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公开(公告)号：US07208635B2
公开(公告)日：2007-04-24
申请号：US10500722
申请日：2003-01-16
摘要： The invention relates to a hydroformylation process in which at least one olefin having from 2 to 6 carbon atoms is reacted continuously with carbon monoxide and hydrogen in the presence of a hydroformylation catalyst in a reaction zone in which a liquid phase is present and a stream S) is taken from the liquid phase, heat is removed from this stream and the stream is subsequently returned to the reaction zone without removal of a material component.
摘要翻译： 本发明涉及一种加氢甲酰化方法，其中至少一种具有2至6个碳原子的烯烃在加氢甲酰化催化剂存在下，在存在液相的反应区中与一氧化碳和氢气连续反应，流S ）从液相中取出，从该流中除去热量，随后将物流返回到反应区而不去除材料成分。
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公开(公告)号：US20050119509A1
公开(公告)日：2005-06-02
申请号：US10500722
申请日：2003-01-16
摘要： The invention relates to a hydroformylation process in which at least one olefin having from 2 to 6 carbon atoms is reacted continuously with carbon monoxide and hydrogen in the presence of a hydroformylation catalyst in a reaction zone in which a liquid phase is present and a stream S) is taken from the liquid phase, heat is removed from this stream and the stream is subsequently returned to the reaction zone without removal of a material component.
摘要翻译： 本发明涉及一种加氢甲酰化方法，其中至少一种具有2至6个碳原子的烯烃在加氢甲酰化催化剂存在下，在存在液相的反应区中与一氧化碳和氢气连续反应，流S ）从液相中取出，从该流中除去热量，随后将物流返回到反应区而不去除材料成分。
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3.发明授权Method for producing propylene hydroformylation products and acrylic acid and/or acrolein 有权制备丙烯加氢甲酰化产物和丙烯酸和/或丙烯醛的方法公开(公告)号：US06864391B2
公开(公告)日：2005-03-08
申请号：US10312362
申请日：2001-06-27
申请人： Roland Krokoszinski , Ulrich Hammon , Kevin Todd
发明人： Roland Krokoszinski , Ulrich Hammon , Kevin Todd
IPC分类号： C07C27/14 , C07B61/00 , C07C45/33 , C07C45/35 , C07C45/50 , C07C47/02 , C07C47/22 , C07C51/215 , C07C51/235 , C07C51/25 , C07C57/05 , C07C57/055 , C07C27/10 , C07C51/16
CPC分类号： C07C51/215 , C07C45/33 , C07C45/35 , C07C45/50 , C07C51/235 , C07C47/22 , C07C47/02 , C07C57/04
摘要： A process for preparing hydroformylation products of propylene and for preparing acrylic acid and/or acrolein comprises a) feeding a propylene-containing feed in which from 2 to 40% by weight of propane is present and also carbon monoxide and hydrogen into a reaction zone and reacting this mixture in the presence of a hydroformylation catalyst to form hydroformylation products of propane, b) separating a stream consisting essentially of unreacted propylene and propane from the output from the reaction zone, and c) subjecting the stream consisting essentially of propylene and propane to a catalytic gas-phase oxidation in the presence of molecular oxygen to form acrylic acid and/or acrolein.
