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    • 15. 发明授权
    • Catalysts and their preparation
    • 催化剂及其制备
    • US4504590A
    • 1985-03-12
    • US453474
    • 1982-12-27
    • Michael J. DesmondMarc A. Pepera
    • Michael J. DesmondMarc A. Pepera
    • B01J23/745B01J29/14B01J37/04C07C1/04B01J29/34
    • B01J37/04B01J23/745B01J29/146C07C1/0445C07C2521/18C07C2529/072
    • Catalysts comprising a medium to large port zeolite modified by the oxide or acid of an element selected from the group consisting of Group IIIA to VIIA elements and, a Fischer-Tropsch catalyst wherein the ratio of zeolite to Fischer-Tropsch component is from about 0.1 to 50:1 can be employed to produce fuel grade saturated gaseous hydrocarbons from synthesis gas. A process is employed which includes the step of contacting synthesis gas over the foregoing catalyst at a reaction temperature of from about 100.degree. C. to 500.degree. C. and at a pressure of from about one atmosphere (0.1 MPa) to about 200 atmospheres (20 MPa) and at a gas hourly space velocity of from about 10 to 100,000. A method is also provided for the preparation of the combination catalyst. The catalyst and process for its use results in a small liquid aromatic product also being formed which is suitable for forming gasoline. Olefins and oxygenates are essentially eliminated.
    • 包含由选自IIIA至VIIA族元素的元素的氧化物或酸改性的中等至大口沸石的催化剂,以及费 - 托催化剂,其中沸石与费 - 托成分的比例为约0.1至 50:1可用于从合成气中生产燃料级饱和气态烃。 使用的方法包括在约100℃至500℃的反应温度和约1个大气压(约0.1MPa)至约200个大气压(压力)下将合成气与上述催化剂接触的步骤 20MPa),气时空速为10〜10万左右。 还提供了用于制备组合催化剂的方法。 用于其使用的催化剂和方法导致还形成适于形成汽油的小液体芳族化合物。 基本上消除了烯烃和含氧化合物。
    • 18. 发明授权
    • Process for the reductive deposition of polyoxometallates
    • 多金属氧酸盐还原沉积工艺
    • US4634502A
    • 1987-01-06
    • US769557
    • 1985-08-26
    • James L. CallahanMichael J. DesmondMarc A. Pepera
    • James L. CallahanMichael J. DesmondMarc A. Pepera
    • B01J37/34C25D9/08C25D3/00C25D13/02
    • B01J37/348C25D9/08
    • A process for the reductive deposition of polyoxometallate complexes on supports. The process includes the steps of forming a solution of at least one polyoxometallate compound in a solvent, said compound having the formula A.sub.a (L.sub.l M.sub.m J.sub.z O.sub.y), adding a quantity of a support material having electronic conductivity to the solution, charging the solution containing the support material to an electrolytic cell in contact with the cathode thereof, the cell having a separate compartment for the anode, passing a current of from about 0.1 to about 500 mA/cm.sup.2 of electrode area through the cell whereby the support material receives a deposit of a polyoxometallate wherein the average oxidation state of the metals therein has been reduced to a valence greater than zero and, thereafter separating and recovering the support material carrying the reduced metallate complex.
    • 多金属氧酸盐配合物在载体上还原沉积的方法。 该方法包括以下步骤:在溶剂中形成至少一种多金属氧酸盐化合物的溶液,所述化合物具有式Aa(L1MmZzOy),向溶液中加入一定量的具有电子导电性的载体材料,将含有载体材料的溶液 到与阴极接触的电解池中,电池具有用于阳极的单独的隔室,使约0.1至约500mA / cm 2的电极面积的电流通过电池,由此支撑材料接收多金属氧酸盐沉积物 其中金属中的平均氧化态已经降低到大于零的价态,然后分离和回收载有还原的金属化合物的载体材料。
    • 19. 发明授权
    • Novel catalysts and their preparation and process for the production of
saturated gaseous hydrocarbons
    • 新型催化剂及其制备和制备饱和气态烃的方法
    • US4568698A
    • 1986-02-04
    • US652893
    • 1984-09-21
    • Michael J. DesmondMarc A. Pepera
    • Michael J. DesmondMarc A. Pepera
    • B01J23/745B01J29/14B01J37/04C07C1/04
    • B01J37/04B01J23/745B01J29/146C07C1/0445C07C2521/18C07C2529/072
    • Catalysts comprising a medium to large port zeolite modified by the oxide or acid of an element selected from the group consisting of Group IIIA to VIIA elements and, a Fischer-Tropsch catalyst wherein the ratio of zeolite to Fischer-Tropsch component is from about 0.1 to 50:1 can be employed to produce fuel grade saturated gaseous hydrocarbons from synthesis gas. A process is employed which includes the step of contacting synthesis gas over the foregoing catalyst at a reaction temperature of from about 100.degree. C. to 500.degree. C. and at a pressure of from about one atmosphere (0.1 MPa) to about 200 atmospheres (20 MPa) and at a gas hourly space velocity of from about 10 to 100,000. A method is also provided for the preparation of the combination catalyst. The catalyst and process for its use results in a small liquid aromatic product also being formed which is suitable for forming gasoline. Olefins and oxygenates are essentially eliminated.
    • 包含由选自IIIA至VIIA族元素的元素的氧化物或酸改性的中等至大口沸石的催化剂,以及费 - 托催化剂,其中沸石与费 - 托成分的比例为约0.1至 50:1可用于从合成气中生产燃料级饱和气态烃。 使用的方法包括在约100℃至500℃的反应温度和约1个大气压(约0.1MPa)至约200个大气压(压力)下将合成气与上述催化剂接触的步骤 20MPa),气时空速为10〜10万左右。 还提供了用于制备组合催化剂的方法。 用于其使用的催化剂和方法导致还形成适于形成汽油的小液体芳族化合物。 基本上消除了烯烃和含氧化合物。