Catalyst and process for producing aromatic compounds from C.sub.2 -C.sub.6
    1.
    发明授权
    Catalyst and process for producing aromatic compounds from C.sub.2 -C.sub.6 失效
    用于从C2-C6脂族烃生产芳族化合物的催化剂和方法

    公开(公告)号:US5169812A

    公开(公告)日:1992-12-08

    申请号:US760294

    申请日:1991-09-16

    IPC分类号: B01J29/40 C07C2/00

    摘要: A catalyst for converting C.sub.2 to C.sub.6 aliphatic hydrocarbons to aromatics is described. The catalyst contains a zeolite, an aluminum phosphate binder and a gallium component. Examples of zeolites which can be used are the ZSM family of zeolites, with ZSM-5 being a specific example. The catalyst is characterized in that it is tolerant to exposure to hydrogen at tempertures of about 500.degree. to about 700.degree. C. The catalyst's tolerance to hydrogen exposure is the result of treating the catalyst with an aqueous solution of a weakly acidic ammonium salt or a dilute acid solution at a temperature of about 50.degree. to about 100.degree. C. for a time of about 1 to about 48 hours, followed by calcination. A process for preparing the catalyst is also described.

    摘要翻译: 描述了将C2转化为C6脂族烃到芳族化合物的催化剂。 催化剂含有沸石,磷酸铝粘合剂和镓成分。 可以使用的沸石的实例是沸石的ZSM族,ZSM-5是具体的实例。 该催化剂的特征在于它在约500℃至约700℃的温度下耐受暴露于氢气。催化剂对暴露于氢的耐受性是用弱酸性铵盐或 稀酸溶液在约50℃至约100℃的温度下搅拌约1至约48小时,然后煅烧。 还描述了制备催化剂的方法。

    Process for producing aromatic compounds from C2-C6 aliphatic
hydrocarbons using a hydrogen tolerant catalyst
    2.
    发明授权
    Process for producing aromatic compounds from C2-C6 aliphatic hydrocarbons using a hydrogen tolerant catalyst 失效
    使用耐氢催化剂从C2-C6脂族烃生产芳族化合物的方法

    公开(公告)号:US5258564A

    公开(公告)日:1993-11-02

    申请号:US933129

    申请日:1992-08-21

    IPC分类号: B01J29/40 C07C2/00 C07C12/02

    摘要: A process for converting C.sub.2 to C.sub.6 aliphatic hydrocarbons to aromatics is described. The process uses a catalyst which contains a zeolite, an aluminum phosphate binder and a gallium component. Examples of zeolites which can be used are the ZSM family of zeolites, with ZSM-5 being a specific example. The catalyst is characterized in that it is tolerant to exposure to hydrogen at temperatures of about 500.degree. to about 700.degree. C. The catalyst's tolerance to hydrogen exposure is the result of treating the catalyst with an aqueous solution of a weakly acidic ammonium salt or a dilute acid solution at a temperature of about 50.degree. to about 100.degree. C. for a time of about 1 to about 48 hours, followed by calcination.

    摘要翻译: 描述了将C2转化为C6脂族烃至芳族化合物的方法。 该方法使用含有沸石,磷酸铝粘合剂和镓成分的催化剂。 可以使用的沸石的实例是沸石的ZSM族,ZSM-5是具体的实例。 催化剂的特征在于它在约500℃至约700℃的温度下耐受暴露于氢气。催化剂对暴露于氢的耐受性是用弱酸性铵盐或 稀酸溶液在约50℃至约100℃的温度下搅拌约1至约48小时,然后煅烧。

    Process for reactivating a deactivated dehydrocyclodimerization catalyst
    3.
    发明授权
    Process for reactivating a deactivated dehydrocyclodimerization catalyst 失效
    重新激活失活的脱氢环化二聚催化剂的方法

    公开(公告)号:US5212127A

    公开(公告)日:1993-05-18

    申请号:US790315

    申请日:1991-11-08

    IPC分类号: B01J29/90 B01J38/66 C07C2/76

    摘要: This invention relates to a process for reactivating a dehydrocyclodimerization catalyst. Dehydrocyclodimerization catalysts which contain an aluminum phosphate binder can be deactivated when they are exposed to hydrogen at temperatures above 500.degree. C. The instant process restores substantially all of the catalyst's lost activity. The process involves treating the catalyst with an aqueous solution of a weakly acidic ammonium salt or a dilute acid solution at a temperature of about 50.degree. to about 100.degree. C. for a time of about 1 to about 48 hours. An ammonium nitrate solution is preferred. Next the catalyst is calcined at a temperature of about 500.degree. to about 700.degree. C. for a time of about 1 to about 15 hours to provide a reactivated catalyst. The catalyst can be reactivated several times using this process.

    摘要翻译: 本发明涉及一种使脱氢环二聚化催化剂再活化的方法。 含有磷酸铝粘合剂的脱氢环化二聚催化剂在高于500℃的温度下暴露于氢气时可以失活。本工艺基本恢复所有催化剂的失活活性。 该方法包括在约50℃至约100℃的温度下用弱酸性铵盐或稀酸溶液的水溶液处理催化剂约1至约48小时。 优选硝酸铵溶液。 接下来,催化剂在约500至约700℃的温度下煅烧约1至约15小时,以提供再活化的催化剂。 使用该方法可以将催化剂重新活化数次。

    Production of alkyl aromatic compounds
    4.
    发明授权
    Production of alkyl aromatic compounds 失效
    烷基芳族化合物的生产

    公开(公告)号:US5003121A

    公开(公告)日:1991-03-26

    申请号:US399044

    申请日:1989-08-28

    摘要: Alkyl aromatic compounds may be prepared by reacting an aromatic compound with an alkylating agent such as an olefin in the presence of an alkylation catalyst. The alkylation catalyst of the present invention comprises a composite which has been prepared by coextruding a clay component and at least one multi-valent metal component in which the metal is selected from the group consisting of Groups IIIA, IIIB and IVB of the Periodic Table, followed by drying the resultant extrudate and calcination thereof. By utilizing a catalyst which has been prepared by this method in an alkylation reaction it is possible to obtain an improved alkylate selectivity.

