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    Process for the production of alumina suitable for use as a catalyst carrier
    1.
    发明授权
    Process for the production of alumina suitable for use as a catalyst carrier 失效
    用于生产适合用作催化剂载体的氧化铝的方法

    公开(公告)号：US4248852A

    公开(公告)日：1981-02-03

    申请号：US66869

    申请日：1979-08-15

    申请人： Motoyoshi Wakabayashi ,  Takeo Ono ,  Osamu Togari ,  Munekazu Nakamura

    发明人： Motoyoshi Wakabayashi ,  Takeo Ono ,  Osamu Togari ,  Munekazu Nakamura

    IPC分类号： B01J21/04 ,  B01J35/10 ,  C01F7/02 ,  C01F7/34

    CPC分类号： B01J21/04 ,  C01F7/02 ,  C01P2004/10 ,  C01P2004/50 ,  C01P2004/61 ,  C01P2006/12 ,  C01P2006/14

    摘要： Improved .gamma.-alumina suitable for use as a catalyst carrier having high mechanical strength, a large specific surface area, and a substantially uniform pore size distribution in a relatively small portion of the pore size range below 500 A. Said alumina is produced by first establishing a seed aluminum hydroxide hydrogel having a pH of between 6 and 10 and then repetitively and sequentially adding an aluminum compound to adjust the pH to less than 5 or more than 11 to dissolve crystallites of aluminum hydroxide followed by addition of a neutralizing agent to return the hydrogel to the pH range from about 6 to 10 to cause pseudo-boehmite crystallites to grow. After a sufficient number of repetitions of said sequential addition, sparse aggregates of crystallites of the desired structure are formed. These are dried and calcined to produce the said alumina.

    摘要翻译： 改进的γ-氧化铝适合用作具有高机械强度，大的比表面积，以及孔径尺寸范围在500A以下的较小部分中的基本均匀的孔径分布的催化剂载体。所述氧化铝是通过首先建立 pH为6〜10的酸式氢氧化铝水凝胶，然后重复依次加入铝化合物以将pH调节至小于5或大于11，以溶解氢氧化铝的微晶，然后加入中和剂以使 水凝胶至约6至10的pH范围，以使假勃姆石微晶生长。 在所述顺序添加的足够数量的重复之后，形成所需结构的微晶聚集体。 将它们干燥并煅烧以产生所述氧化铝。

    Method for hydrogenation of coal tar pitch
    2.
    发明授权
    Method for hydrogenation of coal tar pitch 失效
    煤焦油沥青加氢方法

    公开(公告)号：US4909923A

    公开(公告)日：1990-03-20

    申请号：US4168

    申请日：1987-01-15

    申请人： Hiroshi Okazaki ,  Tadashi Komoto ,  Munekazu Nakamura ,  Osamu Togari ,  Noriyuki Yoneda ,  Haruhiko Yoshida ,  Hideki Hashimoto

    发明人： Hiroshi Okazaki ,  Tadashi Komoto ,  Munekazu Nakamura ,  Osamu Togari ,  Noriyuki Yoneda ,  Haruhiko Yoshida ,  Hideki Hashimoto

    IPC分类号： B01J35/10 ,  C10C1/20 ,  C10G1/08 ,  C10C3/02

    CPC分类号： C10G1/086 ,  B01J23/881 ,  B01J23/882 ,  B01J27/19 ,  B01J35/0026 ,  B01J35/1019 ,  B01J35/1038 ,  B01J35/1042 ,  B01J35/1061 ,  C10C1/205

    摘要： A method for the hydrogenation of coal tar pitch which comprises subjecting said coal tar pitch containing toluene insolubles to slight hydrogenation in the presence of a hydrogenation catalyst having carried on a refractory inorganic oxide carrier at least one member selected from the class consisting of elemental metals, belonging to Groups VI B and VIII in the Periodic Table and oxides and sulfides thereof, under the conditions of 280.degree. to 400.degree. C. of reaction temperature, 20 to 200 kg/cm.sup.2. G of hydrogen pressure, 0.1 to 10 hr.sup.-1 of LHSV, and 500 to 2,000 Nl/liter of hydrogen to liquid ratio, and a catalyst therefor. The "slight" hydrogenation is hydrogenation to a degree such that the difference of hydrogen to carbon atomic ratio between the untreated coal tar pitch and the hydrogenated coal tar pitch falls in the range of 0.03 to 0.5. The coal tar pitch can be coal tar pitch itself, coal tar pitch pretreated for the removal of organic sodium compounds, or pretreated for the removal of quinoline insolubles and, preferably, the coal tar pitch has a density in the range of 1.13 to 1.17 g/cm.sup.2 at 40 degrees C.

