A PROCESS FOR PURIFYING PROPYLENE OXIDE

    公开(公告)号:MY190769A

    公开(公告)日:2022-05-12

    申请号:MYPI2018002334

    申请日:2017-07-19

    Applicant: BASF SE

    Abstract: The present invention is related to a process for purifying propylene oxide, comprising (i) providing a stream (S0) comprising propylene oxide, acetonitrile, water, and an organic compound comprising a carbonyl group -C(=O)-, wherein said organic compound comprising a carbonyl group -C(=O)- comprises one or more of acetone and propionaldehyde; (ii) separating propylene oxide from the stream (S0) by distillation, comprising subjecting the stream (S0) to distillation conditions in a distillation column, obtaining a gaseous top stream (S1c) which is enriched in propylene oxide compared to the stream (S0), a liquid bottoms stream (S1a) which is enriched in acetonitrile and water compared to the stream (S0), and a side stream (S1b) comprising propylene oxide which is enriched in the carbonyl compound compared to the stream (S0); wherein the distillation column is operated at an absolute pressure at the top of the distillation column in the range of from 0.01 to 0.2 MPa (0.1 to 2.0 bar) and an internal reflux ratio in the range of from 2.0 to 6.0; wherein the distillation column exhibits at least 100 theoretical trays, the rectifying section of the distillation column consists of from 30 to 70 % of the theoretical trays and the stripping section of the distillation column consists of from 70 to 30 % of the theoretical trays. (Fig.1)

    POST-TREATMENT OF DEBORONATED ZEOLITE BETA

    公开(公告)号:MY185228A

    公开(公告)日:2021-04-30

    申请号:MYPI2015001014

    申请日:2013-10-09

    Applicant: BASF SE

    Abstract: A process for the post-treatment of a zeolitic material having a BEA framework structure, the process comprising (i) providing a zeolitic material having a BEA framework structure, wherein the framework structure of the zeolitic material comprises X203 and Y02, wherein Y is a tetravalent element and X is a trivalent element and wherein the molar ratio X203 : Y02 is greater than 0.02 : 1; (ii) treating the zeolitic material provided in (i) with a liquid solvent system thereby obtaining a zeolitic material having a molar ratio X203 : Y02 of at most 0.02 : 1, and at least partially separating the zeolitic material from the liquid solvent system; (iii) treating the zeolitic material obtained from (ii) with a liquid aqueous system having a pH in the range of 5.5 to 8 and a temperature of at least 75 ?C.

    POST-TREATMENT OF A ZEOLITIC MATERIAL

    公开(公告)号:ZA201503392B

    公开(公告)日:2019-12-18

    申请号:ZA201503392

    申请日:2015-05-15

    Applicant: BASF SE

    Abstract: A process for the post-treatment of a zeolitic material, the process comprising (i) providing a zeolitic material, wherein the framework structure of the zeolitic material comprises YO2 and X2O3, wherein Y is a tetravalent element and X is a trivalent element; (ii) subjecting the zeolitic material provided in (i) to a method comprising (a) treating the zeolitic material with an aqueous solution having a pH of at most 5, (b) treating the zeolitic material obtained from (a) with a liquid aqueous system having a pH in the range of 5.5 to 8 and a temperature of at least 75° C.; wherein in (ii) and after (b), the zeolitic material is optionally subjected to at least one further treatment according to (a) and/or at least one further treatment according to (b).

    Procedimiento para preparar óxido de propileno

    公开(公告)号:ES2730990T3

    公开(公告)日:2019-11-13

    申请号:ES14739188

    申请日:2014-07-16

    Abstract: Un proceso continuo para la preparación de óxido de propileno, que comprende: (i) proporcionar una corriente de alimentación de líquido que comprende propeno, peróxido de hidrógeno, acetonitrilo, agua, opcionalmente propano, y la al menos una sal de potasio disuelta de un oxiácido de fósforo; (ii) pasar la corriente de alimentación de líquido proporcionada en (i) a un reactor de epoxidación que comprende un catalizador que comprende una zeolita de titanio de estructura tipo MWW que comprende zinc y someter la corriente de alimentación de líquido a condiciones de reacción de epoxidación en el reactor de epoxidación, obteniendo una mezcla de reacción que comprende óxido de propileno, acetonitrilo, agua, la al menos una sal de potasio disuelta de un oxiácido de fósforo, opcionalmente propeno, y opcionalmente propano; (iii) eliminar una corriente efluente del reactor de epoxidación, comprendiendo la corriente efluente óxido de propileno, acetonitrilo, agua, al menos una porción de la al menos una sal de potasio disuelta de un oxiácido de fósforo, opcionalmente propeno, y opcionalmente propano, en donde la relación molar de potasio en relación con fósforo en la al menos una sal de potasio de un oxiácido de fósforo está en el intervalo de desde 0.6 hasta 1.4 y en donde si se emplean dos o más sales de potasio disueltas, la relación molar de potasio en relación con fósforo se define mediante la cantidad molar total de potasio de las sales disueltas en relación con la cantidad molar total de fósforo de las sales disueltas .

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