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    • 1. 发明授权
    • Process for removing metallic corrosion products from carbonylation
reactions carried out under anhydrous conditions
    • 从非强制性条件下运输的碳化反应中除去金属腐蚀产物的方法
    • US5124290A
    • 1992-06-23
    • US777066
    • 1991-10-16
    • Heinz ErpenbachReinhard GradlErhard JagersAndreas SeidelPeter Prinz
    • Heinz ErpenbachReinhard GradlErhard JagersAndreas SeidelPeter Prinz
    • B01J38/00C07B61/00C07C51/12C07C51/42C07C51/47C07C51/573C07C53/08C07C53/12
    • C07C51/573C07C51/47
    • A process for removing metallic corrosion products from carbonylation reactions which are carried out under anhydrous conditions and in which methyl acetate and/or methanol and/or dimethyl ether are reacted over a noble metal catalyst system which comprises a noble metal of group VIII of the periodic table of the elements, a co-catalyst, such as iodide or bromide, in particular methyl iodide, and a promoter, such as an organophosphonium or organoammonium salt, and if appropriate a lithium salt, to give acetic acid and/or acetic anhydride is described, the process comprisinga) bringing the reaction solution which is contaminated with metallic corrosion products and contains the catalyst system into contact with an ion exchanger;b) separating this reaction solution which has been brought into contact in this way from the ion exchanger;c) desorbing the promoter adsorbed on the ion exchanger before regeneration with acetic acid and/or acetic anhydride;d) combining the eluate obtained in step c) with the reaction solution separated off in step b) and recycling the components together into the carbonylation reaction;e) regenerating the ion exchanger obtained from step c) with a strong mineral acid; andf) washing the ion exchanger regenerated in this way with acetic acid and/or acetic anhydride until free from water, before use in step a).
    • 一种在无水条件下进行羰基化反应的金属腐蚀产物的方法,其中乙酸甲酯和/或甲醇和/或二甲醚在贵金属催化剂体系上反应,贵金属催化剂体系包含周期性的第VIII族贵金属 表中的元素,助催化剂如碘化物或溴化物,特别是甲基碘,以及促进剂如有机鏻盐或有机铵盐,以及如果合适的话,锂盐,得到乙酸和/或乙酸酐是 描述了该方法,该方法包括:a)将被金属腐蚀产物污染的反应溶液带入与离子交换器接触的催化剂体系; b)将已经以这种方式接触的反应溶液从离子交换器分离; c)在用乙酸和/或乙酸酐再生之前解吸吸附在离子交换剂上的促进剂; d)将步骤c)中获得的洗脱液与步骤b)中分离的反应溶液合并,并将组分一起再循环到羰基化反应中; e)用强无机酸再生步骤c)获得的离子交换剂; 以及f)在步骤a)中使用之前,用乙酸和/或乙酸酐洗涤离子交换剂,直至不含水再洗涤。
    • 7. 发明授权
    • Process for purifying and recovering the contaminated catalyst solution
arising in the carbonylation of methanol and/or methyl acetate and/or
dimethyl ether
    • 用于纯化和回收在甲醇和/或乙酸甲酯和/或二甲醚的羰基化中产生的污染的催化剂溶液的方法
    • US5002914A
    • 1991-03-26
    • US491352
    • 1990-03-09
    • Heinz ErpenbachWinfried LorkNorbert WeferlingPeter Prinz
    • Heinz ErpenbachWinfried LorkNorbert WeferlingPeter Prinz
    • B01J38/00B01J31/40C07B61/00C07C27/00C07C51/12C07C51/42C07C51/48C07C51/56C07C51/573C07C53/08C07C53/12C07C67/36C07C67/37C07C67/48C07C69/16
    • C07C51/56C07C51/12C07C51/42C07C51/48C07C51/573C07C67/48Y02P20/584
    • A process for purifying and recovering the contaminated catalyst solution arising from the carbonylation of methanol, methyl acetate and/or dimethyl ether. The solution contains carbonyl complexes of rhodium, quaternary organophosphorus compounds as organic promoters, undistillable organic impurities, and acetic acid, acetic anhydride and ethylidene diacetate. The carbonyl complex of rhodium together with acetic acid, acetic anhydride and ethylidene diacetate are extracted from the contaminated catalyst solution by using a tri-C.sub.3 - to C.sub.8 -alkylphosphine. The trialkylphosphine phase is separated from the promoter phase and is separated into the volatile constituents acetic acid, acetic anhydride and ethylidene diacetate as well as trialkylphosphine. The rhodium carbonyl complex remaining as the residue and the recovered trialkylphosphine is used for further extraction. The contaminated promoter phase is freed of the organic impurities by extraction with dialkyl ethers, carboxylic acid esters or hydrocarbons and, after the extractant phase has been separated off, is recombined with the recovered acetic acid/acetic anhydride and ethylidene diacetate mixture and with the rhodium carbonyl complex and recycled to the carbonylation reactor. The impurities remaining as the residue from a distillation of the extractant phase which has been separated off are removed from the system.
