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公开(公告)号:US20190210989A1
公开(公告)日:2019-07-11
申请号:US16315680
申请日:2017-07-19
Applicant: BASF SE
Inventor: Joaquim Henrique TELES , Marvin KRAMP , Christian MUELLER , Nicolai Tonio WOERZ , Bernd METZEN , Tobias KELLER , Dominic RIEDEL , Markus WEBER , Daniel URBANCZYK , Andrei-Nicolae PARVULESCU , Ulrike WEGERLE , Ulrich MUELLER
IPC: C07D301/32 , C07D301/12 , C07D303/04
Abstract: Disclosed herein is a process for purifying propylene oxide, including the steps of: (i) providing a stream S0 containing propylene oxide, acetonitrile, water, and an organic compound containing a carbonyl group —C(═O)—; and (ii) separating propylene oxide from the stream S0 by subjecting the stream S0 to distillation conditions in a distillation column to obtain a gaseous top stream S1c which is enriched in propylene oxide compared to the stream S0, a liquid bottoms stream S1a which is enriched in acetonitrile and water compared to the stream S0, and a side stream S1b containing propylene oxide which is enriched in the carbonyl compound compared to the stream S0.
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公开(公告)号:US20210403447A1
公开(公告)日:2021-12-30
申请号:US17056741
申请日:2019-05-08
Applicant: BASF SE , Kolon Plastics Inc.
Inventor: Thomas HEITZ , Marvin KRAMP , Manfred HEILIG , HyunSoo CHANG , JongMoon KIM , In Gi CHO
IPC: C07D317/12
Abstract: The present invention relates to a process for preparing dioxolane by reacting ethylene glycol with an aqueous solution of formaldehyde in the presence of an acid catalyst. The raw product comprising water, dioxolane and methanol is fed to a phase separation unit (20) wherein an organic extracting agent is present. An organic fraction stream from the phase separation unit is transferred to an upper part of a purification column (30) from which dioxolane is withdrawn as a bottom product while the distillate stream of the purification column is recycled to the phase separation unit. An aqueous fraction stream from the phase separation unit is transferred to a waste water column (40), withdrawing a waste water stream from the bottom of the waste water column, withdrawing a side stream (42) from a stage between the feed stage and the reflux stage of the waste water column and recycling this stream (42) to the phase separation unit, and withdrawing a distillate stream (43) containing methanol from the waste water column.
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公开(公告)号:US20250074859A1
公开(公告)日:2025-03-06
申请号:US18292365
申请日:2022-07-19
Applicant: BASF SE
Inventor: Tile GIESHOFF , Marvin KRAMP , Cornelis Hendricus DE RUITER , Karl-Friedrich SCHNEIDER , Felix HUELSMANN , Christian REIN , David ELIXMANN
IPC: C07C67/54
Abstract: A process for continuously distiling acrylates by means of a rectification column, wherein the acrylate content in the feed to the rectification column is at least 80% by weight, the liquid in the bottom region of the rectification column is heated by means of an evaporator, and the parts of the evaporator that are in contact with product are made from stainless steel.
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公开(公告)号:US20210002241A1
公开(公告)日:2021-01-07
申请号:US16500313
申请日:2018-04-13
Applicant: BASF SE
Inventor: Nicolai Tonio WOERZ , Ulrich MUELLERE , Andrei-Nicolae PARVULESCU , Dominic RIEDEL , Marvin KRAMP , Daniel URBANCZYK , Ulrike WEGERLE , Christian MUELLER , Bernd METZEN , Markus WEBER , Joaquim Henrique TELES
IPC: C07D301/32 , C07D301/19
Abstract: The invention relates to a process for preparing propylene oxide, comprising (i) providing a stream comprising propene, propane, hydrogen peroxide or a source of hydrogen peroxide, water, and an organic solvent; (ii) passing the liquid feed stream provided in (i) into an epoxidation zone comprising an epoxidation catalyst comprising a titanium zeolite, and subjecting the liquid feed stream to epoxidation reaction conditions in the epoxidation zone, obtaining a reaction mixture comprising propene, propane, propylene oxide, water, and the organic solvent; (iii) removing an effluent stream from the epoxidation zone, the effluent stream comprising propene, propane, propylene oxide, water, and the organic solvent; (iv) separating propene and propane from the effluent stream by distillation, comprising subjecting the effluent stream to distillation conditions in a distillation unit, obtaining a gaseous stream (S1) which is enriched in propene and propane compared to the effluent stream subjected to distillation conditions, and a liquid bottoms stream (S2) which is enriched in propylene oxide, water and organic solvent compared to the effluent stream subjected to distillation conditions; (v) separating propane from the stream (S1) in a separation zone, comprising subjecting the stream (S1) to washing conditions in a scrubber, wherein a solvent mixture comprising organic solvent and water is added as entraining agent, obtaining a bottoms stream (S3), which comprises organic solvent, water and at least 70 weight-% of the propene comprised in (S1); and a gaseous top stream (S4), which comprises at least 5 weight-% of the propane comprised in stream (S1).
