ZEOLITE CATALYZED PROCESS FOR THE AMINATION OF PROPYLENE OXIDE

    公开(公告)号:US20220401933A1

    公开(公告)日:2022-12-22

    申请号:US17777759

    申请日:2020-11-19

    Applicant: BASF SE

    Abstract: The present invention relates to a process for the conversion of propylene oxide to 1-amino-2-propanol and/or di(2-hydroxypropyl)amine comprising (i) providing a catalyst comprising a zeolitic material comprising YO2 and optionally comprising X2O3 in its framework structure, wherein Y is a tetravalent element and X is a trivalent element, wherein the zeolitic material has a framework-type structure selected from the group consisting of MFI and/or MEL, including MEL/MFI intergrowths; (ii) providing a mixture in the liquid phase comprising propylene oxide and ammonia; (iii) contacting the catalyst provided in (i) with the mixture in the liquid phase provided in (ii) for converting propylene oxide to 1-amino-2-propanol and/or di(2-hydroxypropyl)amine.

    METHOD FOR PRODUCING ETHANOLAMINES AND/OR ETHYLENEAMINES

    公开(公告)号:US20200079725A1

    公开(公告)日:2020-03-12

    申请号:US16469782

    申请日:2017-12-07

    Applicant: BASF SE

    Abstract: The present invention relates to a process for preparing ethanolamines and/or ethyleneamines in the gas phase by reacting ethylene glycol with ammonia in the presence of an amination catalyst. It is a characteristic feature of the process that the amination catalyst is prepared by reducing a calcined catalyst precursor comprising an active composition, where the active composition comprises one or more active metals selected from the group consisting of the elements of groups 8, 9, 10 and 11 of the Periodic Table of the Elements and optionally one or more added catalyst elements selected group consisting of the metals and semimetals of groups 3 to 7 and 12 to 17, the element P and the rare earth elements. It is a further characteristic feature of the process that a catalyst precursor having low basicity is used, the low basicity being achieved in that a) the catalyst precursor is prepared by coprecipitation and the active composition additionally comprises one or more basic elements selected from the group consisting of the alkali metals and alkaline earth metals; or b) the catalyst precursor, as well as the active composition, additionally comprises a support material and is prepared by impregnating the support material or precipitative application onto the support material and the support material comprises one or more basic elements selected from the group consisting of the alkali metals, Be, Ca, Ba and Sr or one or more minerals selected from the group consisting of hydrotalcite, chrysotile and sepiolite; or c) the catalyst precursor, as well as the active composition, additionally comprises a support material and is prepared by impregnating the support material or precipitative application onto the support material and the active composition of the catalyst support comprises one or more basic elements selected from the group consisting of the alkali metals and the alkaline earth metals; or d) the catalyst precursor is calcined at temperatures of 600° C. or more; or e) the catalyst precursor is prepared by a combination of variants a) and d) or by a combination of variants b) and d) or by a combination of variants c) and d).

    PROCESS FOR PRODUCING NYLON-6,6
    30.
    发明申请
    PROCESS FOR PRODUCING NYLON-6,6 审中-公开
    生产尼龙-6,6的工艺

    公开(公告)号:US20160347908A1

    公开(公告)日:2016-12-01

    申请号:US15103468

    申请日:2014-12-12

    Applicant: BASF SE

    CPC classification number: C08G69/26 C08G69/28

    Abstract: The present invention relates to a process for producing nylon-6,6 by a) providing a muconic acid starting material selected from muconic acid, esters of muconic acid, lactones of muconic acid and mixtures thereof, b) subjecting the muconic acid starting material provided in step a) at least to some extent to a reaction with hydrogen in the presence of at least one hydrogenation catalyst Hb) to give adipic acid, c1) subjecting the muconic acid starting material provided in step a) to some extent to a reaction with hydrogen in the presence of at least one hydrogenation catalyst Hc1) to give 1,6-hexanediol, or c2) subjecting the adipic acid obtained in step b) to some extent to a reaction with hydrogen in the presence of at least one hydrogenation catalyst Hc2) to give 1,6-hexanediol, d) subjecting the 1,6-hexanediol obtained in step c1) or c2) to amination in the presence of an amination catalyst to obtain hexamethylenediamine, e) subjecting the hexamethylenediamine obtained in step d) and at least a portion of the adipic acid obtained in step b) to polycondensation to obtain nylon-6,6.

    Abstract translation: 本发明涉及一种通过以下方法生产尼龙-6,6的方法:a)提供选自粘康酸,粘康酸的粘蛋白的酸,粘康酸的内酯及其混合物的粘康酸起始材料,b)使提供的粘康酸起始物料 在步骤a)至少在一定程度上与至少一种氢化催化剂Hb)存在下的氢反应得到己二酸,c1)使步骤a)中提供的粘酸原料在一定程度上与 在至少一种氢化催化剂Hc1存在下进行氢化)得到1,6-己二醇,或c2)在步骤b)中获得的己二酸在一定程度上与至少一种氢化催化剂Hc2存在下的氢反应 ),得到1,6-己二醇,d)在胺化催化剂存在下使步骤c1)或c2)中得到的1,6-己二醇进行胺化得到六亚甲基二胺,e)使步骤d)中得到的六亚甲基二胺 和步骤b)中获得的至少一部分己二酸进行缩聚以获得尼龙-6,6。

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