摘要:
The invention relates to a method for separating a mixture containing at least one carboxylic acid vinyl ester of general formula R'-C(O)O-CH=CH 2 and at least one carboxylic acid of general formula R'-COOH, wherein R' in either case can be an aliphatic group having 12 to 22 C atoms or a cycloaliphatic group having 12 to 22 C atoms, or an aromatic group having 12 to 22 C atoms, and R' can be identical or different, characterized in that the carboxylic acid is converted to its anhydride R'-C(O)-O-C(O)-R' and the carboxylic acid vinyl ester is subsequently separated.
摘要:
The present invention provides a process for the production of an alkenyl carboxylate by reacting an alkene, a carboxylic acid and a molecular oxygen-containing gas in a reaction zone in the presence of a catalyst at an elevated reaction temperature, T, to produce an outlet stream from the reaction zone comprising alkenyl carboxylate and oxygen, and wherein in said process the catalyst is contacted with the alkene, at a partial pressure, P, optionally in the presence of the carboxylic acid, and the outlet stream comprises less than 2vo1 % oxygen, the improvement comprises reducing the partial pressure of the alkene and/or reducing the reaction temperature so as to suppress formation of benzene and/or suppress inhibition of the catalyst.
摘要:
The invention provides a process for preparing unsaturated carboxylic esters by means of reaction of alkenes having 2 to 6 carbon atoms with alkanecarboxylic acids having 1 to 6 carbon atoms in the presence of an oxygenous gas and in the presence of a heterogeneous noble metal catalyst by means of a continuous homogeneous gas phase process in a reactor, wherein a gaseous phase (cycle gas) is circulated, and the cycle gas is laden with alkanecarboxylic acid in an acid saturator before entry into the reactor, characterized in that, in a presaturator connected upstream of the acid saturator, the cycle gas is laden with a portion of the amount of alkanecarboxylic acid used for saturation, then it is transferred to the acid saturator and laden there with the remaining amount of alkanecarboxylic acid.
摘要:
The present invention relates to a method for producing vinyl esters of carboxylic acids by reacting a carboxylic acid with an alkyne composition in the presence of a catalyst, which is selected from salts of perrhenic acid, at a temperature of ≤ 250°C. The method produces the desired vinyl esters in high yields
摘要:
An integrated process for the production of an alkenyl carboxylate, such as vinyl acetate which process comprises the steps of (a) contacting in an oxidation reaction zone a C2 to C4 alkane, such as ethane, a molecular oxygen-containing gas, optionally the corresponding alkene and optionally water, in the presence of a catalyst to produce a stream comprising alkene, carboxylic acid and water; (b) separating at least a portion of the stream from step (a) into a fraction comprising the alkene and a fraction comprising the carboxylic acid and water; (c) contacting in a second reaction zone at least a portion of said alkene fraction produced in step (b), a carboxylic acid and a molecular oxygen-containing gas, in the presence of a catalyst to produce a product stream comprising an alkenyl carboxylate, water and carboxylic acid; (d) separating at least a portion of the product stream from step (c) and at least a portion of the carboxylic acid and water fraction produced in step (b) by azeotropic distillation into an overhead fraction comprising the alkenyl carboxylate and a base fraction comprising the carboxylic acid; (e) recovering the alkenyl carboxylate from the overhead fraction separated in step (d).
摘要:
The invention relates to a supported catalyst which contains palladium and/or compounds thereof, gold and/or compounds thereof, alkali metal compounds and also vanadium and/or compounds thereof. The invention also relates to the use of said supported catalyst for producing vinyl acetate from acetic acid, ethylene and oxygen, or gases containing oxygen.
摘要:
Die Erfindung betrifft ein Verfahren zur katalytischen Durchführung von Mehrphasenreaktionen in einem Rohrreaktor, wobei der Katalysator in der kontinuierlichen Phase und mindestens ein Edukt in einer dispergierten Phase enthalten ist und der Belastungsfaktor B des Rohrreaktors gleich oder größer 0,8 ist. Das Verfahren ist besonders zur Herstellung von Vinylestern durch Reaktion von Carbonsäuren mit Acetylen geeignet. Die Vinylester finden zur Herstellung von Homo- oder Copolymerisaten Verwendung.