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公开(公告)号:CA1133951A
公开(公告)日:1982-10-19
申请号:CA346105
申请日:1980-02-19
Applicant: BASF AG
Inventor: LINDNER ALFRED , VOLKAMER KLAUS , WAGNER ULRICH
Abstract: O.Z, 0050/033686 of the disclosure: A process for isolating isobutene from C4-hydrocarbon mixtures containing isobutene by reacting the mixture with a primary alcohol in the presence of an acid condensing agent, to form the tertiary ether, separating off the unconverted hydrocarbons and decomposing the tertiary ether in the presence of an acid catalyst at an elevated temperature, wherein a primary C3- or C4-alcohol is used and the temperature at which?the reaction.mixture leaves the etherification stage, in which the tertiary ether is formed, is lower than the mean temperature in the etherification stage.
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公开(公告)号:CA1151217A
公开(公告)日:1983-08-02
申请号:CA355097
申请日:1980-06-30
Applicant: BASF AG
Inventor: VOLKAMER KLAUS , LINDNER ALFRED , MERGER FRANZ , WAGNER ULRICH , BRUNNER ERWIN , SANDROCK GERHARD , STROHMEYER MAX
Abstract: A process for conjointly preparing methyl tert.-butyl ether and obtaining isobutene from an isobutene-containing C4-hydrocarbon mixture, wherein a) the C4-hydrocarbon mixture is reacted, in one or more etherification stages, with methanol and a primary C3 or C4-alcohol in the presence of an acid condensing agent, b) the resulting reaction mixture or mixtures are then separated into a fraction containing the unconverted hydrocarbons, the methyl tert.-butyl ether and a fraction containing the C3- or C4-alkyl tert.butyl ether and c) thereafter the C3- or C4-alkyl tert.-butyl ether is decomposed at r.. elevated temperature, in the presence of an acid catalyst, into isobutene and primary C3- or C4-alcohol.
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公开(公告)号:CA1251473A
公开(公告)日:1989-03-21
申请号:CA487567
申请日:1985-07-26
Applicant: BASF AG
Inventor: HOELDERICH WOLFGANG , LINDNER ALFRED , MROSS WOLF D , STROHMEYER MAX , VOLKAMER KLAUS
Abstract: But-2-enes are obtained from C4-hydrocarbon mixtures which contain but-1-ene and may or may not contain but-2-enes by catalytic isomerization of the but-1-ene to but-2-enes in an isomerization zone at elevated temperatures by a process in which the isomerization is carried out in combination with a distillative separation zone, the said hydrocarbon mixture being fed to the isomerization zone and/or distillative separation zone, the isomerization mixture obtained from the isomerization zone is passed into the distillative separation zone, a but-1-ene-containing fraction is removed above the lower third of the distillative separation zone and passed into the isomerization zone, and the but-2-enes or a fraction containing these are or is removed in the lower third of the distillative separation zone.
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公开(公告)号:CA1222529A
公开(公告)日:1987-06-02
申请号:CA457292
申请日:1984-06-22
Applicant: BASF AG
Inventor: HOELDERICH WOLFGANG , LINDNER ALFRED , MROSS WOLF D , SCHWARZMANN MATTHIAS , VOLKAMER KLAUS , WAGNER ULRICH
IPC: B01J29/00 , B01J29/04 , C07B61/00 , C07C1/00 , C07C5/22 , C07C5/25 , C07C11/02 , C07C67/00 , C07C5/23 , C07C11/08
Abstract: The invention relates to a process for the valence isomerization of an olefin in the presence of a catalyst at elevated temperatures, wherein the said isomerization is carried out in the presence of a pentasil-type zeolite as the catalyst. It is possible with this process to achieve better times-on-stream and selectivities of the catalyst than can be obtained with the conventional processes.
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公开(公告)号:CA1220757A
公开(公告)日:1987-04-21
申请号:CA470880
申请日:1984-12-21
Applicant: BASF AG
Inventor: LINDNER ALFRED , VOLKAMER KLAUS , HOFFMANN HERWIG , SANDROCK GERHARD
Abstract: A C4-hydrocarbon mixture which contains hydrocarbons which are more readily soluble in the selective solvent and those which are more sparingly soluble in the said solvent is separated with the aid of a selective solvent by a process in which the C4-hydrocarbon mixture is separated, in an extractive distillation zone, into a top product (distillate), which contains the more sparingly soluble hydrocarbons, and an extract containing the more readily soluble hydrocarbons and the selective solvent, the extract taken off as the bottom product is fed to a solvent recovery zone, in which the extract is separated into a product containing the hydrocarbons, and the selective solvent which has been partially or completely freed from the hydrocarbons, and the concentration, based on the C4-hydrocarbon/selective solvent mixture formed in the extractive distillation zone, of the selective solvent in the said zone falls below 75% by weight on one or more trays or, in the case of packed extractive distillation columns, at one or more points within the packing.
