Reclaiming apparatus and reclaiming method

Patent metadata

Field	Value
Publication number	US-9254462-B2
Application number	US-201113703211-A
Country	US
Kind code	B2
Filing date	Jul 26, 2011
Priority date	Oct 19, 2009
Publication date	Feb 9, 2016
Grant date	Feb 9, 2016

Abstract

In a reclaiming apparatus ( 106 ) that includes an airtight container ( 106 a ) as an absorbent storing unit that stores a part of an absorbent that absorbs CO 2 included in an exhaust gas and a heating unit that heats the absorbent stored in the airtight container ( 106 a ), a part of the absorbent stored in the airtight container ( 106 a ) is distributed, and a gaseous body is brought into counterflow contact with the absorbent that is distributed. As a result, since the gaseous body is brought into counterflow contact with a part of the absorbent stored in the absorbent storing unit, an absorbent component volatilizes and is separated from a degraded material, and the absorbent component can be extracted from the degraded material, whereby a loss of the absorbent can be reduced.

First claim

The invention claimed is:

1. A reclaiming system comprising:
an absorber that eliminates CO 2 or H 2 S in an exhaust gas by absorbing CO 2 or H 2 S into an absorbent;
a regenerator that releases absorbed CO 2 or H 2 S from the absorbent discharged from the absorber; and
a reclaiming apparatus that reclaims a degraded material that remains in the absorbent discharged from the regenerator, wherein
the reclaiming apparatus includes:
an absorbent storing unit that includes an airtight container to store a part of the absorbent discharged from the regenerator;
a heating unit that heats the absorbent stored in the absorbent storing unit;
an absorbent distributing unit that forms a circulation mechanism that extracts a part of the absorbent stored in the absorbent storing unit and returns the extracted part to the absorbent storing unit for distribution;
a steam supplying unit that generates steam from the absorbent that is heated by the heating unit;
an absorbent component extracting unit that is disposed in the absorbent storing unit and brings the absorbent that is returned to the absorbent storing unit in counterflow contact with the steam of the steam supplying unit; and
a dry steam supplying unit that is connected to an upper part of the airtight container and supplies dry steam having a temperature higher than a temperature to which the absorbent is heated to the absorbent storing unit, wherein the dry steam supplying unit is disposed above a liquid level of the absorbent stored in a lower part of the airtight container stored in the lower part of the airtight container,
wherein a part of the absorbent stored in the absorbent storing unit is distributed, and a gaseous body is brought into counterflow contact with the distributed absorbent.

2. The reclaiming system according to claim 1 , wherein the reclaiming apparatus further includes:
an absorbent distributing unit that extracts and distributes a part of the absorbent that is stored in the absorbent storing unit;
a steam supplying unit that supplies steam generated outside the reclaiming apparatus; and
an absorbent component extracting unit that brings the absorbent extracted by the absorbent distributing unit in counterflow contact with the steam of the steam supplying unit.

3. The reclaiming system according to claim 1 , wherein the reclaiming apparatus further includes:
an absorbent distributing unit that extracts and distributes a part of the absorbent that is stored in the absorbent storing unit;
a gas supplying unit that supplies the gas in which CO 2 or H 2 S is absorbed; and
an absorbent component extracting unit that brings the absorbent extracted by the absorbent distributing unit in counterflow contact with the gas of the gas supplying unit.

4. The reclaiming system according to claim 1 , wherein the reclaiming apparatus further includes a packed bed that brings the absorbent and the steam in gas-liquid contact with each other.

5. The reclaiming system according to claim 1 , wherein the reclaiming apparatus further includes:
a pump that extracts and raises a part of the absorbent from the absorbent storing unit; and
a nozzle that causes the absorbent pumped up by the pump to flow down against the steam that rises.

6. A reclaiming method comprising:
eliminating CO 2 or H 2 S in an exhaust gas by absorbing CO 2 or H 2 S into an absorbent;
releasing absorbed CO 2 or H 2 S from the absorbent after eliminating; and
reclaiming a degraded material that remains in the absorbent after releasing, wherein the reclaiming includes
storing a part of the absorbent;
heating the stored absorbent;
bringing a part of the stored absorbent into counterflow contact with a gaseous body while the part is distributed;
distributing the absorbent by circulating a part of the stored adsorbent solution;
bringing steam of the heated absorbent and the circulated absorbent into counterflow contact with each other;
supplying dry steam above a liquid level of the stored absorbent, and
bringing the absorbent, of which a part is circulated, in counterflow contact with the dry steam having a temperature higher than a temperature to which the absorbent is heated.

7. The reclaiming method according to claim 6 , wherein the reclaiming further includes:
extracting and distributing a part of the stored absorbent; and
bringing steam that is externally generated into counterflow contact with the extracted absorbent.

8. The reclaiming method according to claim 6 , wherein the reclaiming further includes:
extracting and distributing a part of the stored absorbent; and
bringing the gas in which CO 2 or H 2 S is absorbed in counterflow contact with the extracted absorbent.

9. The reclaiming method according to claim 6 , wherein the reclaiming further includes:
measuring an amount of an absorbent component included in the absorbent by sampling the stored absorbent; and
ending the processes in a case where the measured amount of the absorbent component arrives at a predetermined amount or less.

10. The reclaiming method according to claim 6 ,
wherein the heating of the stored absorbent includes maintaining a pressure of steam at a predetermined pressure by performing heat exchange between the absorbent and the steam in a non-contact manner.

11. The reclaiming method according to claim 10 , wherein the pressure of the steam is maintained at 2 to 3 [kg/cm 2 G].

Assignees

• Iijima Masaki
• Tatsumi Masahiko
• Yagi Yasuyuki
• Ogura Kouki
• Mitsubishi Heavy Ind Ltd
• Kansai Electric Power Co

Inventors

• Iijima Masaki
• Tatsumi Masahiko
• Yagi Yasuyuki
• Ogura Kouki

Classifications

• B01D53/1425 Primary

  Regeneration of liquid absorbents · CPC title

• B01D53/1412

  Controlling the absorption process · CPC title

• Y10S502/518

  Carbonaceous contaminant · CPC title

• B01D19/0005

  with one or more auxiliary substances · CPC title

• Y02C10/08

  Cross-Sectional Technologies · mapped topic