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公开(公告)号:EP4146613A1
公开(公告)日:2023-03-15
申请号:EP21725800.3
申请日:2021-05-06
IPC分类号: C04B35/486 , C04B35/626 , H01M10/0525 , C01G25/00
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公开(公告)号:EP3463644B1
公开(公告)日:2022-06-29
申请号:EP17727463.6
申请日:2017-05-23
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公开(公告)号:EP3648879A1
公开(公告)日:2020-05-13
申请号:EP18752327.9
申请日:2018-07-06
发明人: EVANS, Martin , FISHER, Rick
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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
发明人: LORD, Adrian , SMIDT, Martin
IPC分类号: C07C29/17 , C07C31/125 , C07C29/80
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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
发明人: REED, Graham , HILES, Andrew George , ANDERSSON, Rikard Umberto , TILLEY, Simon Nicholas , GORDON, Paul
IPC分类号: C07C67/08
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公开(公告)号:EP3374074A1
公开(公告)日:2018-09-19
申请号:EP16797609.1
申请日:2016-11-10
CPC分类号: B01J8/067 , B01J8/0496 , B01J2208/00212 , C07C45/002 , C07C47/04
摘要: An apparatus for the production of formaldehyde is disclosed. The apparatus comprises a cooled tubular reactor section (8, 108, 208, 308, 408, 508) having a first inlet, a first outlet and a plurality of tubes each having a first end in fluid communication with the first inlet and a second end in fluid communication with the first outlet. The plurality of tubes contain a first catalyst for the production of formaldehyde by oxidative dehydrogenation. The apparatus is characterised in that the apparatus further comprises a pre-reactor section (7, 107, 207, 307, 407, 507). The pre-reactor section (7, 107, 207, 307, 407, 507) has an inlet. The pre-reactor section (7, 107, 207, 307, 407, 507) has an outlet in fluid communication with the first inlet of the cooled tubular reactor section (8, 108, 208, 308, 408, 508). The pre-reactor section (7, 107, 207, 307, 407, 507) is configured to contain, in use, an adiabatic catalyst bed. The adiabatic catalyst bed comprises a second catalyst for the production of formaldehyde by catalytic oxidative dehydrogenation.
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公开(公告)号:EP3359620A1
公开(公告)日:2018-08-15
申请号:EP16781171.0
申请日:2016-10-05
发明人: BRIERLEY, Aidan
摘要: A method of monitoring a parameter of a hydrocarbon well, pipeline or formation is provided. The method comprises introducing a tracer into the hydrocarbon well, pipeline or formation; producing a fluid from the hydrocarbon well, pipeline or formation; and analysing the fluid to determine if the tracer is present in the fluid. The tracer comprises a halogenated alkoxylated-benzoic acid, an alkoxylated benzene sulfonic acid, a salt of a halogenated alkoxylated-benzoic acid or a salt of an alkoxylated benzene sulfonic acid.
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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
发明人: GRAY, Julian
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.
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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
IPC分类号: C07C67/08
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.
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