Purification of alcohols prior to their use in the presence of an acid catalyst
    3.
    发明授权
    Purification of alcohols prior to their use in the presence of an acid catalyst 有权
    醇在使用前在酸催化剂存在下进行纯化

    公开(公告)号:US09000236B2

    公开(公告)日:2015-04-07

    申请号:US13131407

    申请日:2009-11-27

    摘要: Process for the purification of an alcohol in the course of a process comprising: (1) providing a reaction zone (C) comprising an acid type catalyst; (2) providing a reaction zone (B) comprising an acid adsorbent material; (3) providing an alcohol stream comprising impurities; (4) introducing the alcohol stream of (3) into the reaction zone (B) and bringing said stream into contact with the acid adsorbent material at conditions effective to reduce the amount of impurities having an adverse effect on the acid type catalyst of the reaction zone (C); (5) recovering from step (4) an alcohol stream and introducing it into the reaction zone (C); (6) optionally introducing one or more reactants (R) into the reaction zone (C); (7) operating said reaction zone (C) at conditions effective to recover a valuable effluent.

    摘要翻译: 在包括以下步骤的过程中醇的纯化方法:(1)提供包含酸型催化剂的反应区(C); (2)提供包含酸吸附材料的反应区(B); (3)提供包含杂质的醇流; (4)将(3)的醇流引入反应区(B)中,并使所述物流与酸吸附剂材料接触,有效地减少对反应的酸型催化剂具有不利影响的杂质的量 区(C); (5)从步骤(4)中回收醇流并将其引入反应区(C)中; (6)任选地将一种或多种反应物(R)引入反应区(C)中; (7)在有效回收有价值流出物的条件下操作所述反应区(C)。

    PURIFICATION OF ALCOHOLS PRIOR TO THEIR USE IN THE PRESENCE OF AN ACID CATALYST
    4.
    发明申请
    PURIFICATION OF ALCOHOLS PRIOR TO THEIR USE IN THE PRESENCE OF AN ACID CATALYST 有权
    在酸性催化剂存在下使用醇类物质的纯化

    公开(公告)号:US20110313213A1

    公开(公告)日:2011-12-22

    申请号:US13131407

    申请日:2009-11-27

    IPC分类号: C07C29/74

    摘要: Process for the purification of an alcohol in the course of a process comprising: (1) providing a reaction zone (C) comprising an acid type catalyst; (2) providing a reaction zone (B) comprising an acid adsorbent material; (3) providing an alcohol stream comprising impurities; (4) introducing the alcohol stream of (3) into the reaction zone (B) and bringing said stream into contact with the acid adsorbent material at conditions effective to reduce the amount of impurities having an adverse effect on the acid type catalyst of the reaction zone (C); (5) recovering from step (4) an alcohol stream and introducing it into the reaction zone (C); (6) optionally introducing one or more reactants (R) into the reaction zone (C); (7) operating said reaction zone (C) at conditions effective to recover a valuable effluent.

    摘要翻译: 在包括以下步骤的过程中醇的纯化方法:(1)提供包含酸型催化剂的反应区(C); (2)提供包含酸吸附材料的反应区(B); (3)提供包含杂质的醇流; (4)将(3)的醇流引入反应区(B)中,并使所述物流与酸吸附剂材料接触,有效地减少对反应的酸型催化剂具有不利影响的杂质的量 区(C); (5)从步骤(4)中回收醇流并将其引入反应区(C)中; (6)任选地将一种或多种反应物(R)引入反应区(C)中; (7)在有效回收有价值流出物的条件下操作所述反应区(C)。

    Production of Olefins
    5.
    发明申请
    Production of Olefins 审中-公开
    烯烃的生产

    公开(公告)号:US20100076240A1

    公开(公告)日:2010-03-25

    申请号:US12374811

    申请日:2007-07-13

    IPC分类号: C07C4/06

    摘要: A process for converting a hydrocarbon feedstock to provide an effluent containing light olefins, the process comprising passing a hydrocarbon feedstock, the feedstock containing at least 25 wt % C5+ paraffins, through a reactor containing a crystalline silicate catalyst to produce an effluent including propylene.

    摘要翻译: 一种用于转化烃原料以提供含有轻质烯烃的流出物的方法,该方法包括使含烃原料(含有至少25wt%的C 5+链烷烃的原料)通过含有结晶硅酸盐催化剂的反应器,以产生包含丙烯的流出物。

    Process for cracking an olefin-rich hydrocarbon feedstock
    6.
    发明授权
    Process for cracking an olefin-rich hydrocarbon feedstock 失效
    裂化烯烃富烃原料的方法

