公开(公告)号：EP2358460A4

公开(公告)日：2013-10-02

申请号：EP09824193

申请日：2009-10-30

申请人： EMERACHEM LLC

发明人： GIRDLESTONE THOMAS ,  DE CICCO STEVEN ,  EPLING WILLIAM S ,  COLE JERALD A ,  WAGNER GREGORY J

IPC分类号： B01D50/00 ,  B01D53/86 ,  B01D53/94 ,  F01N3/28 ,  F01N11/00

CPC分类号： B01J37/038 ,  B01D53/864 ,  B01D53/8696 ,  B01D53/944 ,  B01D53/9495 ,  B01D53/96 ,  B01D2257/302 ,  B01D2257/404 ,  B01D2257/702 ,  B01D2257/708 ,  B01D2258/01 ,  B01D2258/0283 ,  B01J20/043 ,  B01J23/38 ,  B01J35/04 ,  B01J37/0215 ,  F01N3/0807 ,  F01N3/0814 ,  F01N3/0842 ,  F01N2610/06 ,  Y10S55/30

公开(公告)号：EP1251936A4

公开(公告)日：2003-03-05

申请号：EP00905583

申请日：2000-01-11

申请人： EMERACHEM LLC

发明人： CAMPBELL LARRY E ,  EPLING WILLIAM SHELBOURNE JR ,  PARKS JAMES EDGAR II ,  WAGNER GREGORY J

IPC分类号： B01D53/86 ,  B01D53/94 ,  B01J23/58 ,  B01J23/78 ,  B01J23/89 ,  B01J35/00 ,  F01N3/023 ,  F01N3/08 ,  F01N3/20 ,  F01N13/02 ,  F01N13/04 ,  B01D53/96 ,  B01J23/96 ,  B01J38/10

CPC分类号： F01N3/2066 ,  B01D53/8609 ,  B01D53/8612 ,  B01D53/8628 ,  B01D53/8631 ,  B01D53/9422 ,  B01D53/9431 ,  B01D2255/1021 ,  B01D2255/2027 ,  B01D2255/20738 ,  B01D2255/20746 ,  B01D2255/20753 ,  B01D2255/20761 ,  B01D2255/20769 ,  B01J23/58 ,  B01J23/78 ,  B01J23/8946 ,  B01J35/0006 ,  F01N3/0233 ,  F01N3/0814 ,  F01N3/0842 ,  F01N3/085 ,  F01N3/0878 ,  F01N3/0885 ,  F01N3/2093 ,  F01N13/009 ,  F01N13/0097 ,  F01N13/011 ,  F01N2570/04 ,  F01N2570/14 ,  F01N2610/03 ,  Y02A50/2325 ,  Y02A50/2344 ,  Y02T10/24

摘要： The process contacts a gaseous stream (1) containing gaseous sulfur compounds and NOx with a catalyst system of either: an oxidation catalyst disposed on a high surface area support or an absorber material; or of discrete beds of a catalyst/sorber (A) comprising a noble metal catalyst component, a metal oxide sorber component, and a modifier; and an oxidation catalyst (B) disposed on a high suface area support or an absorber material. The sulfur and NOx compounds are removed from the exhaust (1) into catalyst system and retained therein to remove and retain the sulfur and NOx compounds. The reducing and regenerating gas (8) removes and retains said sulfur compounds and NOx is restored. In the two bed system, the catalyst system is regenerated with a regenerating gas (8) flowing in a direction reversed from direction of the exhaust gas (1).