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1.发明授权Process for the hydroformylation of higher olefins using cobalt compounds as catalyst 有权使用钴化合物作为催化剂的高级烯烃的羰基化方法公开(公告)号：US06720457B2
公开(公告)日：2004-04-13
申请号：US10200752
申请日：2002-07-24
申请人： Stefan Drees , Bernhard Scholz , Alfred Kaizik , Walter Toetsch , Wilfried Bueschken , Martin Trocha
发明人： Stefan Drees , Bernhard Scholz , Alfred Kaizik , Walter Toetsch , Wilfried Bueschken , Martin Trocha
IPC分类号： C07C4549
CPC分类号： C07C29/16 , C07C45/50 , C07C31/125 , C07C47/02
摘要： Olefins having from 5 to 24, in particular from 5 to 12, carbon atoms are hydroformylated by reacting an olefin or a mixture of olefins in the presence of an unmodified cobalt catalyst in a single-stage process in a reactor at a temperature of from 100° C. to 220° C. and a pressure of from 100 bar to 400 bar, to obtain an aldehyde, an alcohol or a mixture thereof. An aqueous bottom phase and an organic phase are present in the reactor, the aqueous bottom phase is mixed with the organic phase, and a concentration of the cobalt catalyst, calculated as metallic cobalt, in the aqueous bottom phase is in the range from 0.4 to 1.7% by mass based on the total weight of the aqueous bottom phase. A level of the aqueous bottom phase in the reactor is kept constant during steady-state operation.
摘要翻译： 具有5至24个，特别是5至12个碳原子的烯烃通过使烯烃或烯烃混合物在未改性的钴催化剂存在下在反应器中的单级方法中在100℃的温度下进行加氢甲酰化 ℃至220℃，压力为100巴至400巴，得到醛，醇或其混合物。 含水底相和有机相存在于反应器中，底部水相与有机相混合，在底部水相中以钴金属计算的钴催化剂浓度在0.4至 相对于底部水相的总重量为1.7质量％。 在稳态运行期间，反应器中的底部水相的水平保持恒定。
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公开(公告)号：US06407295B1
公开(公告)日：2002-06-18
申请号：US09396402
申请日：1999-09-15
申请人： Alfred Kaizik , Bernhard Scholz , Walter Toetsch , Martin Trocha , Wilfried Bueschken , Franz Nierlich
发明人： Alfred Kaizik , Bernhard Scholz , Walter Toetsch , Martin Trocha , Wilfried Bueschken , Franz Nierlich
IPC分类号： C07C2916
CPC分类号： C07C31/125 , C07C29/141 , C07C45/50 , C07C47/02
摘要： The invention relates to a process for preparing higher oxo alcohols from mixtures of isomeric olefins having from 5 to 24 carbon atoms by hydroformylation in the presence of a catalyst at elevated temperature and at elevated pressure, in which the hydroformylation is carried out in one stage, the olefin conversion rate for one pass is restricted to from 40 to 90% to produce a reaction mixture, and the reaction mixture is selectively hydrogenated.
摘要翻译： 本发明涉及一种通过在催化剂存在下在升高的温度和升高的压力下通过加氢甲酰化从具有5至24个碳原子的异构烯烃的混合物制备高级羰基合成醇的方法，其中加氢甲酰化在一个阶段中进行， 一次通过的烯烃转化率限制在40〜90％，生成反应混合物，反应混合物选择性氢化。
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3.发明授权Process for preparing higher oxo alcohols from olefin mixtures by two-stage hydroformylation 失效通过两步加氢甲酰化由烯烃混合物制备高级羰基合成醇的方法公开(公告)号：US06331657B1
公开(公告)日：2001-12-18
申请号：US09396371
申请日：1999-09-15
IPC分类号： C07C2916
CPC分类号： C07C31/125 , C07C29/141 , C07C45/50 , C07C47/02
摘要： A process for preparing higher oxo alcohols from mixtures of isomeric olefins having from 5 to 24 carbon atoms by two-stage hydroformylation in the presence of a cobalt catalyst or rhodium catalyst at elevated temperature and at elevated pressure, which comprises selectively hydrogenating the first hydroformylation stage reaction mixture, separating the hydrogenation mixture in a distillation into crude alcohol and low-boilers predominantly consisting of olefins, passing these low-boilers to the second hydroformylation stage, again selectively hydrogenating the second hydroformylation stage reaction mixture, separating the hydrogenation mixture in one distillation into crude alcohol and low-boilers, working up the crude alcohol by distillation to pure alcohol and taking off at least some of the low-boilers to discharge saturated hydrocarbons.
