专利快速检索-快速检索全球专利，免费商用专利数据库-IPRDB

51. 发明公开

EP4208435A1 PROCESS FOR REFINING A CRUDE ETHYLENE GLYCOL STREAM 审中-实审
公开(公告)号：EP4208435A1
公开(公告)日：2023-07-12
申请号：EP21769795.2
申请日：2021-09-03
申请人： Johnson Matthey Davy Technologies Limited
发明人： SWINNEY, John , GORDON, Paul , WATSON, David John , REED, Graham
IPC分类号： C07C29/88 , C07C31/20 , C07C51/12 , C07C59/06 , C07C67/08 , C07C69/675

52. 发明授权

EP3402772B1 METHANOL PROCESS 有权
公开(公告)号：EP3402772B1
公开(公告)日：2020-09-16
申请号：EP16816361.6
申请日：2016-12-16
申请人： Johnson Matthey Davy Technologies Limited
发明人： YIU, Kar Chi
IPC分类号： C07C29/151 , C07C29/152 , C07C29/154 , C07C31/04

53. 发明公开

EP3526185A1 PROCESS FOR THE PRODUCTION OF 2-ALKYLALKANOL 有权
公开(公告)号：EP3526185A1
公开(公告)日：2019-08-21
申请号：EP17787565.5
申请日：2017-10-12
申请人： Johnson Matthey Davy Technologies Limited
发明人： LORD, Adrian , SMIDT, Martin
IPC分类号： C07C29/17 , C07C31/125 , C07C29/80

54. 发明授权

EP2885268B8 PROCESS FOR THE PREPARATION OF DIALKYL SUCCINATE FROM MALEIC ANHYDRIDE 有权
公开(公告)号：EP2885268B8
公开(公告)日：2019-06-05
申请号：EP14784377.5
申请日：2014-10-13
申请人： Johnson Matthey Davy Technologies Limited
发明人： REED, Graham , HILES, Andrew George , ANDERSSON, Rikard Umberto , TILLEY, Simon Nicholas , GORDON, Paul
IPC分类号： C07C67/08

55. 发明授权

EP1262228B1 PROCESS AND PLANT FOR THE PRODUCTION OF METHANOL 有权
公开(公告)号：EP1262228B1
公开(公告)日：2019-03-20
申请号：EP02253481.2
申请日：2002-05-17
申请人： Johnson Matthey Davy Technologies Limited
发明人： Eastland, Philip Henry Donald
IPC分类号： B01J8/04 , C07C29/152 , C12C11/02

56. 发明公开

EP3429716A1 PROCESS FOR RECOVERING ALDEHYDE OBTAINED BY HYDROFORMULATION IN TWO COLUMNS WITH INCREASING PRESSURE 有权
公开(公告)号：EP3429716A1
公开(公告)日：2019-01-23
申请号：EP17702940.2
申请日：2017-01-30
申请人： Johnson Matthey Davy Technologies Limited
发明人： SMIDT, Martin Lucas
IPC分类号： B01D3/14 , B01D3/00 , B01D1/28

57. 发明公开

EP3402772A1 METHANOL PROCESS 有权
公开(公告)号：EP3402772A1
公开(公告)日：2018-11-21
申请号：EP16816361.6
申请日：2016-12-16
申请人： Johnson Matthey Davy Technologies Limited
发明人： YIU, Kar Chi
IPC分类号： C07C29/151 , C07C29/152 , C07C29/154 , C07C31/04
摘要： A process is described for the synthesis of methanol comprising the steps of: (i) passing a first synthesis gas mixture comprising a make-up gas through a first synthesis reactor containing a cooled methanol synthesis catalyst to form a first product gas stream, (ii) recovering methanol from the first product gas stream thereby forming a first methanol-depleted gas mixture, (iii) combining the first methanol-depleted gas mixture with a loop recycle gas stream to form a second synthesis gas mixture, (iv) passing the second synthesis gas mixture through a second synthesis reactor containing a cooled methanol synthesis catalyst to form a second product gas stream, (v) recovering methanol from the second product gas stream thereby forming a second methanol-depleted gas mixture, and (vi) using at least part of the second methanol-depleted gas mixture as the loop recycle gas stream, wherein the first synthesis reactor has a higher heat transfer per cubic meter of catalyst than the second synthesis reactor, none of the loop recycle gas stream is fed to the first synthesis gas mixture and the recycle ratio of the loop recycle gas stream to form the second synthesis gas mixture is in the range 1.1:1 to 6:1.

