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1.
公开(公告)号:US07115787B2
公开(公告)日:2006-10-03
申请号:US10534973
申请日:2003-11-11
CPC分类号: C07C29/04 , Y02P20/127 , C07C31/12
摘要: The invention relates to a process for preparing tert-butanol (TBA) from isobutene-containing mixtures, in which at least part of the conversion is achieved with the aid of a reactive rectification.
摘要翻译: 本发明涉及从含异丁烯的混合物制备叔丁醇(TBA)的方法,其中至少部分转化是借助于无功精馏而实现的。
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2.
公开(公告)号:US20060025638A1
公开(公告)日:2006-02-02
申请号:US10534973
申请日:2003-11-11
IPC分类号: C07C29/04
CPC分类号: C07C29/04 , Y02P20/127 , C07C31/12
摘要: The invention relates to a process for preparing tert-butanol (TBA) from isobutene-containing mixtures, in which at least part of the conversion is achieved with the aid of a reactive rectification.
摘要翻译: 本发明涉及从含异丁烯的混合物制备叔丁醇(TBA)的方法,其中至少部分转化是借助于无功精馏而实现的。
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公开(公告)号:US07179948B2
公开(公告)日:2007-02-20
申请号:US10739086
申请日:2003-12-19
申请人: Bernhard Scholz , Franz Nierlich , Dieter Reusch , Silvia Santiago Fernandez , Andreas Beckmann , Wilfried Bueschken , Alfred Kaizik
发明人: Bernhard Scholz , Franz Nierlich , Dieter Reusch , Silvia Santiago Fernandez , Andreas Beckmann , Wilfried Bueschken , Alfred Kaizik
摘要: The invention relates to a process for preparing tert-butanol by reaction of a homogeneous mixture comprising water, tert-butanol and an isobutene-containing hydrocarbon mixture over an acidic ion-exchange resin at from 30 to 120° C., wherein the homogeneous mixture contains, at a proportion by mass of isobutene of above 10%, from 30 to 80% of the maximum amount of water made possible by the solubility of water in the mixture of tert-butanol and the isobutene-containing hydrocarbon mixture.
摘要翻译: 本发明涉及一种通过酸性离子交换树脂在30〜120℃下由包含水,叔丁醇和含异丁烯的烃混合物的均匀混合物反应制备叔丁醇的方法,其中均匀混合物 以大于10%的异丁烯的比例含有由水在叔丁醇和含异丁烯的烃混合物的混合物中的溶解度而产生的最大量的水的30至80%。
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公开(公告)号:US07026519B2
公开(公告)日:2006-04-11
申请号:US10893306
申请日:2004-07-19
IPC分类号: C07C29/04
摘要: The invention relates to a process for preparing tert-butanol (TBA) by reacting isobutene-containing hydrocarbon mixtures with water over acidic solid catalysts in a plurality of reactors, wherein the conversion is increased upstream of the last reactor by removing a portion of the TBA present in the reaction mixture.
摘要翻译: 本发明涉及一种在多个反应器中通过使含异丁烯的烃混合物与水在酸性固体催化剂上反应制备叔丁醇(TBA)的方法,其中转化通过除去一部分TBA 存在于反应混合物中。
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公开(公告)号:US20050043571A1
公开(公告)日:2005-02-24
申请号:US10893306
申请日:2004-07-19
摘要: The invention relates to a process for preparing tert-butanol (TBA) by reacting isobutene-containing hydrocarbon mixtures with water over acidic solid catalysts in a plurality of reactors, wherein the conversion is increased upstream of the last reactor by removing a portion of the TBA present in the reaction mixture.
摘要翻译: 本发明涉及一种在多个反应器中通过使含异丁烯的烃混合物与水在酸性固体催化剂上反应制备叔丁醇(TBA)的方法,其中转化通过除去一部分TBA 存在于反应混合物中。
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公开(公告)号:US07002053B2
公开(公告)日:2006-02-21
申请号:US10467844
申请日:2001-12-28
IPC分类号: C07C2/24 , C07C2/02 , C07C61/00 , C07C211/00
CPC分类号: C07C2/28 , C07C29/141 , C07C45/50 , C07C51/235 , C07C2531/10 , C07C11/02 , C07C53/126 , C07C31/125 , C07C47/02
摘要: The invention relates to a process for preparing high-purity diisobutene by reaction of isobutene or isobutene-containing hydrocarbon mixtures over a solid acidic ion-exchange resin containing sulfonic acid groups whose protons have been partly replaced by metal ions and to the use of the diisobutene.