摘要翻译： 在钴催化剂或铑催化剂存在下，在升高的温度和升高的压力下，通过两步加氢甲酰化，从具有5至24个碳原子的异构烯烃的混合物制备高级羰基合成醇的方法，该方法包括选择性氢化第一加氢甲酰化阶段 将蒸馏中的氢化混合物分离成粗醇和主要由烯烃组成的低沸点，将这些低沸点通到第二加氢甲酰化阶段，再次选择性氢化第二加氢甲酰化反应混合物，在一次蒸馏中分离氢化混合物 进入粗酒精和低沸点锅炉，通过蒸馏将粗醇加工成纯酒精，并将至少一些低沸点物质排出饱和碳氢化合物。
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公开(公告)号：US06403836B1
公开(公告)日：2002-06-11
申请号：US09789571
申请日：2001-02-22
IPC分类号： C07C4550
摘要： The present invention is a process for preparing C4-25 aldehydes by hydroformylating the corresponding C3-24 olefins in the presence of a cobalt hydroformylation catalyst, and catalytically decomposing the formic acid formed in the hydroformylation reaction or in the subsequent catalyst work-up. The aldehydes so produced may be hydrogenated to form alcohols.
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5.发明授权Method for the rhodium-catalyzed hydroformylation of olefins with reduction of rhodium losses 有权用铑催化的烯烃加氢甲酰化还原铑损失的方法公开(公告)号：US07232931B2
公开(公告)日：2007-06-19
申请号：US10511280
申请日：2002-12-05
CPC分类号： C07C29/16 , C07C45/50 , C07C31/125 , C07C47/02
摘要： Process for preparing aldehydes and alcohols by rhodium-catalyzed hydroformylation of olefins having 6–20 carbon atoms with subsequent separation by distillation of the output from the hydroformylation reaction into the hydroformylation products and a rhodium-containing solution and recirculation of this solution to the hydroformylation reaction, wherein the rhodium concentration of the recirculated rhodium-containing solution is 20–150 ppm by mass.
摘要翻译： 通过铑催化的具有6-20个碳原子的烯烃的加氢甲酰化制备醛和醇的方法，随后通过蒸馏将加氢甲酰化反应的产物蒸馏成加氢甲酰化产物和含铑溶液并将该溶液再循环到加氢甲酰化反应 其中，再循环的含铑溶液的铑浓度为20〜150质量ppm。
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6.发明授权Process for preparing alkyl tert-butyl ethers and di-n-butene from field butanes 失效从野外丁烷制备烷基叔丁基醚和二正丁烯的方法
公开(公告)号：US5912191A
公开(公告)日：1999-06-15
申请号：US899797
申请日：1997-07-24
摘要： A process for the coupled production of alkyl tert-butyl ethers and butene oligomers from a mixture containing isobutane and n-butane. The isobutane is converted to the alkyl tert-butyl ether and the n-butane is converted to the oligomers. The ratio of the two reaction products may be controlled by setting the ratio of n-butane to isobutane appropriately by isomerization.
