公开(公告)号：EP0145372A3

公开(公告)日：1985-08-28

申请号：EP84308076

申请日：1984-11-21

申请人： Sun Refining and Marketing Company

发明人： Polleck, Richard E. ,  Scott, Kenneth A. ,  Ledley, Robert E.

IPC分类号： C07C07/148

CPC分类号： C10G31/08 ,  C10G29/16

摘要： The reaction rate for the hydrolysis of carbonyl sulfide in liquid petroleum hydrocarbons over alumina, such as propylene, is greatly increased by maintaining water in the hydrocarbons in an amount of one mole of water per mole of carbonyl sulfide to an upper limit of about ten moles of water per mole of carbonyl sulfide or about 30% of saturation of the hydrocarbons, whichever upper limit provides the lesser amount of water.

公开(公告)号：EP0253637A3

公开(公告)日：1988-12-14

申请号：EP87306235

申请日：1987-07-14

申请人： EXXON CHEMICAL PATENTS INC.

发明人： Plotkin, Jeffrey Stuart ,  Michaelson, Robert Charles

IPC分类号： C07C07/148 ,  C07C11/09 ,  C07C11/10 ,  C07C41/20 ,  C07C43/04

CPC分类号： C07C41/20 ,  C07C7/14891 ,  C07C41/06 ,  C07C11/02 ,  C07C43/04 ,  C07C43/15

摘要： In a process for separating C⁴ to C⁷ tertiary mono-olefins(s) present in a C⁴ to C⁷ hydrocarbon mixture containing diolefins which comprises selectively reacting said tertiary mono-olefin mixture with a primary alcohol in the presence of an acid catalyst to convert it to tertiary ether(s). separating the tertiary ether(s) from the unreacted hydrocarbon mixture and containing said tertiary ether(s) in the presence of a catalyst to decompose it to tertiary olefin(s) and a primary alcohol. the improvement which comprises hydrogenating the tertiary ether(s) after it has been separated from the unreacted hydrocarbon mixture and prior to decomposition to saturate the unsaturated ether(s) formed from the diolefins present in the hydrocarbon mixture.

公开(公告)号：EP0071983A3

公开(公告)日：1983-05-18

申请号：EP82107068

申请日：1982-08-05

申请人： VEG-GASINSTITUUT N.V.

发明人： van der Wal, Willem J. J. ,  Geus, John Wilhelm, Prof.

IPC分类号： C10K01/20 ,  C07C07/148 ,  C01B03/56 ,  C01B17/04 ,  B01D53/34

CPC分类号： B01D53/02 ,  B01D53/04 ,  B01D2253/112 ,  B01D2253/304 ,  B01D2253/306 ,  B01D2253/308 ,  B01D2257/30 ,  B01D2257/304 ,  B01D2257/308 ,  C01B3/56 ,  C01B17/04 ,  C01B2203/042 ,  C01B2203/0485 ,  C10K1/20

公开(公告)号：EP0177195A3

公开(公告)日：1986-05-28

申请号：EP85306337

申请日：1985-09-06

申请人： MOBIL OIL CORPORATION

发明人： McWilliams, John Paul ,  Nemet-Mavrodin, Margaret Iosif ,  Sigal, Catherine Teague ,  Wilson, Robert Currin, Jr

IPC分类号： C07C07/148 ,  B01J21/10 ,  C07C06/12 ,  C07C02/66

CPC分类号： B01J37/0009 ,  B01J21/10 ,  C07C7/148 ,  C07C15/00

摘要： A method is provided for removing trace amounts of organic chlorides from feedstocks by contacting the feedstock with a guard bed catalyst comprising shaped particles formed by extruding a mixture of magnesium oxide and a binder inert to the feedstock. The process has particular importance in removing organic chlorides from toluene feedstocks prior to contacting toluene with a disporportionation or alkylation catalyst comprising magnesium-ZSM-5.

公开(公告)号：EP0169828A3

公开(公告)日：1986-05-14

申请号：EP85870101

申请日：1985-07-19

申请人： LABOFINA S.A.

发明人： Debras, Guy L.G. ,  De Clippeleir, Georges E.M.J. ,  Cahen, Raymond M.

IPC分类号： C07C07/148

CPC分类号： C07C7/148 ,  C07C11/02

公开(公告)号：EP0012570A3

公开(公告)日：1980-07-23

申请号：EP79302805

申请日：1979-12-06

申请人： MOBIL OIL CORPORATION

发明人： Wu, Margaret May-Som ,  Young, Lewis Bewster

IPC分类号： C07C15/02 ,  C07C07/148 ,  C07B29/00 ,  B01J29/28 ,  B01J29/36 ,  C07C39/06 ,  C07C37/86 ,  C07C47/542 ,  C07C45/85 ,  C07C25/02 ,  C07C17/38 ,  C07C87/50 ,  C07C85/26

CPC分类号： C07C209/68 ,  B01J29/40 ,  B01J29/70 ,  B01J2229/20 ,  B01J2229/26 ,  B01J2229/36 ,  B01J2229/42 ,  C07C4/18 ,  C07C7/148 ,  C07C17/361 ,  C07C37/50 ,  C07C37/86 ,  C07C45/67 ,  C07C45/85 ,  C07C2529/40 ,  C07C2529/70 ,  Y02P20/52 ,  C07C15/02 ,  C07C25/06 ,  C07C47/55 ,  C07C47/542 ,  C07C39/06 ,  C07C39/04

摘要： isomeric mixtures of disubstituted aromatic compounds are brought into contact with a shape selective crystalline zeolite catalyst, under conversion conditions, to undergo selective reaction of the 1,4-isomer, thereby leaving the 1-2-isomer and/or 1,3-isomer in excess of equilibrium. The shape selective zeolite catalyst employed herein comprises a crystalline zeolite having a silica to alumina ratio of at least 12 and a constraint index, as herein defined, within the approximate range of 1 to 12.