[미국특허]
Process for the regeneration of a catalyst plant and apparatus for performing the process
원문보기
IPC분류정보
국가/구분
United States(US) Patent
등록
국제특허분류(IPC7판)
B01J-020/34
B01J-038/10
출원번호
US-0969769
(2001-10-04)
우선권정보
DE-0049040 (2000-10-04)
발명자
/ 주소
Kaefer, Gisbert
출원인 / 주소
Alstom Technology LTD
대리인 / 주소
Burns, Doane, Swecker &
인용정보
피인용 횟수 :
60인용 특허 :
5
초록▼
A gas stream containing e.g. molecular hydrogen is used for the regeneration of a catalyst for NOx and SO2 removal from the flue gas of a gas turbine. In order to reduce the consumption of regeneration gas, the gas inlet is located between the SCOSOx catalyst (2) and the SCONOx catalyst (3). The reg
A gas stream containing e.g. molecular hydrogen is used for the regeneration of a catalyst for NOx and SO2 removal from the flue gas of a gas turbine. In order to reduce the consumption of regeneration gas, the gas inlet is located between the SCOSOx catalyst (2) and the SCONOx catalyst (3). The regeneration gas leaves the catalyst chamber upstream of the SCOSOx catalyst and is recycled. For the regeneration of the SCONOx catalyst and to keep SO2 containing gas from entering the SCONOx catalyst, a second regeneration gas inlet is located downstream of the SCONOx catalyst. The regeneration gas entering the catalyst chamber through this port passes the SCONOx (3) and the SCOSOx catalyst (2). The direction of the flow in the SCONOx catalyst can also be reversed. In another example, regeneration gas outlets are located both upstream of the SCOSOx and downstream of the SCONOx catalyst. But, only the regeneration gas from the SCONOx catalyst is recycled.
대표청구항▼
1. Process for regeneration of a catalyst plant for treatment of a flue gas from a gas turbine, the catalyst plant including a SCOSOx catalyst for removal of SO2 from the flue gas, and arranged downstream thereof, a SCONOx catalyst for removal of NOx from the flue gas, in which a regenerating gas in
1. Process for regeneration of a catalyst plant for treatment of a flue gas from a gas turbine, the catalyst plant including a SCOSOx catalyst for removal of SO2 from the flue gas, and arranged downstream thereof, a SCONOx catalyst for removal of NOx from the flue gas, in which a regenerating gas including molecular hydrogen or hydrocarbons is conducted through the SCOSOx catalyst and the SCONOx catalyst, the process comprising the steps of:(a) extracting regenerating gas upstream of the SCOSOx catalyst and introducing the extracted regenerating gas between the SCOSOx catalyst and the SCONOx catalyst; and (b) introducing fresh regenerating gas downstream of the SCONOx catalyst and extracting the introduced fresh regenerating gas upstream of the SCOSOx catalyst, wherein step (a) and step (b) are performed simultaneously. 2. Process according to claim 1, comprising the step of adding molecular hydrogen or hydrocarbons to the extracted regenerating gas prior to the step of introducing the extracted regenerating gas.3. Process according to claim 1, comprising the step of expelling the flue gas from the catalyst plant with a substantially oxygen-free cleaning gas before the step of extracting the regenerating gas.4. Process for regeneration of a catalyst plant for treatment of a flue gas from a gas turbine, the catalyst plant including a SCOSOx catalyst for removal of SO2 from the flue gas, and arranged downstream thereof, a SCONOx catalyst for removal of NOx from the flue gas, in which a regenerating gas including molecular hydrogen or hydrocarbons is conducted through the SCOSOx catalyst and the SCONOx catalyst, the process comprising the steps of:(a) extracting regenerating gas downstream of the SCONOx catalyst and introducing the extracted regenerating gas between the SCOSOx catalyst and the SCONOx catalyst; and (b) introducing fresh regeneration gas between the SCOSOx catalyst and the SCONOx catalyst and extracting the fresh regenerating gas upstream of the SCOSOx catalyst, wherein step (a) and step (b) are performed simultaneously. 5. Process according to claim 4, comprising the step of adding molecular hydrogen or hydrocarbons to the extracted regenerating gas prior to the step of introducing the extracted regenerating gas.6. Process according to claim 4, comprising the step of expelling the flue gas from the catalyst plant with a substantially oxygen-free cleaning gas before the step of extracting the regenerating gas.7. Process for regeneration of a catalyst plant for treatment of a flue gas from a gas turbine, the catalyst plant including a SCOSOx catalyst for removal of SO2 from the flue gas, and arranged downstream thereof, a SCONOx catalyst for removal of NOx from the flue gas, in which a regenerating gas including molecular hydrogen or hydrocarbons is conducted through the SCOSOx catalyst and the SCONOx catalyst, the process comprising the steps of:(a) extracting regenerating gas between the SCOSOx catalyst and the SCONOx catalyst and introducing the extracted regenerating gas upstream of the SCOSOx catalyst; and (b) introducing fresh regenerating gas downstream of the SCONOx catalyst and extracting the introduced fresh regenerating gas between the SCOSOx catalyst and the SCOSOx catalyst during the step of introducing the extracted regenerating gas wherein step (a) and step (b) are performed simultaneously. 8. Process according to claim 7, comprising the step of adding molecular hydrogen or hydrocarbons to the extracted regenerating gas prior to the step of introducing the extracted regenerating gas.9. Process according to claim 7, comprising the step of expelling the flue gas from the catalyst plant with a substantially oxygen-free cleaning gas before the step of extracting the regenerating gas.10. Process for regeneration of a catalyst plant for treatment of a flue gas from a gas turbine, the catalyst plant including a SCOSOx catalyst for removal of SO2 from the flue gas, and arranged downstream thereof, a SCONOx catalyst for removal of NOx from the flue gas, in which a regenerating gas including molecular hydrogen or hydrocarbons is conducted through the SCOSOx catalyst and the SCONOx catalyst, the process comprising:maintaining a recirculating flow of the regenerating gas through a first catalyst; maintaining a linear flow of the regenerating gas through a second catalyst; and controlling the recirculating flow and the linear flow to substantially prevent the regenerating gas that has passed through the SCOSOx catalyst from passing through the SCONOx catalyst, wherein when the first catalyst is the SCOSOx catalyst, the second catalyst is the SCONOx catalyst, and when the first catalyst is the SCONOx catalyst, the second catalyst is the SCOSOx catalyst.
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