摘要翻译： 从含有异丁烷和正丁烷的混合物偶联生产烷基叔丁基醚和丁烯低聚物的方法。 将异丁烷转化为烷基叔丁基醚，将正丁烷转化为低聚物。 可以通过将正丁烷与异丁烷的比例通过异构化适当地控制来控制两种反应产物的比例。
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7.发明授权Process for preparing alkyl tert-butyl ethers and di-n-butene from field butanes 失效从野外丁烷制备烷基叔丁基醚和二正丁烯的方法
公开(公告)号：US5864052A
公开(公告)日：1999-01-26
申请号：US899792
申请日：1997-07-24
摘要： The invention relates to a process for preparing di-n-butene and alkyl tertbutyl ethers in a coupled production from field butanes, which indicates (a) separating the field butanes 1 into n-butane and isobutane in the separation stage 4, (b) dehydrogenating the n-butane 5 in a dehydrogenation stage 6 to give an n-butene-containing dehydrogenation mixture 7, oligomerizing the n-butene in the oligomerization stage 10 to give an oligomer mixture 11 and separating di-n-butene 12 off from this, and (c) de-hydrogenating the isobutane 15 in the dehydrogenation stage 16 to give an isobutene-containing dehydrogenation mixture 17 and reacting the isobutene with an alkanol 20 in the etherification stage 19 to give an alkyl tert-butyl ether 21. In an advantageous embodiment, the field butanes 1, prior to entry into the separation stage 4, are subjected to hydrogenation conditions in the hydrogenation stage 2 and an isomerization stage 3 is assigned to the separation stage 4, by means of which isomerization stage the ratio of n-butane to isobutane is set in accordance with the desired ratio of alkyl tertbutyl ether to di-n-butene.
摘要翻译： 本发明涉及一种从场丁烷偶联制备二正丁烯和烷基叔丁基醚的方法，其表明（a）在分离段4中将场丁烷1分离成正丁烷和异丁烷;（b） 在脱氢阶段6中使正丁烷5脱氢，得到含正丁烯的脱氢混合物7，使低聚反应阶段10中的正丁烯低聚，得到低聚物混合物11，并从其中分离出二 - 正丁烯12 ，和（c）脱氢阶段16中的异丁烷15脱氢，得到含异丁烯的脱氢混合物17，并使异丁烯与醚化阶段19中的链烷醇20反应，得到烷基叔丁基醚21.在 有利的实施方案中，进入分离阶段4之前的现场丁烷1在氢化阶段2中经受氢化条件，异构化阶段3分配给分离阶段4 根据所需的烷基叔丁醚与二正丁烯的比例来设定正丁烷与异丁烷的比例。
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公开(公告)号：US5998685A
公开(公告)日：1999-12-07
申请号：US899897
申请日：1997-07-24
CPC分类号： C07C29/16 , C07C11/02 , C07C2/24 , C07C5/3337 , C07C7/005 , C07C7/04 , C07C7/12 , C07C7/163 , C07C2523/04 , C07C2523/14 , C07C2523/62 , C07C2529/76
摘要： A highly flexible process for preparing butene oligomers from field butanes. The process can be controlled to produce the desired oligomerization products by appropriate selection of the starting materials.
摘要翻译： 一种用于从场丁烷制备丁烯低聚物的高度灵活的方法。 可以通过适当选择原料来控制该方法以产生所需的低聚产物。
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公开(公告)号：US5994601A
公开(公告)日：1999-11-30
申请号：US899819
申请日：1997-07-24
CPC分类号： C07C11/02 , C07C29/16 , C07C29/175 , C07C41/06
摘要： A process is described in which butene oligomers are prepared from Fischer-Tropsch olefins, in which the butenes present in a C.sub.4 fraction of Fischer-Tropsch hydrocarbons are oligomerized to obtain dibutene. The dibutene can be fractionated in a fine distillation stage into di-n-butene and di-isobutene. In one embodiment of the process, the ethylene present in the Fischer-Tropsch olefins is dimerized and the dimerization mixture is recycled to the C.sub.4 fraction. In another embodiment, the isobutene present in the C.sub.4 fraction is reacted with an alcohol to give an alkyl tert-butyl ether, and only the remaining n-butene is oligomerized so that di-n-butene is formed as the sole dibutene.
摘要翻译： 描述了一种方法，其中丁烯低聚物由费 - 托烯烃制备，其中存在于费 - 托烃的C4馏分中的丁烯被低聚以获得二丁烯。 二丁烯可以在细蒸馏阶段分馏成二正丁烯和二异丁烯。 在该方法的一个实施方案中，存在于费 - 托烯烃中的乙烯被二聚化，二聚化混合物再循环到C4级分。 在另一个实施方案中，存在于C4馏分中的异丁烯与醇反应得到烷基叔丁基醚，只剩余的正丁烯低聚，从而形成二正丁烯作为唯一的二丁烯。
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