Method and apparatus for separation of carbon dioxide from an off-gas from a fossil-fueled power station

Patent metadata

Field	Value
Publication number	US-9429318-B2
Application number	US-201514799898-A
Country	US
Kind code	B2
Filing date	Jul 15, 2015
Priority date	Mar 31, 2010
Publication date	Aug 30, 2016
Grant date	Aug 30, 2016

Abstract

A carbon dioxide separation process for a fossil-fueled power station process, including an absorption process and a desorption process, the carbon dioxide separation process includes when a special operating state which deviates from the normal operating state, opening a first bypass so that regenerated solvent from the desorption process is at least partially fed back again into the desorption process; and opening a second bypass so that a laden solvent from the absorption process is at least partially fed back again into the absorption process.

First claim

What is claimed is:

1. A carbon dioxide separation process for a fossil-fueled power station process, including an absorption process and a desorption process, the carbon dioxide separation process comprising:
establishing a special operating state which deviates from the normal operating state,
opening a first bypass so that regenerated solvent from the desorption process is at least partially fed back again into the desorption process; and
opening a second bypass so that a laden solvent from the absorption process is at least partially fed back again into the absorption process

wherein between 80% and 98% of the regenerated solvent from the desorption process is fed back again via the first bypass into the desorption process, and between 2% and 20% is fed to the absorption process, so that heat is introduced into the absorption process, and
wherein between 80% and 98% of the laden solvent from the absorption process is fed back again via the second bypass in to the absorption process, and between 2% and 20% is fed to the desorption process.

2. The carbon dioxide separation process as claimed in claim 1 , wherein heat is transferred from a regenerated solvent of the desorption process to a laden solvent of the absorption process.

3. The carbon dioxide separation process as claimed in claim 1 ,
wherein the regenerated solvent from the desorption process is fed back again completely via the first bypass into the desorption process,
wherein the laden solvent from the absorption process is fed back again completely via the second bypass into the absorption process, and
wherein the regenerated solvent exchanges heat with the laden solvent so that the laden solvent is heated.

4. The carbon dioxide separation process as claimed in claim 1 , wherein as a result of the special operating state an average temperature of between 30° C. and 70° C. is established in the absorber of the absorption process, and an average temperature of between 80° C. and 120° C. is established in the desorber of the desorption process.

5. The carbon dioxide separation process as claimed in claim 1 , wherein an amino-acid salt solution is used as the solvent.

6. The carbon dioxide separation process as claimed in claim 1 , wherein the flow rate of the laden solvent in the absorption process and/or of the regenerated solvent in the desorption process is reduced in the special operating state compared with the normal operating state.

7. The carbon dioxide separation process as claimed in claim 1 , wherein the special operating state is operated when the fossil-fueled power station process is completely or partially shut down.

8. A carbon dioxide separation process for a fossil-fueled power station process, including an absorption process and a desorption process, the carbon dioxide separation process comprising:
establishing a special operating state which deviates from the normal operating state,
opening a first bypass so that regenerated solvent from the desorption process is at least partially fed back again into the desorption process; and
opening a second bypass so that a laden solvent from the absorption process is at least partially fed back again into the absorption process,

wherein no cooling of the solvent which is introduced into the absorption process is carried out in the special operating state compared with the normal operating state.

Assignees

• Siemens Ag

Inventors

• Rost Mike
• Schneider Rüdiger
• Schramm Henning

Classifications

• F23J15/04 Primary

  using washing fluids {(scrubbers for removing solids only F23J15/022)} · CPC title

• Y02E20/16

  Combined cycle power plant [CCPP], or combined cycle gas turbine [CCGT] · CPC title

• F23J2219/60

  Sorption with dry devices, e.g. beds · CPC title

• B01D53/1475 Primary

  Removing carbon dioxide · CPC title

• B01D53/1425 Primary

  Regeneration of liquid absorbents · CPC title