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公开(公告)号:KR860000515B1
公开(公告)日:1986-05-02
申请号:KR820001971
申请日:1982-05-06
Applicant: STAMICARBON
Inventor: RULKANS PETER F M , HAASEN NICOLAAS F , PLANTEMA OTTO G
IPC: B01D3/14 , C07D201/16
Abstract: The purifn. of epsilon-caprolactam (I), which is obtd. by the rearrangement of cyclohexanone oxine by H2SO4 or oleum and is used as an intermediate for Nylon, comprises a two-stage vacuum distn. The crude(I) is passed to the first column, which has an evaporator with a packed column with a pressure drop of less than 2.5 mbar per theoretical tray, and from which low b.p. impurities are removed as overheads. The bottom prods. are passed to the second column wherepure(I) is septd. as overhead and the high b.p. impurities as bottoms.
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公开(公告)号:KR830001756B1
公开(公告)日:1983-09-03
申请号:KR800002956
申请日:1980-07-25
Applicant: STAMICARBON
Inventor: GEMM PAUL C VAN , GRAAF THEODORUS F M DE , KNOL DIRK , PLANTEMA OTTO G
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公开(公告)号:KR870000056B1
公开(公告)日:1987-02-09
申请号:KR830001703
申请日:1983-04-22
Applicant: STAMICARBON
Inventor: HOUSMANS JOHANNES G H M , NISPEN SIMON J M VAN , PLANTEMA OTTO G
IPC: C07C27/00 , B01J27/00 , B01J27/053 , B01J27/25 , B01J31/00 , B01J31/04 , C07B61/00 , C07C27/12 , C07C29/132 , C07C29/50 , C07C35/08 , C07C45/00 , C07C45/33 , C07C45/53 , C07C49/403 , C07C67/00 , C07C407/00 , C07C409/06 , C07C409/14
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4.
公开(公告)号:CA1123457A
公开(公告)日:1982-05-11
申请号:CA332513
申请日:1979-07-25
Applicant: STAMICARBON
Inventor: PLANTEMA OTTO G
IPC: C07C49/385 , C07C45/00 , C07C45/85 , C07C67/00 , C07C45/78
Abstract: Aldehydes are removed by aldol condensation from a mixture containing a C5-C12 ring atom cycloalkanone, aldehydes and corresponding cycloalkyl esters of C4 or greater carboxylic acids, the mixture resulting from the liquid phase oxidation of the corresponding cycloalkane with molecular oxygen. The aldol condensation reaction converts at least 80% of the aldehydes present while no more than 20% of the cycloalkyl esters are saponified. A slight excess of no more than 2% of the cycloalkanone required for the aldehyde removal is converted in the aldol condensation. Cycloalkanones thus treated and freed of the aldehyde are processed into polylactams exhibiting particularly high mechanical strengths.
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公开(公告)号:CA1244475A
公开(公告)日:1988-11-08
申请号:CA426474
申请日:1983-04-22
Applicant: STAMICARBON
Inventor: HOUSMANS JOHANNES G H M , VAN NISPEN SIMON P J M , PLANTEMA OTTO G
IPC: C07C27/00 , B01J27/00 , B01J27/053 , B01J27/25 , B01J31/00 , B01J31/04 , C07B61/00 , C07C27/12 , C07C29/132 , C07C29/50 , C07C35/08 , C07C45/00 , C07C45/33 , C07C45/53 , C07C49/403 , C07C67/00 , C07C407/00 , C07C409/06 , C07C409/14 , C07C31/135
Abstract: Process for preparing cyclohexanol and cyclohexanone by oxidizing cyclohexane with a gas containing molecular oxygen to form an oxidation mixture containing cyclohexyl hydroperoxide and treating the oxidation mixture with a metal salt in the presence of an aqueous solution of an alkali metal hydroxide for the decomposition of the cyclohexyl hydroperoxide is characterized in that the treatment of the oxidation mixture is effected at a temperature of about 70 .degree.C to about 115 .degree.C. When temperatures less than 70 .degree.C are employed the reaction velocity is too low. Temperatures in excess of about 115 .degree.C unexpectedly reduced the yield of the desired products. Thus the about 70 .degree.C to about 115 .degree.C temperature range is critical. The process produces cyclohexanol and cyclohexanone of sufficient purity for conversion in nylon 6 monomers without intervening purification.
