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    • 1. 发明授权
    • Process for producing carboxylic acids
    • 制备羧酸的方法
    • US06784313B2
    • 2004-08-31
    • US10263643
    • 2002-10-04
    • Chia Jung TsaiYao Lung LiuHsi Chin Tsai
    • Chia Jung TsaiYao Lung LiuHsi Chin Tsai
    • C07C5110
    • C07C51/12C07C53/08
    • A process for producing a carboxylic acid having (n+1) carbon atoms, which includes carbonylating an alcohol having n carbon atoms, and/or an ester of the alcohol and the carboxylic acid in each alkyl group with carbon monoxide in the presence of a catalytic system containing a rhodium catalyst. The process uses a reaction medium for the carbonylation that includes: (1) a rhodium catalyst, (2) an organic halide corresponding to said alcohol, (3) an ester of the alcohol and the carboxylic acid, (4) the carboxylic acid, optionally (5) water, a haloid acid, an inorganic halogen salt or an acetate, and (6) a cocatalyst selected from arginine, N-acetyl alanine, or nitrogen- and oxygen-containing organic compounds.
    • 一种具有(n + 1)个碳原子的羧酸的方法,该方法包括在每个烷基中羰基化具有n个碳原子的醇,和/或每个烷基中的醇和羧酸的酯与一氧化碳在一种 含有铑催化剂的催化体系。 该方法使用羰基化反应介质,其包括:(1)铑催化剂,(2)对应于所述醇的有机卤化物,(3)醇和羧酸的酯,(4)羧酸, 任选的(5)水,卤代酸,无机卤素盐或乙酸盐,和(6)选自精氨酸,N-乙酰丙氨酸或含氮和氧的有机化合物的助催化剂。
    • 2. 发明授权
    • Method for preparing acetic acid and/or methyl acetate by isomerization and carbonylation
    • 通过异构化和羰基化制备乙酸和/或乙酸甲酯的方法
    • US06395927B1
    • 2002-05-28
    • US09142175
    • 1998-09-23
    • Carl PatoisRobert PerronDaniel Thiebaut
    • Carl PatoisRobert PerronDaniel Thiebaut
    • C07C5110
    • C07C51/353C07C67/293C07C53/08C07C69/14
    • A method for preparing acetic acid and/or methyl acetate by simultaneous isomerization and carbonylation reactions. A reaction mixture is provided containing at least one reagent which provides formyl radicals and at least one further reagent which provides methyl radicals, together with water in an amount of at most 5% by weight, carbon monoxide at a partial pressure between 0.1·105 Pa and 25·105 Pa, a solvent and a catalytic system which contains at least one halogenated promoter and at least one iridium-based compound. In a typical reaction mixture, methyl formate is isomerized to form acetic acid according to the reaction: HCOOCH3CH3COOH while methanol undergoes carbonylation to form acetic acid according to the reaction: CH3OH+COCH3COOH The reagent which provides the formyl radicals is kept at or below 20% by weight of the reaction mixture, while the molar ratio of methyl radicals to formyl radicals in the mixture is greater than 1.
    • 通过同时异构化和羰基化反应制备乙酸和/或乙酸甲酯的方法。 提供了含有至少一种提供甲酰基的试剂和至少一种其它试剂的反应混合物,所述试剂在0.1.105Pa的分压下,以至多5重量%的量与水一起提供一氧化碳 和25.105Pa,溶剂和含有至少一种卤化助催化剂和至少一种铱基化合物的催化体系。 在典型的反应混合物中,甲酸甲酯根据反应异构化形成乙酸,而甲醇根据反应进行羰基化形成乙酸:提供甲酰基的试剂保持在或低于20%(重量) 反应混合物中甲基与甲酰基的摩尔比大于1。
    • 3. 发明授权
    • Process for the preparation of a carboxylic acid
    • 制备羧酸的方法
    • US06444844B1
    • 2002-09-03
    • US09817810
    • 2001-03-20
    • Abdul Majeed SeayadJayasree SeayadRaghunath Vitthal Chaudhari
    • Abdul Majeed SeayadJayasree SeayadRaghunath Vitthal Chaudhari
    • C07C5110
    • C07C51/14C07C51/10C07C51/12C07C57/30C07C59/64C07C53/126
    • The present invention relates to a process for the preparation of a carboxylic acid of the formula III, wherein R1 is aryl, substituted aryl, naphthyl, substituted naphthyl or alkyl, R2, R3, R4 and R5 are independently hydrogen or alkyl, by reacting the corresponding olefin of formula I or the corresponding organic halide or alcohol of the formula II, wherein R1 is selected from the group consisting of aryl, substituted aryl, naphthyl, substituted naphthyl or alkyl, R2, R3, R4 and R5 are independently hydrogen or alkyl and X is a halogen atom or a —OH group, using a novel water soluble palladium complex catalyst of general formula IV wherein R1, R2 and R3 are substituents on the phosphine ligand and selected from the group consisting of alkyl, aryl, arylalkyl, and cycloaliphatic, at least one of which carries a sulfonic acid and salts thereof, X is aryl or alkyl sulfonato or aryl or alkyl carboxylate or formato or a halide, is an anionic chelating ligand containing a N donor and O— group.