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公开(公告)号:US20190169149A1
公开(公告)日:2019-06-06
申请号:US16318221
申请日:2017-07-19
Applicant: BASF SE , Dow Global Technologies LLC
Inventor: Joaquim Henrique TELES , Marvin KRAMP , Christian MUELLER , Nicolai Tonio WOERZ , Bernd METZEN , Tobias KELLER , Dominic RIEDEL , Heiner SCHELLING , Markus WEBER , Daniel URBANCZYK , Andrei-Nicolae PARVULESCU , Ulrike WEGERLE , Ulrich MUELLER , Meinolf WEIDENBACH , Werner J. WITZL , Karsten LUECKE
IPC: C07D301/32 , C07D301/12 , B01D3/00 , B01D3/40 , B01D3/14 , B01D5/00
CPC classification number: C07D301/32 , B01D1/28 , B01D3/00 , B01D3/009 , B01D3/143 , B01D3/40 , B01D5/006 , B01J29/085 , B01J29/7038 , B01J29/86 , B01J29/89 , B01J35/002 , B01J35/023 , B01J37/0045 , B01J2229/186 , B01J2229/42 , C07D301/12 , C07D303/04 , Y02P20/127 , Y02P20/52
Abstract: The present invention is related to a process for preparing propylene oxide, comprising (i) providing a stream comprising propene, hydrogen peroxide or a source of hydrogen peroxide, water, and an organic solvent; (ii) passing the liquid feed stream provided in (i) into an epoxidation zone comprising an epoxidation catalyst comprising a titanium zeolite, and subjecting the liquid feed stream to epoxidation reaction conditions in the epoxidation zone, obtaining a reaction mixture comprising propene, propylene oxide, water, and the organic solvent; (iii) removing an effluent stream from the epoxidation zone, the effluent stream comprising propylene oxide, water, organic solvent, and propene; (iv) separating propene from the effluent stream by distillation, comprising (iv.1) subjecting the effluent stream to distillation conditions in a distillation unit, obtaining a gaseous top stream S0 enriched in propene compared to the effluent stream subjected to distillation conditions, and a liquid bottoms stream S01 enriched in propylene oxide, water and organic solvent compared to the effluent stream subjected to distillation conditions; (iv.2) returning a condensed portion of the stream S0 to an upper part of the distillation unit.
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6.
公开(公告)号:US20240198263A1
公开(公告)日:2024-06-20
申请号:US18288043
申请日:2022-04-19
Applicant: BASF SE
Inventor: Yunfei ZHOU , Ortmund LANG , Matthias Wilhelm MEIER , Cornelis Hendricus DE RUITER , Marvin KRAMP , Gregor GRACKIEWICZ , Josef MACHT , Markus GITTER , Claus HECHLER
Abstract: The invention relates to a centrifugal droplet separator for separating liquid droplets out of a gas stream, comprising a shell (1) having a circular cross section and a vertical longitudinal axis (11), an upper hood (2) that bounds the shell (1) at the top and has a gas exit port (7) for the gas stream cleaned in the centrifugal droplet separator, a drip plate (8) disposed beneath the gas exit port (7), a lower hood (10) that bounds the shell (1) at the bottom and has a liquid exit port (4) for removal of the deposited liquid droplets, and an inlet (3) that opens tangentially into the shell (1) for supply of the gas stream,
wherein
there are at least two nozzles (9) for feeding a stabilizer liquid into the interior of the centrifugal droplet separator, the respective nozzle outlet (15) of which is disposed between the tangential inlet (3) and the drip plate (8) in vertical direction, where the main spraying direction (12) of the nozzles (9) is directed upward at an internal angle of 0 to 60° relative to the vertical longitudinal axis (11).