摘要翻译: 本发明涉及一种通过异丁烯或含异丁烯的烃混合物在含有质子部分被金属离子取代的磺酸基的固体酸性离子交换树脂上进行反应制备高纯度二异丁烯的方法,以及使用二异丁烯 。
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公开(公告)号:US07161053B2
公开(公告)日:2007-01-09
申请号:US10634894
申请日:2003-08-06
申请人: Andreas Beckmann , Franz Nierlich , Udo Peters , Wilfried Büschken , Lothar Kerker , Dietrich Maschmeyer , Dirk Röttger
发明人: Andreas Beckmann , Franz Nierlich , Udo Peters , Wilfried Büschken , Lothar Kerker , Dietrich Maschmeyer , Dirk Röttger
摘要: Isobutene in isobutenic hydrocarbon mixtures is oligomerized over a solid acidic ion exchange resin, said acidic ion exchange resin containing, for example, sulfonic acid groups, some of whose protons have been exchanged for metal ions.
摘要翻译: 异丁烯烃混合物中的异丁烯在固体酸性离子交换树脂上低聚,所述酸性离子交换树脂含有例如磺酸基团,其中一些质子已经被交换成金属离子。
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8.
公开(公告)号:US07432407B2
公开(公告)日:2008-10-07
申请号:US10487950
申请日:2002-09-20
申请人: Andreas Beckmann , Armin Rix , Udo Knippenberg , Franz Nierlich , Wilfried Bueschken , Ralf Duessel
发明人: Andreas Beckmann , Armin Rix , Udo Knippenberg , Franz Nierlich , Wilfried Bueschken , Ralf Duessel
CPC分类号: C07C5/05 , C07C5/2562 , C07C2523/44 , C07C2531/02 , C07C11/09
摘要: The invention relates to a process by which C4- to C6-olefins or an essentially sulfur-free olefin cut comprising C4- to C6-olefins is isomerized over a catalyst comprising an element of the eighth transition group of the Periodic Table, in the presence of at least one added sulfur compound, and any polyunsaturated hydrocarbons contained therein are selectively hydrogenated and hydroisomerized, and also the sulfur compounds are separated from the product and optionally recycled, so that virtually sulfur-free products are obtained.
摘要翻译: 本发明涉及一种方法,其中C 4 - 至C 6 - 烯烃或基本上不含硫的烯烃馏分包含C 4 - 至 在至少一种添加的硫化合物的存在下,C 6 - 6烯烃在包含元素周期表第八转化基团的元素的催化剂上异构化,并且其中包含的任何多不饱和烃被选择性氢化和 加氢异构化,并且硫化合物与产物分离并任选地循环使用,从而获得实质上无硫的产物。
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9.
公开(公告)号:US07128814B2
公开(公告)日:2006-10-31
申请号:US10790707
申请日:2004-03-03
申请人: Andreas Beckmann , Dieter Reusch
发明人: Andreas Beckmann , Dieter Reusch
CPC分类号: C07C29/80 , Y10S203/09 , C07C31/12
摘要: The present invention relates to a process for separating 2-butanol from tert-butanol/water by adding of tert-butanol such that the water concentration lowers to less than the limit concentration of the distillation boundary line connecting the two azeotropes TBA/water and SBA/water and is subsequently worked up by distillation.
摘要翻译: 本发明涉及通过加入叔丁醇从叔丁醇/水中分离2-丁醇的方法,使得水浓度降低到小于连接两种共沸物TBA /水和SBA的蒸馏边界线的极限浓度 /水,随后通过蒸馏处理。
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公开(公告)号:US20050014985A1
公开(公告)日:2005-01-20
申请号:US10868904
申请日:2004-06-17
IPC分类号: B01J31/10 , B01J8/00 , B01J8/02 , B01J8/06 , B01J19/00 , B01J19/24 , C07B61/00 , C07C1/24 , C07C11/09 , C07C1/00 , B01J8/04 , B01J10/00 , C07C9/00
CPC分类号: B01J8/0242 , B01J8/0005 , B01J8/06 , B01J19/0013 , B01J19/2475 , B01J2219/00006 , C07C1/24 , C07C2531/08 , C07C11/09
摘要: Isobutene is prepared by dissociating tert-butanol into isobutene and water over an acid ion-exchange resin arranged as a fixed bed in at least one reactor at a temperature of from 80 to 150° C. and at a pressure of from 5 to 25 bar to obtain a reaction mixture, separating the reaction mixture into isobutene, a by-product, water and at least one mixture of undissociated tert-butanol and water. The reactor is operated pseudo-isothermally, with a temperature difference between inflowing and outflowing streams of less than 15 K.
摘要翻译: 异丁烯是通过在80至150℃的温度和5至25巴的压力下,在至少一个反应器中将叔丁醇离解成异丁烯和水,在酸性离子交换树脂上作为固定床排列的, 以获得反应混合物,将反应混合物分离成异丁烯,副产物,水和至少一种未离解的叔丁醇和水的混合物。 反应器假模拟运行,流入和流出之间的温度差小于15K。
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