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    Method for producing tricyclodecandialdehyde
    21.
    发明授权
    Method for producing tricyclodecandialdehyde 失效
    三环癸二醛生产方法

    公开(公告)号：US07321068B2

    公开(公告)日：2008-01-22

    申请号：US10581802

    申请日：2004-12-14

    申请人： Rainer Papp ,  Rocco Paciello ,  Christoph Benisch

    发明人： Rainer Papp ,  Rocco Paciello ,  Christoph Benisch

    IPC分类号： C07C45/50 ,  C07C35/21 ,  C07C209/00

    CPC分类号： C07C209/26 ,  C07C29/141 ,  C07C47/347 ,  C07C2603/68 ,  C07C211/19 ,  C07C31/278

    摘要： Process for preparing tricyclodecanedialdehyde by hydroformylation of dicyclopentadiene by means of a CO/H2 mixture at elevated temperature and under superatmospheric pressure in the presence of a rhodium catalyst which has not been modified by means of a ligand and is homogeneously dissolved in the hydroformylation medium, wherein the hydroformylation is carried out at a pressure of from 200 to 350 bar in at least two reaction zones, with a reaction temperature of from 80 to 120° C. being set in a first reaction zone and a reaction temperature of from 120 to 150° C. being set in a reaction zone following this reaction zone, with the proviso that the reaction temperature in the subsequent reaction zone is at least 5° C. higher than in the preceding reaction zone.

    摘要翻译： 在高温和超大气压下，在没有通过配体修饰的铑催化剂存在下，通过二环戊二烯加氢甲酰化二环戊二烯制备三环癸二醛的方法， 均匀地溶解在加氢甲酰基化介质中，其中加氢甲酰化在至少两个反应区中在200-350巴的压力下进行，反应温度为80-120℃设定在第一反应区和 在该反应区之后的反应区中设置120至150℃的反应温度，条件是后续反应区中的反应温度比前述反应区高至少5℃。

    Method for the continuous production of aldehydes
    22.
    发明申请
    Method for the continuous production of aldehydes 失效
    连续生产醛的方法

    公开(公告)号：US20070004939A1

    公开(公告)日：2007-01-04

    申请号：US10575843

    申请日：2004-10-14

    申请人： Martin Volland ,  Thomas Mackewitz ,  Wolfgang Ahlers ,  Ansgar Schafer ,  Wolfgang Richter ,  Rocco Paciello

    发明人： Martin Volland ,  Thomas Mackewitz ,  Wolfgang Ahlers ,  Ansgar Schafer ,  Wolfgang Richter ,  Rocco Paciello

    IPC分类号： C07C45/50

    CPC分类号： B01J31/186 ,  B01J2231/321 ,  B01J2531/822 ,  C07C45/50 ,  C07C47/02

    摘要： The invention relates to a method for the continuous production of aldehydes comprising between 5 and 21 carbon atoms, by the isomerising hydroformylation in a homogenous phase of olefin compositions comprising between 4 and 20 carbon atoms and containing α-olefins and olefins with internal double bonds, by means of a synthesis gas, in the presence of a homogeneous rhodium catalyst that is complexed with an organophosphorus ligand containing oxygen atoms and/or nitrogen atoms and a free ligand. Said production is carried out at high temperature and high pressure in a multi-stage reaction system consisting of at least two reaction zones. According to said method, the olefin composition is first reacted in a first reaction zone or a group of several first reaction zones at a total pressure of between 10 and 40 bar, using a synthesis gas with a CO/H2 molar ratio of between 4:1 and 1:2 until a 40 to 95% conversion of the α-olefins is obtained. The hydroformylation product from the first reaction zone or group of several first reaction zones is then reacted in a subsequent reaction zone or group of several reaction zones at a total pressure of between 5 and 30 bar, using a synthesis gas with a CO/H2 molar ratio of between 1:4 and 1:1000. The total pressure in the subsequent reaction zone or zones is respectively 1 to (G1−Gf) bar lower than that of the preceding reaction zone, whereby G1 represents the total pressure in the respective preceding reaction zone and Gf represents the total pressure in the respective reaction zone that succeeds said first reaction zone or zones, with the proviso that the difference between G1 and Gf is greater than 1 bar and the partial CO pressure in the subsequent reaction zone or zones is respectively lower than that of the preceding reaction zone.

