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公开(公告)号：EP2324923B2
公开(公告)日：2023-08-23
申请号：EP09813179.0
申请日：2009-09-10
发明人： SAKAMOTO, Toru , HASEGAWA, Shoji
IPC分类号： B01J37/18 , B01J23/80 , C07C29/149 , C07C31/125 , C07B61/00 , B01J38/10 , B01J23/94
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3.发明公开
公开(公告)号：EP3804851A1
公开(公告)日：2021-04-14
申请号：EP19811341.7
申请日：2019-05-29
发明人： DASANAYAKE ALUTHGE Rasika , SHINMEI, Kenichi , YAGIHASHI, Noritoshi , NISHIYAMA, Haruka , MORI, Taiyou
IPC分类号： B01J23/78 , B01D53/86 , B01J23/80 , B01J23/83 , B01J23/89 , B01J37/04 , B01J38/10 , C01B32/40
摘要： A catalyst of the present invention contains a first transition metal oxide (A1) represented by the general formula M 1 O x , wherein M 1 represents a transition metal element, and x represents a positive real number, and a metal compound (B1) capable of adsorbing carbon dioxide. The first transition metal oxide (A1) is supported on the metal compound (B1), and the first transition metal oxide (A1) can produce a compound represented by the general formula M 1 O x-n by reduction, wherein M 1 and x are as defined above, and n represents a positive real number equal to or less than x.
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公开(公告)号：EP2621630B1
公开(公告)日：2019-03-27
申请号：EP11831126.5
申请日：2011-08-26
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公开(公告)号：EP3371137A1
公开(公告)日：2018-09-12
申请号：EP16862663.8
申请日：2016-10-07
CPC分类号： C07C5/373 , B01J8/062 , B01J29/44 , B01J29/90 , B01J38/10 , B01J38/12 , B01J2208/00504 , B01J2208/0053 , B01J2229/183 , B01J2229/186 , C07C5/333 , C07C2529/44 , C07C2601/10 , Y02P20/584 , C07C13/15
摘要： Disclosed is a process and system to convert acyclic C5 feedstock to non-aromatic, cyclic C5 hydrocarbon. A furnace and reactor tubes comprising a catalyst compound are disclosed. A process involving contacting acyclic C5 feedstock with catalyst composition and obtaining cyclic C5 hydrocarbon is also disclosed.
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公开(公告)号：EP3371135A1
公开(公告)日：2018-09-12
申请号：EP16862661.2
申请日：2016-10-07
CPC分类号： C07C5/373 , B01J29/44 , B01J29/90 , B01J38/10 , B01J38/12 , B01J2229/183 , B01J2229/186 , C07C5/333 , C07C2529/44 , C07C2601/10 , Y02P20/125 , Y02P20/584 , C07C13/15
摘要： Disclosed is an integrated process and system to generate power and convert acyclic C5 feedstock to non-aromatic, cyclic C5 hydrocarbon. A combustion device, such as a turbine, and reactor tubes containing catalyst compound are disclosed. A process involving contacting acyclic C5 feedstock with catalyst composition and obtaining cyclic C5 hydrocarbon is also disclosed.
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公开(公告)号：EP2823019B1
公开(公告)日：2018-09-12
申请号：EP13757416.6
申请日：2013-03-06
IPC分类号： C10B53/02 , C10G1/08 , C10L10/02 , B01J37/03 , B01J37/18 , B01J38/06 , B01J38/10 , B01J38/12 , B01J23/889 , B01J23/94 , B01J23/00 , B01J23/70 , B01J23/78 , B01J23/835 , B01J23/85 , B01J37/00 , C10B57/06 , C10G1/00
CPC分类号： C10B53/02 , B01J23/002 , B01J23/70 , B01J23/78 , B01J23/835 , B01J23/85 , B01J23/8892 , B01J23/94 , B01J37/0045 , B01J37/03 , B01J37/18 , B01J38/06 , B01J38/10 , B01J38/12 , C10B57/06 , C10G1/002 , C10G1/08 , C10G1/086 , C10G2300/1011 , Y02E50/13 , Y02E50/14 , Y02E50/32 , Y02P20/145 , Y02P30/20 , Y02T50/678
摘要： Described herein are processes for converting a biomass starting material (such as lignocellulosic materials) into a low oxygen containing, stable liquid intermediate that can be refined to make liquid hydrocarbon fuels. More specifically, the process can be a catalytic biomass pyrolysis process wherein an oxygen removing catalyst is employed in the reactor while the biomass is subjected to pyrolysis conditions. The stream exiting the pyrolysis reactor comprises bio-oil having a low oxygen content, and such stream may be subjected to further steps, such as separation and/or condensation to isolate the bio-oil.