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公开(公告)号:CA1115737A
公开(公告)日:1982-01-05
申请号:CA318369
申请日:1978-12-21
Applicant: BASF AG
Inventor: BRUNNER ERWIN , SCHUBERT ECKART , LINDNER ALFRED , MERGER FRANZ , VOLKAMER KLAUS , STROHMEYER MAX , SANDROCK GERHARD
Abstract: A process for obtaining isobutene from a C4-hy-drocarbon mixture containing isobutene, which comprises (a) reacting the mixture with a primary C3- or C4-alcohol in the presence of an ion exchanger in its acid form as a condensing agent to form the corresponding C3- or C4-alkyl tert.-butyl ether by feeding the primary C3- or C4-alcohol and the C4-hydro-carbon mixture, with or without prior mixing, to an etherification reaction zone which contains the ion exchanger; (b) distilling the reaction mixture obtained from the etherification reaction zone in a first distillation zone, taking off as the top product without water washing a C4-hydrocarbon mixture comprising the unconverted hydrocarbons such top product being substantially free from isobutene and the primary C3- or C4-al-cohol and taking off as the bottom product the resulting C3or C4-alkyl tert.-butyl ether, which may contain therein primary C3- or C4-alcohol which may have been added in excess; (c) feeding the bottom product to a second reaction zone, containing an acid catalyst, in which the C3- or C4-alkyl tert.-butyl ether is decomposed at an elevated temperature to give isobutene and primary C3- and C4-alcohol; (d) feeding the mixture of isobutene and primary C3- and C4-alcohol produced in step (c) to a second distillation zone, taking off as the top product isobutene and as the bottom product the remaining C3- or C4-alcohol produced in step (c); and (e) recyoling the primary C3- or C4-alcohol which is the bottom product of step (d) to the etherification reaction zone.
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公开(公告)号:CA1222258A
公开(公告)日:1987-05-26
申请号:CA455081
申请日:1984-05-24
Applicant: BASF AG
Inventor: LINDNER ALFRED , BROELLOS KLAUS , SANDROCK GERHARD , VOLKAMER KLAUS , HEFNER WERNER
Abstract: The invention relates to a process for the separation of a C4-hydrocarbon mixture which essentially contains n-butenes and butanes. This process is characterized in that the mixture is reacted with a carboxylic acid in the presence of an acidic catalyst to form a butyl carboxylate; the reaction mixture obtained from the esterification zone is distilled to give, as the top product, a fraction containing the butanes, and, as the bottom product, a fraction containing the resulting butyl carboxylate; the butyl carboxylate is decomposed at elevated temperatures to give the carboxylic acid and n-butenes; and the mixture of n-butenes and carboxylic acid is then distilled, the n-butenes being obtained as the top product, and the carboxylic acid as the bottom product. This process permits to use apparatus that are less expensive than those required for the conventional extractive distillation method.
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公开(公告)号:CA1219882A
公开(公告)日:1987-03-31
申请号:CA457291
申请日:1984-06-22
Applicant: BASF AG
Inventor: LINDNER ALFRED , WAGNER ULRICH , VOLKAMER KLAUS , HOELDERICH WOLFGANG , HOCHSTEIN WALDHELM , IMMEL WOLFGANG
IPC: B01J27/00 , B01J27/28 , B01J29/00 , C07B61/00 , C07C1/00 , C07C5/23 , C07C5/25 , C07C7/04 , C07C11/08 , C07C67/00
Abstract: 1-Butene is recovered from a C4-hydrocarbon mixture which contains 2-butenes and may or may not contain 1-butene by catalytic isomerization of the 2-butenes to 1-butene at elevated temperatures and isolation of the 1-butene, by a process in which the said isomerization is carried out in the presence of an acidic catalyst at from 150 to 500.degree.C, the isomerization mixture obtained from the isomerization zone is fed into a distillation zone, 1-butene is taken off at the top of the distillation zone, a fraction containing 2-butenes is taken off in the lower third of the distillation zone and fed into the isomerization zone, and the starting C4hydrocarbon mixture which contains 2-butenes and may or may not contain 1-butene is fed to the distillation zone and/or the isomerization zone.
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公开(公告)号:CA1182774A
公开(公告)日:1985-02-19
申请号:CA402343
申请日:1982-05-05
Applicant: BASF AG
Inventor: BROELLOS KLAUS , VOLKAMER KLAUS , LINDNER ALFRED
Abstract: A process for obtaining a conjugated diolefin from a mixture of C4 or C5 hydrocarbons which contains this diolefin, by single-stage or multistage extractive distillation using a selective solvent and recycling the latter to the extractive distillation, after it has been obtained from the stripping zone downstream from each extractive distillation, a bleed stream of the recycled selective solvent being regenerated in a solvent purification stage in which the high-boiling or non-volatile impurities present in the solvent are separated off, and the regenerated solvent obtained from the solvent purification stage also being recycled, which process comprises regenerating the solvent in a thin-film evaporation zone.
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公开(公告)号:CA1145290A
公开(公告)日:1983-04-26
申请号:CA347098
申请日:1980-03-06
Applicant: BASF AG
Inventor: VOLKAMER KLAUS , BROELLOS KLAUS , LINDNER ALFRED , WAGNER ULRICH , WEITZ HANS-MARTIN , SCHNEIDER KLAUS-JUERGEN
Abstract: A process for isolating a conjugated diolefin from a C4- or C5-hydrocarbon mixture containing the diolefin, by single-stage or multi-stage extractive distillation using a selective solvent, wherein the selective solvent is a solvent mixture which comprises: a) from 50 to 98 percent by weight of an N-alkyl-substituted lower aliphatic acid amide or of an N-alkyl-substituted alicyclic acid amide having 5 ring members and b) from 2 to 50 percent by weight of a lower aliphatic carboxylic acid ester or carbonic acid ester boiling at from 30.degree.C to 200.degree.C.
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