    摘要翻译： 本发明涉及通过在包含4至20个碳原子并含有具有内部双键的α-烯烃和烯烃的烯烃组合物的均质相中的异构化加氢甲酰化来连续生产含有5至21个碳原子的醛的方法， 在与含有氧原子和/或氮原子的有机磷配体和游离配体络合的均匀的铑催化剂的存在下，通过合成气。 所述生产在由至少两个反应区组成的多级反应体系中在高温高压下进行。 根据所述方法，首先使用具有CO / H 2 O 2的合成气在第一反应区或一组几个第一反应区中以10至40巴的总压力反应烯烃组合物， 的摩尔比在4:1和1:2之间，直到获得40-95％的α-烯烃转化率。 然后使用具有CO / H 2的合成气使来自第一反应区或几个第一反应区的组的加氢甲酰化产物在随后的反应区或几个反应区的组中以5至30巴的总压力反应， 1摩尔比为1:4-1:1000。 后续反应区域或区域中的总压力分别比前述反应区域低1〜（G1-Gf）巴，由此G1表示前述反应区域中的总压力，Gf表示相应的 所述第一反应区或区域成功的反应区，条件是G 1和G f之间的差大于1巴，并且后续反应区或区中的部分CO压力分别低于前述反应区。

    Method for producing phosphabenzene compounds
    25.
    发明授权
    Method for producing phosphabenzene compounds 失效
    膦酸化合物的制备方法

    公开(公告)号：US06255532B1

    公开(公告)日：2001-07-03

    申请号：US09509672

    申请日：2000-03-30

    申请人： Rocco Paciello ,  Edgar Zeller ,  Bernhard Breit ,  Michael Röper

    发明人： Rocco Paciello ,  Edgar Zeller ,  Bernhard Breit ,  Michael Röper

    IPC分类号： C07F950

    CPC分类号： C07F9/6568 ,  B01J31/2419 ,  B01J31/2461 ,  B01J2231/321 ,  B01J2531/822 ,  B01J2531/845

    摘要： A process for the preparation of phosphabenzene compounds of the formulae I and II where R1 to R6, independently of one another, are hydrogen, COOM SO3M, NR3X, NR2, OR, COOR or SR, where M is hydrogen, NH4 or an alkali metal, X is an anion, R is hydrogen, C1-6-alkyl, or C1-12-alkyl, C6-12-aryl, C7-12-aralkyl or C3-6-heterocycloalkyl having 1 to 3 heteroatoms which may be substituted by the above radicals or linked to form fused rings, and —W— is a bridge comprising a covalent bond, an oxo group, a sulfur group, an amino group, a di-C1-6-alkylsilicon group or a C1-16-radial, which may be part of one or more linked cyclic or aromatic rings and may be interrupted by 1 to 3 heteroatoms, where the phosphabenzene ring o- or m-position not bonded to the bridge may carry one of the radicals R1 to R6, with the exception of bis-3,3′-(2,4,6-triphenyl-3-phosphabenzene)-1,1-biphenyl, by reacting corresponding pyrilium salts with PH3 in the presence of a catalytic amount of acid and in the presence or absence of a solvent or diluent, where the pyrilium salts are mixed with PH3 at above 0° C. and reacted at from 0° C. to 200° C. and at a pressure greater than 1 bar.