58. 发明授权

EP3265545B1 PROCESS FOR PRODUCING A SUBSTITUTE NATURAL GAS 有权
公开(公告)号：EP3265545B1
公开(公告)日：2018-10-17
申请号：EP16707531.6
申请日：2016-02-25
申请人： Johnson Matthey Davy Technologies Limited
发明人： JANARDHANAN, Madhanakrishnan , KHAMBATI, Riyaz Ezzuddin
IPC分类号： C10L3/08
CPC分类号： C10L3/08 , C10L2290/04 , C10L2290/06 , C10L2290/10 , C10L2290/148 , C10L2290/46
摘要： A process is described for producing a substitute natural gas (SNG) comprising the steps of: feeding a first synthesis gas feed stream comprising hydrogen, methane, carbon monoxide and/or carbon dioxide in parallel to two or more bulk methanators in a first bulk methanation zone comprising a first bulk methanator and a final bulk methanator, feeding a second synthesis gas feed stream comprising hydrogen, carbon monoxide and/or carbon dioxide to one or more bulk methanators in a second bulk methanation zone comprising a first bulk methanator, each bulk methanator containing a methanation catalyst such that the feed streams are at least partially methanated, dividing the methanated gas stream recovered from the final bulk methanator in the first bulk methanation zone into a first portion and a second portion, recirculating the first portion in a recirculation loop to the first bulk methanator of the first bulk methanation zone to dilute the first synthesis gas feed stream fed to said first bulk methanator, and feeding the second portion to the first bulk methanator of the second bulk methanation zone to dilute the second synthesis gas feed stream fed to said first bulk methanator, wherein the feed pressure of the second synthesis gas feed stream is lower than the feed pressure of the first synthesis gas feed stream and the difference in pressure between the first and second feed streams is at least the pressure drop through the first bulk methanation zone.

59. 发明授权

EP3200909B1 ANNULAR CATALYST CARRIER CONTAINER FOR USE IN A TUBULAR REACTOR 有权
公开(公告)号：EP3200909B1
公开(公告)日：2018-07-18
申请号：EP15766137.2
申请日：2015-09-16
申请人： Johnson Matthey Davy Technologies Limited
发明人： GRAY, Julian
IPC分类号： B01J8/06 , B01J8/00 , B01J8/02 , B01J8/04
CPC分类号： B01J8/0214 , B01J8/0015 , B01J8/0415 , B01J8/06 , B01J8/067 , B01J2208/00814 , B01J2208/06
摘要： In a catalyst carrier for insertion in a reactor tube of a tubular reactor, the catalyst carrier includes a container for holding catalyst in use. The container has a bottom surface closing the container, and a top surface. A carrier outer wall extends from the bottom surface to the top surface. A seal extends from the container by a distance which extends beyond the carrier outer wall. The carrier outer wall has apertures located below the seal.

60. 发明授权

EP2958885B1 PROCESS FOR THE PREPARATION OF SUCCINIC ACID ESTER 有权
公开(公告)号：EP2958885B1
公开(公告)日：2018-07-04
申请号：EP14809676.1
申请日：2014-12-02
申请人： Johnson Matthey Davy Technologies Limited
发明人： SMIDT, Martin Lucas , CAMPBELL, Ian , REED, Graham , GORDON, Paul , FERGUSON, Christopher
IPC分类号： C07C67/08
CPC分类号： C07C67/08 , B01D3/009 , B01D3/143 , B01D17/0208 , C07C67/54 , C07C69/40
摘要： A process for the production of dialkyl succinate from a bio-succinic acid feedstock commencing by feeding bio-succinic acid to a reaction distillation column to enable esterification of the succinic acid. The feedstock is passed co-currently with upflowing alkanol such that an esterification reaction occurs. An overhead vapor stream is removed from the reaction distillation column comprising di-ester, alkanol, water of esterification and organic components. The vapor stream is sent to an alkanol separation column where alkanol is separated from the water of esterification and organic components. A side draw is removed from the alkanol separation column comprising partially immiscible organic and aqueous phases. The side draw is passed to a phase separation apparatus where the partially immiscible organic and aqueous phases are separated. The organic phase is passed to a column where the dialkyl succinate is recovered from residual water and other organic components.

你已经成功收藏专利！

检索式保存成功!

IPRDB

热门服务

关于我们

友情链接

联系方式