    公开(公告)号:US07375257B2

    公开(公告)日:2008-05-20

    申请号:US10398603

    申请日:2001-10-03

    IPC分类号: C07C4/02 C10G11/02

    CPC分类号: C10G11/16 C10G2400/20

    摘要: A process for cracking an olefin containing hydrocarbon feedstock which is selective towards light olefins in the effluent, the process comprising passing a hydrocarbon feedstock containing one or more olefins through a moving bed reactor containing a crystalline silicate catalyst selected from an MFI-type crystalline silicate having a silicon/aluminium atomic ratio of at least 180 and an MEL-type crystalline silicate having a silicon/aluminium atomic ration of from 150 to 800 which has been subjected to a steaming step, at an inlet temperature of from 500 to 600° C., at an olefin partial pressure of from 0.1 to 2 bars and the feedstock being passed over the catalyst at an LHSV of from 5 to 30 h−1 to produce an effluent with an olefin content of lower molecular weight than that of the feedstock, intermittently removing a first fraction of the catalyst from the moving bed reactor, regenerating the first fraction of the catalyst in a regenerator and intermittently feeding into the moving bed reactor a second fraction of the catalyst which has been regenerated in the regenerator, the catalyst regeneration rate being controlled whereby the propylene purity is maintained constant at a value corresponding to the average value observed in a fixed bed reactor using the same feedstock, catalyst and cracking conditions, for example at least 94 wt. %.

    摘要翻译: 一种用于裂解对流出物中的轻质烯烃具有选择性的含烯烃的原料的方法,该方法包括使含有一种或多种烯烃的烃原料通过含有结晶硅酸盐催化剂的移动床反应器,该结晶硅酸盐催化剂选自MFI型结晶硅酸盐, 入口温度为500-600℃的硅/铝原子比至少为180的硅/铝原子比为150〜800的MEL型结晶硅酸盐,其进行了蒸汽工序。 ,烯烃分压为0.1至2巴,原料以5至30小时-1的LHSV通过催化剂以产生具有较低分子量的烯烃含量的流出物 比原料间歇地从移动床反应器中除去催化剂的第一部分,在再生器中再生催化剂的第一馏分并间歇地进料 在移动床反应器中,在再生器中再生的催化剂的第二部分,控制催化剂再生速率,由此丙烯纯度保持恒定在与使用相同原料的固定床反应器中观察到的平均值的值 ,催化剂和裂化条件,例如至少94wt。 %。

    Polymer hydrogenation process
    7.
    发明申请
    Polymer hydrogenation process 失效
    聚合物加氢工艺

    公开(公告)号:US20050222342A1

    公开(公告)日:2005-10-06

    申请号:US10484484

    申请日:2002-07-16

    IPC分类号: C08C19/02 C08F8/04 C08F36/00

    CPC分类号: C08C19/02 C08F8/04

    摘要: A process for hydrogenating unsaturations in polymers, the process comprising contacting at least one polymer having unsaturations with a catalyst comprising at least one Group Ia, Ib, IIb, VIb, VIIb or VIII metal on a support of an alkaline earth metal silicate having a surface area of at least 30 m2/g at a temperature of from 50 to 250° C. and a pressure of from 5 to 150 bar.

    摘要翻译: 一种用于氢化聚合物中的不饱和度的方法,该方法包括使具有不饱和度的至少一种聚合物与包含至少一种Ia,Ib,IIb,VIb,VIIb或VIII族金属的催化剂接触在具有表面的碱土金属硅酸盐的载体上 在50至250℃的温度和5至150巴的压力下至少30m 2 / g的面积。

    Production of olefins
    8.
    发明授权
    Production of olefins 失效
    生产烯烃

    公开(公告)号:US06388161B1

    公开(公告)日:2002-05-14

    申请号:US09594282

    申请日:2000-06-15

    IPC分类号: C10G4702

    摘要: A process for cracking an olefin-rich hydrocarbon feedstock which is selective towards propylene in the effluent, the process comprising contacting a hydrocarbon feedstock containing one or more olefinic components of C4 or greater with a crystalline silicate catalyst to produce an effluent having a second composition of one or more olefinic components of C3 or greater, the feedstock and the effluent having substantially the same olefin content by weight therein characterized in that ethylene is added to the feedstock before the feedstock contacts the catalyst.

    摘要翻译: 一种用于裂解在流出物中对丙烯有选择性的富烯烃的原料的方法,该方法包括将含有一种或多种C4或更多烯烃组分的烃原料与结晶硅酸盐催化剂接触以产生具有第二组成的流出物 C3或更高的一种或多种烯烃组分,所述原料和流出物具有基本上相同的烯烃含量,其特征在于在原料接触催化剂之前将乙烯加入到原料中。

    Catalytic Conversion of Alkylaromatic Compounds
    10.
    发明申请
    Catalytic Conversion of Alkylaromatic Compounds 失效
    烷基芳族化合物的催化转化

    公开(公告)号:US20100130801A1

    公开(公告)日:2010-05-27

    申请号:US12374814

    申请日:2007-07-13

    IPC分类号: C07C4/18

    摘要: A process for catalytically converting alkylaromatic compounds in a hydrocarbon feedstock, the process comprising passing a hydrocarbon feedstock including at least one alkylaromatic compound, wherein the alkyl group comprises at least two carbon atoms, through a reactor containing a crystalline silicate catalyst to produce an effluent including at least one aromatic compound and at least one light olefin selected from C2 and C3 olefins.

    摘要翻译: 一种用于在烃原料中催化转化烷基芳族化合物的方法,该方法包括使包含至少一种烷基芳族化合物的烃原料(其中烷基包含至少两个碳原子)通过含有结晶硅酸盐催化剂的反应器,以产生流出物,其包括 至少一种芳族化合物和至少一种选自C2和C3烯烃的轻质烯烃。