    摘要翻译： 制备式I和II的膦酸化合物的方法，其中R 1至R 6彼此独立地为氢，COOM SO 3 M，NR 3 X，NR 2，OR，COOR或SR，其中M为氢，NH 4或碱金属， X是阴离子，R是氢，C 1-6 - 烷基或C 1-12 - 烷基，C 6-12 - 芳基，C 7-12 - 芳烷基或具有1至3个杂原子的C 3-6 - 杂环烷基，其可以被 并且-W-是包含共价键，氧代基团，硫基团，氨基基团，二-C1-6烷基硅基团或C1-16-放射状核团的桥， 其可以是一个或多个连接的环状或芳香环的一部分，并且可以被1至3个杂原子中断，其中未键合到桥的膦酰基环或 - 位置可以携带基团R1至R6中的一个，其中 通过使相应的吡啶鎓盐与PH 3在催化量的酸的存在下反应，并在存在或不存在下，将双-3'' - （2,4,6-三苯基-3-苯基苯基） 没有溶剂或稀释剂，其中吡啶鎓盐在0℃下与PH3混合，并在0℃至200℃和大于1巴的压力下反应。

    Preparation of n-butyraldehyde and/or n-butanol
    26.
    发明授权
    Preparation of n-butyraldehyde and/or n-butanol 失效
    正丁醛和/或正丁醇的制备

    公开(公告)号：US5892125A

    公开(公告)日：1999-04-06

    申请号：US793480

    申请日：1997-07-23

    申请人： Jurgen Kanand ,  Michael Roper ,  Rocco Paciello ,  Alfred Thome

    发明人： Jurgen Kanand ,  Michael Roper ,  Rocco Paciello ,  Alfred Thome

    IPC分类号： C07C27/00 ,  C07B61/00 ,  C07C29/00 ,  C07C29/09 ,  C07C29/17 ,  C07C31/12 ,  C07C45/51 ,  C07C45/56 ,  C07C47/02 ,  C07D295/023

    CPC分类号： C07D295/023 ,  C07C29/00 ,  C07C45/516 ,  C07C45/56 ,  C07C45/562

    摘要： A process for the preparation of n-butyraldehyde and/or n-butanol, in whicha) 1,3-butadiene is caused to react with an amine of the formula IR.sup.1 R.sup.2 NH, I in which R.sup.1 and R.sup.2 independently denote hydrogen, optionally substituted aliphatic or cycloaliphatic radicals, or aryl or aralkyl radicals or are linked to form a bridging member which can contain hetero atoms, at elevated temperature and under superatmospheric pressure in the presence of a compound of a Group VIIIb element and in the presence of an alkali metal amide or a basic metal oxide to form a mixture of the adducts of the formulas II ##STR1## and III ##STR2## b) the adduct III is isomerized to the adduct II, c) the adduct II is isomerized in the presence of a homogeneous or heterogeneous transition metal element catalyst in the liquid phase or in the presence of a heterogeneous catalyst containing a transition metal element in the gaseous phase to form the enamine of the formula IV ##STR3## and d) n-butyraldehyde and/or n-butanol is/are produced from this enamine.

    摘要翻译： PCT No.PCT / EP95 / 03358 Sec。 371日期1997年7月23日 102（e）日期1997年7月23日PCT 1995年8月24日PCT PCT。 出版物WO96 / 07630 日期：1996年3月14日制备正丁醛和/或正丁醇的方法，其中a）使1,3-丁二烯与式ⅠR1R2NH，Ⅰ的胺反应，其中R1和R2独立地为 表示氢，任选取代的脂族或脂环族基团，或芳基或芳烷基，或连接形成可含有杂原子的桥连构件，在高温和超大气压下，在VIIIb族元素的化合物存在下， 存在碱金属酰胺或碱性金属氧化物以形成式II II和III III的加合物的混合物b）加合物III异构化为加合物II，c）加合物II为 在均相或非均相过渡金属元素催化剂存在下在液相中或在气相中含有过渡金属元素的多相催化剂存在下异构化，形成式IV的烯胺IV和d）n -但 从该烯胺产生乙醛和/或正丁醇。

    Preparation of aldehydes
    27.
    发明授权
    Preparation of aldehydes 失效
    醛的制备

    公开(公告)号：US5387719A

    公开(公告)日：1995-02-07

    申请号：US120427

    申请日：1993-09-14

    申请人： Heinz-Josef Kneuper ,  Michael Roeper ,  Rocco Paciello

    发明人： Heinz-Josef Kneuper ,  Michael Roeper ,  Rocco Paciello

    IPC分类号： C07B61/00 ,  C07C45/50 ,  C07C47/02 ,  C07C45/00 ,  C07C45/78

    CPC分类号： B01J31/20 ,  B01J31/181 ,  B01J31/4046 ,  C07C45/50 ,  B01J2231/321 ,  B01J2531/822 ,  B01J2540/32 ,  B01J31/2234 ,  Y02P20/584