摘要翻译： 制备丙烯的加氢甲酰化产物和用于制备丙烯酸和/或丙烯醛的方法包括：a）将含丙烯的进料，其中存在2-40重量％的丙烷，还有一氧化碳和氢气进入反应区， 在加氢甲酰化催化剂存在下使该混合物反应以形成丙烷的加氢甲酰化产物，b）从反应区的输出中分离基本上由未反应的丙烯和丙烷组成的物流，和c）将基本上由丙烯和丙烷组成的料流 在分子氧存在下进行催化气相氧化以形成丙烯酸和/或丙烯醛。
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4.发明授权Method for the continuous hydroformylation of polyakenes having 30 to 700 carbon atoms 失效具有30至700个碳原子的聚酮的连续加氢甲酰化的方法公开(公告)号：US06849769B2
公开(公告)日：2005-02-01
申请号：US10363660
申请日：2001-09-11
申请人： Michael Röper , Heinrich-Josef Blankertz , Armin Volker Grenacher , Roland Krokoszinski , Willi Schönmann
发明人： Michael Röper , Heinrich-Josef Blankertz , Armin Volker Grenacher , Roland Krokoszinski , Willi Schönmann
CPC分类号： C08F8/00 , Y02P20/584 , Y10S585/901 , C08F110/10
摘要： Essentially monounsaturated polyalkylenes having from 30 to 700 carbon atoms are continuously hydroformylated by a process in which i) a hydroformylation-active cobalt carbonyl catalyst is prepared from a catalyst precursor dissolved in an aqueous phase in the absence of the polyalkylenes, ii) the polyalkylenes are hydroformylated by means of synthesis gas in the presence of the cobalt carbonyl catalyst in a reaction zone, iii) the cobalt carbonyl catalyst is separated from the output from the reaction zone with at least partial reformation of the catalyst precursor and the catalyst precursor is recirculated to step i).
摘要翻译： 具有30至700个碳原子的基本单不饱和聚亚烷基通过以下方法连续加氢甲酰化，其中i）在不存在聚亚烷基的情况下由溶解在水相中的催化剂前体制备加氢甲酰化 - 活性钴羰基催化剂，ii）聚亚烷基 在羰基催化剂存在下，通过合成气在反应区中加氢甲酰化，iii）将钴羰基催化剂与反应区的输出分离，至少部分重新形成催化剂前体，催化剂前体再循环至 步骤i）。
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公开(公告)号：US06380443B1
公开(公告)日：2002-04-30
申请号：US09677862
申请日：2000-10-03
申请人： Detlef Kratz , Harald Rust , Roland Krokoszinski , Volker Helf
发明人： Detlef Kratz , Harald Rust , Roland Krokoszinski , Volker Helf
IPC分类号： C07C2704
CPC分类号： C07C45/72 , C07C29/141 , C07C45/50 , C07C47/02 , C07C31/20 , C07C31/125
摘要： A process for preparing 1,3-diols having 6 or more carbon atoms comprises a) provision of at least one alkanal having at least three carbon atoms; b) thermal treatment of the alkanal in the absence of a basic catalyst; c) hydrogenation of the aldol addition product formed in step b); and d) isolation of the 1,3-diol obtained. The process of the present invention makes it possible to prepare 1,3-diols simply and inexpensively.
摘要翻译： 制备具有6个或更多个碳原子的1,3-二醇的方法包括：a）提供至少一种具有至少三个碳原子的链烷烃; b）在没有碱性催化剂的情况下热处理链烷烃; c）步骤b）中形成的醛醇加成产物的氢化; 和d）所获得的1,3-二醇的分离。本发明的方法使得可以简单且廉价地制备1,3-二醇。
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公开(公告)号：US20130131416A1
公开(公告)日：2013-05-23
申请号：US13680910
申请日：2012-11-19
申请人： Sven CRONE , Oliver RYLL , Till BLUM , Alexander WECK , Rainer PAPP , Roland KROKOSZINSKI , Heinrich-Josef BLANKERTZ
发明人： Sven CRONE , Oliver RYLL , Till BLUM , Alexander WECK , Rainer PAPP , Roland KROKOSZINSKI , Heinrich-Josef BLANKERTZ
IPC分类号： C07C2/06
CPC分类号： C07C2/06 , C07C2/10 , C07C2523/755 , C07C11/02
摘要： Process for preparing oligomers by continuous oligomerization of butenes, wherein a) a feed stream comprising 1-butene and 2-butene in a total concentration of from 10 to 70% by weight and from 10 to 60% by weight of isobutane is used (hereinafter referred to as feed stream 1), b) this feed stream 1 is reacted until more than 60% by weight of the 1-butene comprised in the feed stream 1 but less than 50% by weight of the 2-butene comprised in feed stream 1 have been converted into oligomers, c) the oligomers obtained in b) are separated off and optionally passed to a further work-up and the remaining residual stream is fed to work-up by distillation, d) isobutane is separated off by distillation from the residual stream, e) the isobutane-depleted stream obtained after the work-up by distillation d) (hereinafter referred to as feed stream 2) is reacted to form oligomers.