The invention additionally also relates to a method of separating liquid droplets out of a gas stream in such a centrifugal droplet separator.-
公开(公告)号:US20240067596A1
公开(公告)日:2024-02-29
申请号:US18273790
申请日:2022-01-24
Applicant: BASF SE
Inventor: Ortmund LANG , Claus HECHLER , Cornelis DE RUITER , Marvin KRAMP , Dominik HERBRECHT
CPC classification number: C07C69/54 , B01D1/0088
Abstract: The present invention relates to a continuous process for obtaining 2-ethylhexyl acrylate (2-EHA) from a mixture (1) that is liquid under an absolute pressure in the range from 0.5 to 100 bar and has a temperature in the range from 0 to 300° C., comprising 2-EHA, at least one high boiler, at least one homogeneous catalyst, and at least one low boiler, wherein the mixture (1) is depressurized by a pressure-maintenance device (3) to an absolute pressure level in the range from 0.1 to 10 bar, wherein the resulting two-phase gas/liquid mixture (16) is continuously supplied to a helical-tube evaporator (4) in which, at a temperature in the range from 50 to 300° C., the 2-EHA content of the liquid phase of the two-phase gas/liquid mixture is reduced by partial evaporation, this being accompanied by a parallel increase in the 2-EHA content of the gas phase of the two-phase gas/liquid mixture, and the two phases are discharged in the form of a resulting two-phase gas/liquid output stream (17).
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公开(公告)号:US20240010603A1
公开(公告)日:2024-01-11
申请号:US18039986
申请日:2021-12-08
Applicant: BASF SE
Inventor: Dominik HERBRECHT , Cornelis Hendricus DE RUITER , Marvin KRAMP , Maike FEUERSTEIN , Piotr MAKARCZYK , Tile GIESHOFF
IPC: C07C67/08
CPC classification number: C07C67/08
Abstract: The present invention relates to a process for the continuous preparation of (meth)acrylate by reacting an alcohol with a (meth)acrylic acid using at least one control unit which is closed-loop controlled by a sensor (S).
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公开(公告)号:US20230249098A1
公开(公告)日:2023-08-10
申请号:US18012996
申请日:2021-06-17
Applicant: BASF SE
Inventor: Bernd METZEN , Christian KUNKELMANN , Ortmund LANG , Marvin KRAMP , Claus HECHLER
Abstract: The invention relates to an apparatus for carrying out mass transfer processes, comprising a column having at least two inlet pipes for introducing a gaseous phase, where separation-active internals are accommodated in the column and a column section extends from the at least two inlet pipes to the separation-active internals, in which section a coverage of a cross-sectional area of the column is less than 25%, based on the total cross-sectional area, and where the at least two inlet pipes have a height offset which corresponds to not more than three times an inlet pipe diameter and the at least two inlet pipes are at an angle (α) of from 60° to 150° to one another and have asymmetry with respect to one another. The invention further relates to a use of the apparatus and also a method for designing the apparatus.
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公开(公告)号:US20220073490A1
公开(公告)日:2022-03-10
申请号:US17056750
申请日:2019-05-08
Applicant: BASF SE , Kolon Plastics Inc.
Inventor: Thomas HEITZ , Marvin KRAMP , Manfred HEILIG , HyunSoo CHANG , JongMoon KIM , In Gi CHO
IPC: C07D317/12
Abstract: The present invention relates to a process for preparing dioxolane by reacting ethylene glycol with an aqueous solution of formaldehyde in the presence of an acid catalyst. The raw product comprising water, dioxolane and methanol is fed to a phase separation unit (20) wherein an organic extracting agent is present. An organic fraction stream from the phase separation unit is transferred to an upper part of a purification column (30) from which dioxolane is withdrawn as a bottom product while the distillate stream of the purification column is recycled to the phase separation unit. An aqueous fraction stream from the phase separation unit is transferred to a waste water column (40), withdrawing a waste water stream from the bottom of the waste water column, recycling a distillate stream (42) from the waste water column to the phase separation unit, and withdrawing a side stream (43) containing methanol from a stage below the feed stage of the waste water column.
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