    • 一种纯化和回收由甲醇,乙酸甲酯和/或二甲醚羰基化产生的污染的催化剂溶液的方法。 该溶液含有铑羰基络合物,季有机磷化合物作为有机促进剂,不可渗透的有机杂质,以及乙酸,乙酸酐和亚乙基二乙酸酯。 通过使用三-C 3 -C 8烷基膦,从污染的催化剂溶液中提取铑与乙酸,乙酸酐和亚乙基二乙酸酯的羰基络合物。 将三烷基膦相与助催化剂相分离,并分离成挥发性成分乙酸,乙酸酐和亚乙基二乙酸酯以及三烷基膦。 剩余的作为残留物的铑羰基络合物和回收的三烷基膦用于进一步萃取。 被污染的促进剂相通过用二烷基醚,羧酸酯或烃萃取除去有机杂质,并且在萃取相分离后,与回收的乙酸/乙酸酐和亚乙基二乙酸酯混合物与铑重组 羰基络合物并循环到羰基化反应器中。 从分离出的萃取相的蒸馏中残留的杂质作为残留物从体系中除去。
    • 9. 发明授权
    • Process for making carboxylic acid halides
    • 制备羧酸卤化物的方法
    • US4414160A
    • 1983-11-08
    • US301984
    • 1981-09-14
    • Heinz ErpenbachKlaus GehrmannWinfried LorkPeter Prinz
    • Heinz ErpenbachKlaus GehrmannWinfried LorkPeter Prinz
    • C07C53/38C07C51/58
    • C07C51/58
    • The invention relates to the manufacture of carboxylic acid halides. To this end, an alkyl halide having from 1 to 6 carbon atoms or an aryl halide is reacted with carbon monoxide under practically anhydrous conditions at temperatures of 350 to 575 K. and under pressures of 1 to 300 bars in the presence of a catalyst system containing at least one of the noble metals selected from rhodium, palladium, iridium or their compounds, iodine and/or its compounds, methyl trialkyl phosphonium iodide and/or methyl triaryl phosphonium iodide, and optionally trialkyl phosphine oxide or triaryl phosphine oxide as well as an inert organic solvent. More specifically, the reaction mixture is admixed with 0.02 to 0.75 mol of hydrogen per mol of carbon monoxide.
    • 本发明涉及羧酸卤化物的制造。 为此,将具有1至6个碳原子的烷基卤或芳基卤化物在几乎无水条件下在350至575K的温度和1至300巴的压力下,在催化剂体系存在下与一氧化碳反应 含有选自铑,钯,铱或它们的化合物中的至少一种贵金属,碘和/或其化合物,碘化甲基三烷基碘和/或碘化三甲基三碘化鏻,和任选的三烷基氧化膦或三芳基氧化膦以及 惰性有机溶剂。 更具体地,将反应混合物与每摩尔一氧化碳0.02至0.75摩尔的氢气混合。