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公开(公告)号：EP2880007A4
公开(公告)日：2016-06-08
申请号：EP13826421
申请日：2013-06-05
申请人： CHEVRON USA INC
发明人： TIMKEN HYE KYUNG CHO , DALVAND IZADYAR , CYR DOUGLAS ROBERT , CHENG MICHAEL TUNG-HAI , LUO HUPING , WINTER SHAWN SHLOMO , DRIVER MICHAEL SEAN , MOHR DONALD HENRY
IPC分类号： C07C7/10 , B01J31/02 , B01J38/10 , C07C7/00 , C10G29/20 , C10G45/00 , C10G67/04 , C10G69/14 , C10L1/06 , C10L1/16 , G01N33/28
CPC分类号： G01N33/225 , B01J31/0277 , B01J38/10 , C10G29/205 , C10G45/00 , C10G67/04 , C10G69/14 , C10G2300/301 , C10G2300/305 , C10G2400/02 , C10L1/06 , C10L1/1691
摘要： We provide an extracted conjunct polymer naphtha (45), comprising a hydrogenated conjunct polymer naphtha, from a used ionic liquid catalyst, having a final boiling point less than 246° C. (475° F.), a Bromine Number of 5 or less, and at least 30 wt % naphthenes. We also provide a blended alkylate gasoline (97) comprising the extracted conjunct polymer naphtha (45), and integrated alkylation processes to make the extracted conjunct polymer naphtha (45) and the blended alkylate gasoline (97). We also provide a method to analyze alkylate products, by determining an amount of methylcyclohexane in the alkylate products (80).
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公开(公告)号：EP2606104A1
公开(公告)日：2013-06-26
申请号：EP11748970.8
申请日：2011-08-17
申请人： GTL. F1 AG
CPC分类号： C10G3/62 , B01J23/005 , B01J23/75 , B01J23/94 , B01J33/00 , B01J35/023 , B01J35/1014 , B01J35/1038 , B01J38/10 , B01J38/12 , C07C1/045 , C07C2521/04 , C07C2523/36 , C07C2523/42 , C07C2523/75 , C07C2523/889 , C07C2523/89 , C10G2/332 , Y02P20/584 , Y02P30/20 , Y10S502/514 , Y10S502/518
摘要： A process for the regeneration of deactivated catalyst from a Fischer- Tropsch synthesis reactor, the catalyst being a supported cobalt catalyst. The process comprises the following steps: a withdrawal step, in which a portion of deactivated catalyst together with liquid hydrocarbon is withdrawn from the reactor; a concentration step, in which the concentration of the catalyst in the liquid hydrocarbon is increased; a calcination step, in which the deactivated catalyst composition is subjected to an oxidising gas to oxidise carbonaceous material contained in the deactivated catalyst in to gaseous oxides of the components of the carbonaceous material; and a reactivation step, in which the deactivated catalyst composition is reactivated to produced a regenerated catalyst.
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公开(公告)号：EP2448675A2
公开(公告)日：2012-05-09
申请号：EP10729775.6
申请日：2010-06-30
申请人： Virent, Inc.
发明人： BLOMMEL, Paul, George , WOODS, Elizabeth, M. , WERNER, Michael, J. , IMRIE, Aaron, James , CORTRIGHT, Randy, D.
IPC分类号： B01J38/10
CPC分类号： B01J38/10 , C07C29/132 , Y02P20/584 , C07C31/26
摘要： Processes and reactor systems are provided for the conversion of sugars to sugar alcohols using a hydrogenation catalyst, which includes apparatus and method for in-line regeneration of the hydrogenation catalyst to remove carbonaceous deposits.
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