    摘要： A process for the preparation of aldehydes by hydroformylation of olefins having more than 7 carbon atoms, comprising hydroformylation by means of a rhodium catalyst dissolved homogeneously in the reaction medium, removal of the rhodium catalyst from the hydroformylation reaction product, and recycling of the rhodium separated off from the hydroformylation product into the hydroformylation step, in which the rhodium catalyst is extracted from the hydroformylation product into the aqueous phase by means of an aqueous solution of a nitrogen-containing complexing agent from the group comprising of sulfonated pyridines, sulfonated quinolines, substituted or unsubstituted, sulfonated or sulfonated substituent-carrying 2,2'-bipyridines, 1,10-phenanthrolines, 2,2'-biquinolines, 2,2',6',2"-terpyridines and porphines, and/or from the group comprising of carboxylated pyridines, carboxylated quinolines, substituted or unsubstituted, carboxylated or carboxylated substituent-carrying 2,2'-bipyridines, 1,10-phenanthrolines, 2,2'-biquinolines, 2,2',6',2"-terpyridines and porphines, and the aqueous, rhodium-containing extract is recycled into the hydroformylation step.

    摘要翻译： 一种通过使具有多于7个碳原子的烯烃的加氢甲酰化制备醛的方法，包括通过均匀地溶解在反应介质中的铑催化剂进行加氢甲酰化，从加氢甲酰化反应产物中除去铑催化剂，以及回收分离的铑 从加氢甲酰化产物进入加氢甲酰化步骤，其中通过含有磺化吡啶，磺化喹啉，取代的含氮络合剂的水溶液将铑催化剂从加氢甲酰化产物中提取到水相中 或未取代的磺化或磺化取代基的2,2'-联吡啶，1,10-菲咯啉，2,2'-二喹啉，2,2'，6'，2“ - 三联吡啶和卟吩，和/或 羧基化吡啶类，羧基化喹啉，取代或未取代的羧基化或羧基取代基的2,2'-二吡啶基 nes，1,10-菲咯啉，2,2'-二喹啉，2,2'，6'，2“ - 三联吡啶和卟吩，并将含水铑的提取物再循环到加氢甲酰化步骤中。

    Process for the preparation of formic acid
    28.
    发明授权
    Process for the preparation of formic acid 有权
    制备甲酸的方法

    公开(公告)号：US08901350B2

    公开(公告)日：2014-12-02

    申请号：US13171598

    申请日：2011-06-29

    申请人： Daniel Schneider ,  Klaus-Dieter Mohl ,  Martin Schäfer ,  Karin Pickenäcker ,  Stefan Rittinger ,  Thomas Schaub ,  Joaquim Henrique Teles ,  Rocco Paciello ,  Gerd Kaibel

    发明人： Daniel Schneider ,  Klaus-Dieter Mohl ,  Martin Schäfer ,  Karin Pickenäcker ,  Stefan Rittinger ,  Thomas Schaub ,  Joaquim Henrique Teles ,  Rocco Paciello ,  Gerd Kaibel

    IPC分类号： C07C51/44 ,  C07C51/09

    CPC分类号： C07C51/09 ,  C07C51/44 ,  C07C53/02

    摘要： Process for obtaining formic acid by thermal separation of a stream comprising formic acid and a tertiary amine (I), in which a liquid stream comprising formic acid and a tertiary amine (I) in a molar ratio of from 0.5 to 5 is produced by combining tertiary amine (I) and a formic acid source, from 10 to 100% by weight of the secondary components present therein are separated off and formic acid is removed by distillation in a distillation apparatus at a bottom temperature of from 100 to 300° C. and a pressure of from 30 to 3000 hPa abs from the liquid stream obtained, the bottom discharge from the distillation apparatus being separated into two liquid phases and the upper liquid phase being recycled to the formic acid source and the lower liquid phase being recycled for separating off the secondary components and/or to the distillation apparatus.

