Process for removing carbon dioxide regeneratively from gas streams

• US 5,520,894 A
• Filed: 12/23/1994
• Issued: 05/28/1996
• Est. Priority Date: 07/02/1992
• Status: Expired due to Term

• Current Assignee: Nederlandse Organisatie Voor Toegepast-Natuurwetenschappelijk Onderzoek Tno
• Original Assignee: Nederlandse Organisatie Voor Toegepast-Natuurwetenschappelijk Onderzoek Tno
• Inventors: Temmink, Herman M. G., Heesink, Albertus B. M.
• Primary Examiner(s): Straub, Gary P.
• Assistant Examiner(s): Vanoy, Timothy C.
• Application Number:
  US08/360,767
• Time in Patent Office: 522 Days
• Field of Search: 423/230, 423/437 M, 423/220, 165/104.18, 95/139, 96/123, 96/130, 96/146, 96/150, 422/223, 422/173, 422/168
• US Class Current: 423/230
• CPC Class Codes: B01D 53/12 according to the "fluidised technique"
• CPC Class Codes: B01D 53/62 Carbon oxides
• CPC Class Codes: B01J 20/041 Oxides or hydroxides
• CPC Class Codes: B01J 20/043 Carbonates or bicarbonates, e.g. limestone, dolomite, aragonite
• CPC Class Codes: B01J 20/3433 of sorbents or filter aids other than those covered by B01J20/3408 - B01J20/3425
• CPC Class Codes: B01J 20/3458 in the gas phase
• CPC Class Codes: C10K 1/20 by treating with solids; Regenerating spent purifying masses separation by adsorption B01D53/02; separation by chemical reaction B01D53/34; refining of hydrocarbon oils with acids C10G17/02, C10G27/02, C10G29/12
• CPC Class Codes: C10K 1/26 Regeneration of the purifying material contains also apparatus for the regeneration of the purifying material
• CPC Class Codes: Y02C 20/40 of CO2
• CPC Class Codes: Y02P 20/151 Reduction of greenhouse gas [GHG] emissions, e.g. CO2

Abstract

A process for removing carbon dioxide regeneratively from a hot gas stream, containing flue gases or fuel gases, wherein the gas stream is successively: a) used for heating (1) and/or desorbing (2) a solid absorbent loaded with carbon dioxide; b) optionally used for generating energy (12); c) passed through an absorber (3) in which carbon dioxide from the gas stream is absorbed on the absorbent, and: d) is discharged (11); and wherein: e) the absorbent from step c) is desorbed in ta desorber (2) at least partially and optionally under elevated pressure and is then returned to step c). A system for carrying out the process is also described. The process and the system are suitable for removing carbon dioxide from combustion gases and for shifting (coal) gasification gases toward hydrogen.

Claims

1. Process for removing carbon dioxide from a hot gas stream selected from the group consisting of fuel gas and flue gas, which comprises the following sequential steps of:

a) passing the gas stream through an absorbent-containing absorber wherein carbon dioxide from the gas stream is absorbed on the absorbent which is selected from the group consisting of CaO, MgO, CaCO₃ ·

MgO and mixtures thereof, the absorption being carried out at such a temperature that the heat resulting from the absorption is captured in a heat exchanger and can be used for generating energy,

b) discharging the gas stream from the absorber,

c) desorbing at least partially the CO₂ from the absorbent from step a) in a desorber by transferring at least a portion of the CO₂ -loaded absorbent from the desorber into a heat exchanger where the heat from the hot gas stream liberates at least a portion of the CO₂ from the CO₂ -loaded absorbent thereby regenerating the absorbent and returning the regenerated absorbent back into said desorber

d) returning the absorbent to the absorber of step a).

2. Process according to claim 1, wherein the absorbent used is CaCO₃ ·

MgO.

3. Process according to claim 1, wherein the absorption in step a) takes place at a temperature of 150°

-500°

C.

4. Process according to claim 1, wherein the desorption in step c) takes place at a temperature of 300°

-850°

C.

5. Process according to claim 1, wherein the absorption is carried out in at least two fluidized beds connected in parallel.

6. Process according to claim 1, wherein the desorption is carried out in at least two fluidized beds connected in parallel.

7. Process according to claim 1, wherein the gas stream comprises carbon monoxide which, prior to step a), is converted at least partially into carbon dioxide.

8. Process according to claim 7, wherein conversion of carbon monoxide takes place in the absorber.

9. Process according to claim 8, wherein a catalyst added to the absorbent catalyses the conversion.

10. Process according to claim 1, wherein the desorption of step c is carried out at elevated pressure.