Method of regenerating absorbent

• US 7,985,704 B2
• Filed: 03/07/2008
• Issued: 07/26/2011
• Est. Priority Date: 03/09/2007
• Status: Expired due to Fees

• Current Assignee: Kabushiki Kaisha Toshiba (Toshiba Corporation)
• Original Assignee: Kabushiki Kaisha Toshiba (Toshiba Corporation)
• Inventors: Kato, Masahiro, Essaki, Kenji, Muramatsu, Takehiko, Kato, Yasuhiro
• Primary Examiner(s): Johnson; Edward M
• Application Number:
  US12/044,563
• Publication Number:
  US 20080227626A1
• Time in Patent Office: 1,236 Days
• Field of Search: 502/34, 502/55, 502/56, 502/514
• US Class Current: 502/34
• CPC Class Codes: B01J 20/10 comprising silica or silicate
• CPC Class Codes: B01J 20/3433 of sorbents or filter aids other than those covered by B01J20/3408 - B01J20/3425
• CPC Class Codes: B01J 20/3483 by thermal treatment not covered by groups B01J20/3441 - B01J20/3475, e.g. by heating or cooling
• CPC Class Codes: B01J 23/755 Nickel
• CPC Class Codes: B01J 23/78 with alkali- or alkaline earth metals
• CPC Class Codes: B01J 23/94 of catalysts comprising metals, oxides or hydroxides of the iron group metals or copper
• CPC Class Codes: B01J 35/19 Catalysts containing parts with different compositions
• CPC Class Codes: C01B 2203/0233 the reforming step being a steam reforming step
• CPC Class Codes: C01B 2203/0425 In-situ adsorption process during hydrogen production
• CPC Class Codes: C01B 2203/0475 the impurity being carbon dioxide
• CPC Class Codes: C01B 2203/1011 Packed bed of catalytic structures, e.g. particles, packing elements
• CPC Class Codes: C01B 2203/1229 Ethanol
• CPC Class Codes: C01B 3/323 Catalytic reaction of gaseous or liquid organic compounds other than hydrocarbons with gasifying agents
• CPC Class Codes: C01B 3/56 by contacting with solids; Regeneration of used solids C01B3/508 takes precedence
• CPC Class Codes: Y02C 20/40 of CO2
• CPC Class Codes: Y02P 20/52 using catalysts, e.g. selective catalysts
• CPC Class Codes: Y02P 20/584 Recycling of catalysts
• CPC Class Codes: Y10S 502/514 Process applicable either to preparing or to regenerating or to rehabilitating catalyst or sorbent

Abstract

A method of regenerating an absorbent includes preparing a reactor having a gas inlet portion and a discharge portion, filling the reactor with a reforming catalyst and an absorbent for absorbing carbon dioxide, feeding the feedstock gas and the steam via the gas inlet portion to the reactor to allow a steam reforming reaction to take place, allowing the absorbent to absorb carbon dioxide generated with hydrogen at the steam reforming reaction, and releasing the carbon dioxide from the absorbent after the carbon dioxide absorption capacity of the absorbent has been degraded. In this method, the temperature in an inside of the reactor is set to 625° C. or more at the release of the carbon dioxide, and an inert gas is fed via the discharge portion to the reactor.

Claims

1. A method of regenerating an absorbent comprising:

preparing a reactor having opened opposite ends, one end of which being connected to a gas inlet portion for introducing a feedstock gas and steam and the other end being connected to a discharge portion of reforming reaction gas;

filling the reactor with a reforming catalyst and an absorbent comprising lithium silicate for absorbing carbon dioxide;

feeding the feedstock gas and the steam via the gas inlet portion to the interior of the reactor to allow a steam reforming reaction to take place;

allowing the absorbent to absorb carbon dioxide generated with hydrogen at the steam reforming reaction; and

releasing the carbon dioxide from the absorbent after the carbon dioxide absorption capacity of the absorbent is degraded;

wherein temperature in an inside of the reactor is set to 625°

C. or more at the release of the carbon dioxide, and an inert gas or a mixed inert gas containing not more than 5% by volume of carbon dioxide is employed as a treatment gas and fed via the discharge portion to the interior of the reactor in a manner that the direction of flow of the treatment gas is opposite to the feeding direction of the feedstock gas and the steam.

2. The method according to claim 1, wherein the feedstock gas and the steam are formed of vapor of aqueous ethanol solution.

3. The method according to claim 1, wherein the reforming catalyst is formed of a structure where catalytic metal fine particles are supported on a support.

4. The method according to claim 1, wherein the reforming catalyst is particles or pellets having the diameter of 2 to 10 mm.

5. The method according to claim 1, wherein the absorbent is lithium silicate.

6. The method according to claim 1, wherein the absorbent is made of a mixture of lithium silicate and an alkaline compound.

7. The method according to claim 1, wherein the absorbent is particles or pellets having the diameter of 2 to 10 mm.

8. The method according to claim 1, wherein a mixing ratio between the reforming catalyst and the absorbent is the range of 1:

1 to 1;

8 by weight.

9. The method according to claim 1, wherein the temperature in an inside of the reactor is an upper limit to 720°

C.

10. The method according to claim 1, wherein the inert gas is selected from the group consisting of nitrogen, argon and helium.

11. The method according to claim 1, wherein a couple of the reactors are juxtaposed, one of the reactors is assigned to perform the steam reforming reaction of the feedstock gas and steam, while the other is assigned to perform the regeneration of absorbent wherein carbon dioxide is released from the absorbent loaded in the other reactor.