    • 本发明涉及一种制备式Ⅲ羧酸的方法,其中R1是芳基,取代的芳基,萘基,取代的萘基或烷基,R2,R3,R4和R5独立地是氢或烷基, 式I的相应的烯烃或式II的相应的有机卤化物或醇,其中R 1选自芳基,取代的芳基,萘基,取代的萘基或烷基,R 2,R 3,R 4和R 5独立地是氢或烷基 并且X是卤素原子或-OH基团,使用新的通式IV的水溶性钯络合物催化剂,其中R 1,R 2和R 3是膦配体上的取代基,并且选自烷基,芳基,芳基烷基和环脂族 ,其中至少一个携带磺酸及其盐,X是芳基或烷基磺酸根或芳基或烷基羧酸酯或格式或卤素,是含有N供体和O-基团的阴离子螯合配体。
    • 4. 发明授权
    • Process for monitoring a continuous acetic acid and/or methyl acetate production
    • 用于监测连续乙酸和/或乙酸甲酯生产的方法
    • US06642413B2
    • 2003-11-04
    • US09950819
    • 2001-09-13
    • Daniel Thiebaut
    • Daniel Thiebaut
    • C07C5110
    • C07C67/36C07C51/12C07C67/37C07C53/08C07C69/14
    • A continuous preparative process, including monitoring production, for acetic acid, methyl acetate or a mixture thereof, by carbonylation, in an industrial installation, of methanol or a carbonylatable derivative of methanol with carbon monoxide in a liquid phase in the presence of water and a homogeneous catalyst system. In a reaction zone I, the carbonylation is carried out in the liquid phase at a temperature of 150 to 250° C., under a pressure of 5·105 to 200·105 Pa and with venting of part of a gaseous canopy above a liquid phase level in said reactor. Then, in a vaporization or flash zone II, a liquid originating from the zone I at a pressure below that of zone I is partially vaporized to form a liquid fraction which is recycled into the reactor, and in a purification zone III, a vaporized fraction originating from flash zone II is distilled on a distillation column. At an outlet of the column, the product is recovered, other constituents of the vaporized fraction being at least partially recycled into said reactor. In the process, the reactor temperature and feed rate of the methanol or carbonylatable derivative in said reactor are brought under control of the carbon monoxide feed rate and of at least one of the parameters defining the composition of the reaction medium, or of the venting or of both the reaction medium and of the venting.
    • 一种连续的制备方法,包括在工业装置中通过羰基化,乙酸,乙酸甲酯或它们的混合物在甲醇或甲醇的可羰基化衍生物与一氧化碳在液体存在下在水和 均相催化剂体系。 在反应区域I中,羰基化在液相中在150〜250℃的温度下,在5.10〜5.0×10 5 Pa的压力下进行,并且将部分气体顶盖排出 在所述反应器中的液相水平。 然后,在蒸发或闪蒸区域II中,来自区域I的压力低于区域I的液体的液体被部分蒸发以形成再循环到反应器中的液体馏分,并且在净化区域III中,蒸发馏分 来自闪蒸区II的蒸馏塔在蒸馏塔上蒸馏。 在塔的出口处,产物被回收,蒸发馏分的其它组分至少部分地再循环到所述反应器中。 在此过程中,所述反应器中的甲醇或羰基化衍生物的反应器温度和进料速率受到一氧化碳进料速率以及限定反应介质的组成或排放或 的反应介质和排气。