contact with each other to make the carbon dioxide adsorbent adsorb the carbon dioxide contained in the treatment target gas; and bringing the carbon dioxide adsorbent which has adsorbed the carbon dioxide and superheated steam into contact with each other to desorb the carbon dioxide from the carbon dioxide adsorbent and thereby regenerate the carbon dioxide adsorbent, and recovering the desorbed carbon dioxide, wherein: a saturation temperature of the superheated steam which is brought into contact with the carbon dioxide adsorbent is not more than a temperature of the carbon dioxide adsorbent which contacts the superheated steam; and the regenerated carbon dioxide adsorbent is utilized for adsorption of the carbon dioxide again without being subjected to a drying step.

Assignees

• Research Institute Of Innovative Tech For The Earth
• Kawasaki Heavy Ind Ltd

Inventors

• Yamamoto Shin
• Yamada Hidetaka
• Yogo Katsunori
• Nishibe Shohei
• Tanaka Kazuo
• Yoshizawa Katsuhiro
• Okumura Takeshi
• Numaguchi Ryohei

Classifications

• B01D53/83

  with moving reactants · CPC title

• B01D53/96

  Regeneration, reactivation or recycling of reactants · CPC title

• B01D53/62 Primary

  Carbon oxides · CPC title

• B01D53/08

  according to the "moving bed" method · CPC title

• B01D2257/504

  Carbon dioxide · CPC title