-
公开(公告)号:US09656928B2
公开(公告)日:2017-05-23
申请号:US14538993
申请日:2014-11-12
CPC分类号: C07C4/06 , B01J29/40 , B01J35/002 , B01J37/06 , B01J2229/16 , B01J2229/37 , B01J2229/38 , C01B39/026 , C01B39/36 , C07C4/02 , C07C2529/035 , Y02P20/52 , C07C11/06 , C07C11/04
摘要: A novel process and a novel catalyst for the production of light olefins. 1-butene is cracked in the presence of an acid- or base-modified silicalite-1 catalyst bed, wherein the modified silicalite-1 has a Si/Al ratio of greater than 1000. The modification procedures described herein increase the selectivity of the silicalite-1 catalyst toward light olefins such as ethylene and propylene. The catalytic cracking of 1-butene may be carried out in a fixed bed reactor or a fluidized bed reactor.
-
公开(公告)号:US09783464B2
公开(公告)日:2017-10-10
申请号:US15489382
申请日:2017-04-17
CPC分类号: C07C4/06 , B01J29/40 , B01J35/002 , B01J37/06 , B01J2229/16 , B01J2229/37 , B01J2229/38 , C01B39/026 , C01B39/36 , C07C4/02 , C07C2529/035 , Y02P20/52 , C07C11/06 , C07C11/04
摘要: A novel process and a novel catalyst for the production of light olefins. 1-butene is cracked in the presence of an acid- or base-modified silicalite-1 catalyst bed, wherein the modified silicalite-1 has a Si/Al ratio of greater than 1000. The modification procedures described herein increase the selectivity of the silicalite-1 catalyst toward light olefins such as ethylene and propylene. The catalytic cracking of 1-butene may be carried out in a fixed bed reactor or a fluidized bed reactor.
-
公开(公告)号:US09783465B1
公开(公告)日:2017-10-10
申请号:US15658879
申请日:2017-07-25
CPC分类号: C07C4/06 , B01J29/40 , B01J35/002 , B01J37/06 , B01J2229/16 , B01J2229/37 , B01J2229/38 , C01B39/026 , C01B39/36 , C07C4/02 , C07C2529/035 , Y02P20/52 , C07C11/06 , C07C11/04
摘要: A novel process and a novel catalyst for the production of light olefins. 1-butene is cracked in the presence of an acid- or base-modified silicalite-1 catalyst bed, wherein the modified silicalite-1 has a Si/Al ratio of greater than 1000. The modification procedures described herein increase the selectivity of the silicalite-1 catalyst toward light olefins such as ethylene and propylene. The catalytic cracking of 1-butene may be carried out in a fixed bed reactor or a fluidized bed reactor.
-
-