Conversion of methane into larger organic hydrocarbons
    1.
    发明授权
    Conversion of methane into larger organic hydrocarbons 失效
    将甲烷转化为较大的有机碳氢化合物

    公开(公告)号:US4795843A

    公开(公告)日:1989-01-03

    申请号:US105930

    申请日:1987-10-08

    IPC分类号: C07C1/26 C07C11/20 C07C1/00

    摘要: Organic hydrocarbons which comprise useful compounds may be obtained in a two-step process utilizing methane as a feedstock. The desired compounds are prepared by treating said methane with a halogenating agent such as chlorine, followed by contacting the methyl halide with a conversion catalyst comprising a silicalite. The silicalite which is employed is a silica polymorph consisting of crystalline silica which, after calcination in air at a temperature of 600.degree. C. for 1 hour, has a mean refractory index of 1.39.+-.0.01 and a specific gravity at 25.degree. C. of 1.70.+-.0.05 g/cc.

    摘要翻译: 包含有用化合物的有机烃可以以使用甲烷为原料的两步法获得。 通过用卤化剂如氯处理所述甲烷,然后将甲基卤化物与包含硅沸石的转化催化剂接触来制备所需的化合物。 使用的硅沸石是由结晶二氧化硅组成的二氧化硅多晶型物,在空气中在600℃的温度下煅烧1小时后,其平均耐火指数为1.39 +/- 0.01,比重为25℃ 为1.70 +/- 0.05g / cc。

    Alkylation/transalkylation process
    2.
    发明授权
    Alkylation/transalkylation process 失效
    烷基化/烷基转移法

    公开(公告)号:US4857666A

    公开(公告)日:1989-08-15

    申请号:US247810

    申请日:1988-09-21

    IPC分类号: C07C2/70 C07C6/12 C07C15/02

    摘要: An alkylation-transalkylation process for the production of a monoalkylated aromatic compound is disclosed which maximizes the production of desirable monoalkylaromatic compounds, while limiting transalkylation catalyst deactivation. The process entails the combination of an alkylation reaction zone, a first seperation zone, a second separation zone, and a transalkylation reaction zone wherein the alkylation catalyst and transalkylation catalyst are dissimilar and where the alkylation catalyst is comprised of phosphoric acid material and the transalkylation catalyst is comprised of a crystalline aluminosilicate material. The transalkylation catalyst deactivation is reduced by transalkylating only dialkylated aromatic compounds. Additionally, the transalkylation catalyst is regenerable utilizing a hot liquid hydrocarbon wash.

    摘要翻译: 公开了用于制备单烷基化芳族化合物的烷基化 - 烷基转移方法,其使所需的单烷基芳族化合物的产生最大化,同时限制了烷基转移催化剂失活。 该方法需要烷基化反应区,第一分离区,第二分离区和烷基转移反应区的组合,其中烷基化催化剂和烷基转移催化剂是不相似的,其中烷基化催化剂由磷酸材料和烷基转移催化剂 由结晶硅铝酸盐材料组成。 通过仅烷基化二烷基化芳族化合物来降低烷基转移催化剂的失活。 另外,烷基转移催化剂可利用热液体烃洗涤再生。

    Shaped catalyst particles utilizable for the conversion of organic
compounds
    4.
    发明授权
    Shaped catalyst particles utilizable for the conversion of organic compounds 失效
    可用于转化有机化合物的成型催化剂颗粒

    公开(公告)号:US5043509A

    公开(公告)日:1991-08-27

    申请号:US395939

    申请日:1989-08-18

    摘要: Catalyst particles which are employed in reactions involving the conversion of organic compounds should possess a desired configuration in order to maintain a desired voidage which will permit passage of the feedstock through the catalyst bed during the conversion reaction. Solid phosphoric acid catalysts which comprise an admixture of an acid of phosphorus and a solid binder such as a siliceous material may be formed into polylobular, tubular, ridged, fluted, or channeled cylindrical particles which will permit a sufficient amount of voidage in the catalyst bed to be maintained even though the catalyst particles will swell during the reaction due to the formation of coke on the surface thereof.

    摘要翻译: 在涉及有机化合物转化的反应中使用的催化剂颗粒应具有所需的构型,以保持所需的空隙率,这将允许原料在转化反应期间通过催化剂床。 包含磷的酸和诸如硅质材料的固体粘合剂的混合物的固体磷酸催化剂可以形成为多叶状,管状,脊状,槽纹或通道的圆柱形颗粒,这将允许催化剂床中足够的空隙率 即使催化剂颗粒在反应期间由于在其表面上形成焦炭而溶胀而被保持。