摘要翻译： 使用丁烯连续低聚制备低聚物的方法，其中a）以总浓度为10至70重量％和10至60重量％的异丁烷的1-丁烯和2-丁烯的进料流（以下称为“ 称为进料流1），b）将该进料流1反应直至包含在进料流1中的大于60重量％的1-丁烯，但小于进料流中包含的2-丁烯的50重量％ 1）已经转化为低聚物，c）将b）中得到的低聚物分离出来并任选地进一步处理，剩余的剩余物流被进料以通过蒸馏进行后处理，d）通过蒸馏将异丁烷分离出来 残留物流，e）通过蒸馏处理后得到的异丁烷贫化物流d）（以下称为进料流2）反应而形成低聚物。
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公开(公告)号：US20080251458A1
公开(公告)日：2008-10-16
申请号：US12088777
申请日：2006-09-25
IPC分类号： C02F1/44
CPC分类号： C07C45/74 , B01D3/143 , C02F1/04 , C02F1/20 , C02F1/26 , C02F1/66 , C02F9/00 , C02F2103/36 , C02F2209/06 , C07C45/80 , Y10S210/908 , C07C47/21
摘要： Process for the treatment of wastewater from an aldolization process which is contaminated with water-soluble and/or dispersed organic impurities by means of single-stage or multistage extraction with an organic liquid of the aldolization process wastewater which has been set to a pH of from 0 to 6, in which an organic liquid obtained by stripping of the acidified aldolization process wastewater or of the acidified and extracted aldolization process wastewater, condensation of the stripped compounds and phase separation of the condensate is used as extractant for the extraction of organic impurities from the acidified aldolization process wastewater and wastewater having a lower content of organic impurities than the aldolization process wastewater fed to the extraction is taken off from the stripping apparatus.
摘要翻译： 用于通过单级或多级萃取与水溶性和/或分散的有机杂质污染的醛醇醛化方法处理废水的方法，该方法已经设定为pH为 0至6，其中通过汽提酸化的醛化工艺废水或酸化和提取的醛醇化工艺废水获得的有机液体，汽提化合物的冷凝和冷凝物的相分离用作萃取剂，用于萃取有机杂质 酸化的醛醇化工艺废水和有机杂质含量低于进料到萃取的醛化工艺废水中的废水从汽提装置中取出。
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8.发明授权公开(公告)号：US06969777B2
公开(公告)日：2005-11-29
申请号：US10312360
申请日：2001-06-27
申请人： Helmut Walz , Willi Schönmann , Rolf Müller , Roland Krokoszinski
发明人： Helmut Walz , Willi Schönmann , Rolf Müller , Roland Krokoszinski
摘要： Olefins having from 2 to 8 carbon atoms are hydroformylated in a process in which (i) an olefin-containing feed in which a proportion of a saturated hydrocarbon having from 2 to 8 carbon atoms is present and also carbon monoxide and hydrogen are fed into a reaction zone and reacted in the presence of a hydroformylation catalyst, (ii) a stream consisting essentially of unreacted olefin and saturated hydrocarbon is separated off from the output from the reaction zone, (iii) the stream is separated into an olefin-enriched fraction and an olefin-depleted fraction by rectification, and (iv) at least part of the olefin-enriched fraction is recirculated to the reaction zone.