    摘要翻译： 通过热分离包含甲酸和叔胺（I）的流来获得甲酸的方法，其中包含摩尔比为0.5至5的甲酸和叔胺（I）的液体流通过组合 分离叔胺（I）和甲酸源，10至100重量％存在于其中的次要组分，并在蒸馏装置中在100-300℃的底部温度下蒸馏除去甲酸。 从得到的液体流中的压力为30〜3000hPa abs，将来自蒸馏装置的底部排出物分离成两液相，将上液相再循环至甲酸源，将下液相回收分离 脱离第二组分和/或蒸馏装置。

    Process for preparing formamides and formic esters
    29.
    发明授权
    Process for preparing formamides and formic esters 失效
    甲酰胺和甲酸酯的制备方法

    公开(公告)号：US08703994B2

    公开(公告)日：2014-04-22

    申请号：US13559011

    申请日：2012-07-26

    申请人： Thomas Schaub ,  Rocco Paciello ,  Marek Pazicky ,  Giuseppe Fachinetti ,  Debora Preti

    发明人： Thomas Schaub ,  Rocco Paciello ,  Marek Pazicky ,  Giuseppe Fachinetti ,  Debora Preti

    IPC分类号： C07C69/02 ,  C07C67/00 ,  C07C233/00

    CPC分类号： C07C231/10 ,  C07C67/36 ,  C07C233/03 ,  C07C69/06

    摘要： A process for preparing carboxylic acid derivatives of the formula H—(C═O)—R, R is OR1 or NR2R3, R1 is optionally substituted C1-C15-alkyl, C5-C10-cycloalkyl, C5-C10-heterocyclyl, C5-C10-aryl or C5-C10-heteroaryl, substituents are C1-C15-alkyl, C1-C6-alkoxy, C5-C10-cycloalkyl or C5-C10-aryl; R2 and R3 are independently hydrogen or optionally substituted C1-C15-alkyl, C5-C10 cycloalkyl, C5-C10-heterocyclyl, C5-C10-aryl or C5-C10-heteroaryl, substituents are selected from the group consisting of C1-C15-alkyl, C5-C10-cycloalkyl and C5-C10-aryl or R2 and R3 together with the nitrogen atom form a five- or six-membered ring which optionally comprises one or more heteroatoms selected from O, S and N and bearing the substituent R4, R4 is hydrogen or C1-C6-alkyl; by reacting a reaction mixture comprising carbon dioxide, hydrogen and an alcohol of the formula R1—OH or an amine of the formula NHR2R3 in the presence of a catalyst comprising gold at a pressure from 0.2 to 30 MPa and a temperature from 20 to 200° C. in a hydrogenation reactor.

    摘要翻译： 制备式H-（C = O）-R的羧酸衍生物的方法，R是OR 1或NR 2 R 3，R 1是任选取代的C 1 -C 15 - 烷基，C 5 -C 10 - 环烷基，C 5 -C 10 - 杂环基， C 10 - 芳基或C 5 -C 10 - 杂芳基，取代基是C 1 -C 15 - 烷基，C 1 -C 6 - 烷氧基，C 5 -C 10 - 环烷基或C 5 -C 10 - 芳基; R 2和R 3独立地为氢或任选取代的C 1 -C 15 - 烷基，C 5 -C 10环烷基，C 5 -C 10 - 杂环基，C 5 -C 10 - 芳基或C 5 -C 10 - 杂芳基，取代基选自C 1 -C 15 - 烷基，C 5 -C 10 - 环烷基和C 5 -C 10 - 芳基或R 2和R 3与氮原子一起形成五元或六元环，其任选地包含一个或多个选自O，S和N的杂原子并带有取代基R4 R4是氢或C1-C6-烷基; 在包含金的催化剂的存在下，在0.2〜30MPa的压力和20〜200℃的温度下，使包含二氧化碳，氢气和式R 1 -OH的醇或式NHR 2 R 3的胺的反应混合物反应， C.在氢化反应器中。