    摘要翻译: 烷基芳族化合物可以通过在烷基化催化剂的存在下使芳族化合物与烷基化剂如烯烃反应来制备。 本发明的烷基化催化剂包括通过共挤出粘土组分和至少一种多价金属组分制备的复合材料,其中金属选自周期表的IIIA,IIIB和IVB族组, 然后干燥所得挤出物并进行煅烧。 通过利用在烷基化反应中通过该方法制备的催化剂,可以获得改进的烷基化物选择性。

    Novel motor fuel alkylation process
    6.
    发明授权
    Novel motor fuel alkylation process 失效
    新型汽油燃料烷基化工艺

    公开(公告)号:US4677245A

    公开(公告)日:1987-06-30

    申请号:US927462

    申请日:1986-11-06

    摘要: A novel hydrocarbon alkylation process is disclosed wherein the feed hydrocarbons are dried to maintain the water content of the alkylation catalyst at less than 2.0 wt. %, where said alkylation catalyst is comprised of a mineral acid and an ether component selected from the group consisting of tert-butyl ether, methylphenyl ether, tert amylmethyl ether (TAME), or methyl tert-butyl ether (MTBE). This process also incorporates a method of regenerating at least a portion of the alkylation catalyst to prevent build-up of more than 15 wt. % of polymer products therein.

    摘要翻译: 公开了一种新的烃烷基化方法,其中进料烃被干燥以将烷基化催化剂的水含量保持在小于2.0wt。 %,其中所述烷基化催化剂由无机酸和选自叔丁基醚,甲基苯基醚,叔戊基甲基醚(TAME)或甲基叔丁基醚(MTBE)的醚组分组成。 该方法还包括再生烷基化催化剂的至少一部分的方法,以防止累积超过15wt。 %的聚合物产品。

    Production of alkyl aromatic compounds
    8.
    发明授权
    Production of alkyl aromatic compounds 失效
    烷基芳族化合物的生产

    公开(公告)号:US5043511A

    公开(公告)日:1991-08-27

    申请号:US435103

    申请日:1989-11-13

    摘要: Alkyl aromatic compounds may be prepared by reacting an aromatic compound such as benzene with an alkylating agent such as an olefin or alkyl halide in the presence of an alkylation catalyst. The alkylation catalyst of the present invention comprises a clay which has been coextruded with a multi-valent metal and preferably a metal selected from the group consisting of Groups IIIA, IIIB and IVB of the Periodic Table. The resultant extrudate is then impregnated with a dissimilar multi-valent metal selected from the above named groups followed by calcination to form the desired composite. By utiilzing this catalytic composite in an alkylation reaction it is possible to obtain improved yields of alkyl aromatic compounds which may then be used in the preparation of biodegradable detergents.

    摘要翻译: 烷基芳族化合物可以通过芳族化合物如苯与烷基化剂如烯烃或烷基卤在烷基化催化剂的存在下反应来制备。 本发明的烷基化催化剂包括已经与多价金属共挤出的粘土,优选选自周期表的IIIA,IIIB和IVB族的金属。 然后将得到的挤出物用选自上述组的不同的多价金属浸渍,随后煅烧以形成所需的复合材料。 通过在烷基化反应中将该催化复合物实现,可以获得改进的烷基芳族化合物的产率,然后可以将其用于制备可生物降解的洗涤剂。

    Process for the desulfurization of a hydrocarbonaceous oil
    10.
    发明授权
    Process for the desulfurization of a hydrocarbonaceous oil 有权
    含烃油的脱硫方法

    公开(公告)号:US06171478B2

    公开(公告)日:2001-01-09

    申请号:US09365476

    申请日:1999-08-02

    IPC分类号: C10G1700

    CPC分类号: C10G67/14 C10G67/12

    摘要: A process for the desulfurization of hydrocarbonaceous oil wherein the hydrocarbonaceous oil is contacted with a hydrodesulfurization catalyst in a hydrodesulfurization reaction zone to reduce the sulfur level to a relatively low level and then contacting the resulting hydrocarbonaceous stream from the hydrodesulfurization zone with an oxidizing agent to convert the residual, low level of sulfur compounds into sulfur-oxidated compounds. The resulting hydrocarbonaceous oil stream containing the sulfur-oxidated compounds is separated after decomposing any residual oxidizing agent to produce a stream containing the sulfur-oxidated compounds and a hydrocarbonaceous oil stream having a reduced concentration of sulfur-oxidated compounds.

    摘要翻译: 烃类油的脱硫方法,其中烃类油与加氢脱硫反应区中的加氢脱硫催化剂接触,以将硫含量降低到相对较低的水平,然后使得到的来自加氢脱硫区的烃流与氧化剂接触以转化 残留,低水平的硫化合物变成硫氧化化合物。 在分解任何残留的氧化剂之后,分离含有硫氧化化合物的所得烃油流,以产生含有硫氧化化合物的流和具有降低的硫氧化化合物浓度的烃油流。