摘要翻译： 具有2至8个碳原子的烯烃在其中（i）含烯烃的进料中存在一部分具有2至8个碳原子的饱和烃以及一氧化碳和氢气进料到 反应区并在加氢甲酰化催化剂存在下反应，（ii）基本上由未反应的烯烃和饱和烃组成的物流与反应区的输出分离，（iii）将物流分离成富含烯烃的馏分和 通过精馏的烯烃贫化馏分，和（iv）至少部分富烯烃馏分再循环到反应区。
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9.发明授权Method for producing hydroformylation products of olefins with 2 to 8 carbon atoms 有权2-8个碳原子的烯烃加氢甲酰化产物的制备方法公开(公告)号：US06914162B2
公开(公告)日：2005-07-05
申请号：US10312365
申请日：2001-06-27
摘要： A process for preparing hydroformylation products of olefins having from 2 to 8 carbon atoms comprises a) feeding a hydrocarbon feedstock into a cracking/dehydrogenation zone and subjecting it to thermal and/or catalytic cracking and/or dehydrogenation to give an olefin-containing cracker gas, b) subjecting the cracker gas or fractions thereof to a fractionation to give at least one Ci-olefin-enriched hydrocarbon stream and at least one Ci-olefin-depleted hydrocarbon stream, c) feeding the Ci-olefin-enriched hydrocarbon stream together with carbon monoxide and hydrogen into a hydroformylation zone and reacting it in the presence of a hydroformylation catalyst, d) separating a stream consisting essentially of unreacted Ci-olefin and saturated Ci-hydrocarbon from the output from the hydroformylation zone, e) recirculating at least part of the stream consisting essentially of unreacted Ci-olefin and saturated Ci-hydrocarbon to step b), where i is an integer from to 8. The proposed coupling of the hydroformylation with, for example, a steam cracker allows complete hydroformylation of the olefins produced without olefin losses via the waste gas.
摘要翻译： 具有2至8个碳原子的烯烃的加氢甲酰化产物的制备方法包括：a）将烃原料进料到裂化/脱氢区，并进行热和/或催化裂化和/或脱氢，得到含烯烃的裂化气 b）使裂化器气体或其馏分进行分馏以产生至少一种富含C 1 -C 6烃的烃流和至少一种不饱和碳原子的烯烃 烃流，c）将富含碳原子的烃流与一氧化碳和氢气一起加入加氢甲酰化区，并在加氢甲酰化催化剂的存在下使其反应，d）将基本上 的来自加氢甲酰化区的输出的未反应的C 1 - 烯烃和饱和C 1 -C 4烃，e）使至少部分基本上由未反应的C - 烯烃和饱和C 1 - 烃到步骤b），其中i是从8到8的整数。所提出的加氢甲酰化与例如蒸汽裂化器的偶联允许通过废气完全烯烃生成而不产生烯烃。
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公开(公告)号：US06727391B2
公开(公告)日：2004-04-27
申请号：US10203293
申请日：2002-08-08
IPC分类号： C07C4550
摘要： A liquid output from a continuous hydroformylation, which comprises essentially aldehydes, high-boiling by-products, a homogeneously dissolved hydroformylation catalyst, unreacted olefins, low-boiling by-products and dissolved synthesis gas, is worked up by a process in which a) the liquid hydroformylation output is depressurized in a first depressurization stage to a pressure which is from 2 to 20 bar below the reactor pressure, resulting in separation into a liquid phase and a gas phase, and b) the liquid phase obtained in the first depressurization stage is depressurized in a second depressurization stage to a pressure which is lower than the pressure of the first depressurization stage, resulting in separation into a liquid phase comprising essentially high-boiling by-products of the hydroformylation, the homogeneously dissolved hydroformylation catalyst and small amounts of hydroformylation product and unreacted olefin and a gas phase comprising essentially the major part of the hydroformylation product, unreacted olefin and low-boiling by-products.
摘要翻译： 来自连续加氢甲酰化的液体产物，其基本上包含醛，高沸点副产物，均匀溶解的加氢甲酰化催化剂，未反应的烯烃，低沸点副产物和溶解的合成气，其中a） 在第一减压阶段将液体加氢甲酰化产物减压至低于反应器压力2至20巴的压力，从而分离成液相和气相，和b）将第一减压阶段获得的液相减压 在第二减压阶段到低于第一减压阶段的压力的压力，导致分离成包含基本上加氢甲酰化的高沸点副产物的液相，均匀溶解的加氢甲酰化催化剂和少量加氢甲酰化产物 和未反应的烯烃和基本上包含水的主要部分的气相 罗夫酰化产物，未反应的烯烃和低沸点副产物。
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