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公开(公告)号:CA1182775A
公开(公告)日:1985-02-19
申请号:CA402546
申请日:1982-05-07
Applicant: STAMICARBON
Inventor: RULKENS PETER F M , HAASEN NICOLAAS F , PLANTEMA OTTO G
IPC: B01D3/14 , C07D201/16
Abstract: 1. Process for the purification of .epsilon.-caprolactam, obtained through rearrangement of cyclohexanone oxime by means of sulphuric acid or oleum, by subjecting the caprolactam to be purified to distillation under reduced pressure, with separation of low-boiling and high-boiling impurities. The distillation is carried out in two steps with at least in the 1st step an evaporator with a rectification column containing packing material with a pressure drop of less than 2.5 mbar per theoretical tray. The caprolactam to be purified is supplied to the rectification column of the 1st step, the low-boiling impurities are carried off from this column, the bottom product remaining in the 1st step is supplied to the 2nd step and in this step the high-boiling impurities are carried off as bottom product. The purified caprolactam is recovered as top product.
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公开(公告)号:CA1140594A
公开(公告)日:1983-02-01
申请号:CA357158
申请日:1980-07-28
Applicant: STAMICARBON
Inventor: VAN GEEM PAUL C , DE GRAAF THEODORUS F M , KNOL DIRK , PLANTEMA OTTO G
IPC: B01J23/00 , C07B61/00 , C07C5/11 , C07C27/00 , C07C29/04 , C07C29/05 , C07C29/06 , C07C29/08 , C07C35/08 , C07C45/34 , C07C45/39 , C07C67/00 , C07C49/403
Abstract: The invention relates to a method for the preparation of cyclohexanol and/or cyclohexanone by hydrogenating benzene to cyclohexene, hydrating the cyclohexene to cyclohexanol and/or oxidating it to cyclohexanone, recovering the cyclohexanol and/or cyclohexanone, and returning unconverted benzene and/or cyclohexene to the hydrogenating stop. The method according to the invention is characterized in that the mixture of cyclohexane with benzene and/or cyclohexene, which has also been obtained during the separation of cyclohexanol from the reaction mixture of the hydration step and/or cyclohexanone from the reaction mixture of the oxidation step, is subjected to a dehydrogenation reaction, and the benzene thus obtained is returned to the hydrogenation step. The method according to the invention has the great advantage that the difficult separation of cyclohexane from mixtures with benzene and/or cyclohexene can be dispensed with . Losses of expensive extractive distillation agent are avoided. Neither is any cyclohexane left as byproduct for wich a use will have to be found. In the hydrogenation step a higher degree of benzene conversion can be applied, so that economic process operation has become possible.
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公开(公告)号:CA1094578A
公开(公告)日:1981-01-27
申请号:CA292712
申请日:1977-12-08
Applicant: STAMICARBON
Inventor: PLANTEMA OTTO G , PENDERS JOSEF M
Abstract: A process for the preparation of cycloalkanol by way of a two stage reaction from cycloalkene. The first reaction stage consists of reacting cycloalkene with sulphuric acid. The resultant adduct which is cycloalkyl hydrogen sulphate is separated from the reaction mixture by use of an inert solvent. The adduct is then hydrolyzed in the second reaction stage to product the cycloalkanol.
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公开(公告)号:DD145529A5
公开(公告)日:1980-12-17
申请号:DD21491779
申请日:1979-08-10
Applicant: STAMICARBON
Inventor: PLANTEMA OTTO G
IPC: C07C49/385 , C07C45/00 , C07C45/85 , C07C67/00
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公开(公告)号:CS220799B2
公开(公告)日:1983-04-29
申请号:CS526180
申请日:1980-07-25
Applicant: STAMICARBON
Inventor: VAN GREEM PAUL CH , DE GRAFF THEODORUS F , KNOL DIRK , PLANTEMA OTTO G
IPC: B01J23/00 , C07B61/00 , C07C5/11 , C07C27/00 , C07C29/04 , C07C29/05 , C07C29/06 , C07C29/08 , C07C35/08 , C07C45/34 , C07C45/39 , C07C67/00
Abstract: The invention relates to a method for the preparation of cyclohexanol and/or cyclohexanone by hydrogenating benzene to cyclohexene, hydrating the cyclohexene to cyclohexanol and/or oxidating it to cyclohexanone, recovering the cyclohexanol and/or cyclohexanone, and returning unconverted benzene and/or cyclohexene to the hydrogenating step.The method according to the invention is characterized in that the mixture of cyclohexane with benzene and/or cyclohexene, which has also been obtained during the separation of cyclohexanol from the reaction mixture of the hydration step and,or of cyclohexanone from the reaction mixture of the oxidation step, is subjected to a dehydrogenation reaction, and the benzene thus obtained is returned to the hydrogenation step.The method according to the invention has the great advantage that the difficult separation of cyclohexane from mixtures with benzene and / or cyclohexene can be dispensed with. Losses of expensive extractive distillation agent are avoided. Neither is any cyclohexane left as by-product for wich a use will have to be found. In the hydrogenation step a higher degree of benzene conversion can be applied, so that economic process operation has become possible.
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