    摘要翻译： 一种用于加氢煤焦油沥青的方法，其包括在载有无机氧化物载体的氢化催化剂存在下，将含有甲苯不溶物的所述煤焦油沥青进行轻微氢化，所述氢化催化剂至少包含一种选自元素金属， 属于周期表第VIB和VIII族，其氧化物和硫化物在280-400℃的条件下反应温度为20-200kg / cm2。 氢气压力，0.1〜10小时-1的LHSV和500〜2000Nl /升的氢液比，以及催化剂。 “轻微”氢化氢化至一定程度，使得未处理煤焦油沥青与氢化煤焦油沥青之间的氢与碳原子比的差值落在0.03至0.5的范围内。 煤焦油沥青本身可以是煤焦油沥青，预处理用于除去有机钠化合物的煤焦油沥青，或预处理以除去喹啉不溶物，优选煤焦油沥青的密度范围为1.13-1.17g / cm2，40℃

    Catalysts for hydrotreatment of heavy hydrocarbon oils containing asphaltenes
    7.
    发明授权
    Catalysts for hydrotreatment of heavy hydrocarbon oils containing asphaltenes 失效
    用于加氢处理含有沥青质的重质烃油的催化剂

    公开(公告)号：US4422960A

    公开(公告)日：1983-12-27

    申请号：US210059

    申请日：1980-12-14

    申请人： Yoshimi Shiroto ,  Takeo Ono ,  Sachio Asaoka ,  Munekazu Nakamura

    发明人： Yoshimi Shiroto ,  Takeo Ono ,  Sachio Asaoka ,  Munekazu Nakamura

    IPC分类号： B01J21/00 ,  B01J23/74 ,  B01J23/85 ,  B01J23/882 ,  B01J23/887 ,  B01J35/00 ,  B01J35/10 ,  C10G45/04 ,  C10G47/10 ,  C10G55/06 ,  C10G65/04 ,  C10G65/12 ,  B01J21/04 ,  B01J23/22 ,  B01J23/24 ,  B01J27/04

    CPC分类号： B01J23/882 ,  B01J23/85 ,  B01J23/8872 ,  B01J35/10 ,  B01J35/002 ,  B01J35/1019 ,  B01J35/1061 ,  B01J35/108 ,  C10G2300/107

    摘要： A catalyst for hydrotreating a heavy hydrocarbon oil containing asphaltenes comprises a porous carrier composed of one or more inorganic oxides of at least one element selected from among those of Groups II, III and IV of the Periodic Table, and at least one catalytic metal component composited with the carrier. The metal of the catalytic metal component is selected from among those of Groups VB, VIB, VIII and IB of the Periodic Table. The catalyst contains about 1 to 30% by weight of such catalytic metal component and has the following pore characteristics with regard to its pores having a diameter of 75 .ANG. or more: an average pore diameter APD of about 180 to 500 .ANG., a total pore volume PV, expressed in cc/g, being equal to or greater than a value X ##EQU1## the volume of pores with a diameter of about 180 to 500 .ANG. being at least about 0.2 cc/g, the volume of pores with a diameter of at least 1,500 .ANG. being not greater than about 0.03 cc/g, and a total surface area being at least about 60 m.sup.2 /g. The catalyst has an average catalyst diameter ACD, expressed in millimeters, of not greater than a value of the formula, ACD=(APD/100).sup.0.5. Disclosed also are a method of preparing such a catalyst, and a process for hydrotreating a heavy hydrocarbon oil containing asphaltenes in the presence of such a catalyst.

    摘要翻译： 用于加氢处理含有沥青质的重烃油的催化剂包括由一种或多种选自元素周期表II，III和IV族中的至少一种元素的一种或多种无机氧化物组成的多孔载体，以及至少一种催化金属组分 与承运人。 催化金属组分的金属选自元素周期表的VB，VIB，VIII和IB族。 该催化剂含有约1至30重量％的这种催化金属组分，并且对于其直径为75埃或更高的孔具有以下孔特性：平均孔径APD为约180至500安培姆，总孔 体积PV以cc / g表示，等于或大于直径为约180至500的孔的体积至少约0.2cc / g，具有直径的孔的体积 至少1500安培角不大于约0.03cc / g，总表面积为至少约60m 2 / g。 催化剂的平均催化剂直径ACD（以毫米表示）不大于式的值ACD =（APD / 100）0.5。 还公开了制备这种催化剂的方法，以及在这种催化剂存在下，对含有沥青质的重质烃油进行加氢处理的方法。

    Hydrotreatment of heavy hydrocarbon oils containing asphaltenes, and catalysts therefor
    8.
    发明授权
    Hydrotreatment of heavy hydrocarbon oils containing asphaltenes, and catalysts therefor 失效
    含沥青质的重质烃油的加氢处理及其催化剂

    公开(公告)号：US4444655A

    公开(公告)日：1984-04-24

    申请号：US428796

    申请日：1982-09-30

    申请人： Yoshimi Shiroto ,  Takeo Ono ,  Sachio Asaoka ,  Munekazu Nakamura

    发明人： Yoshimi Shiroto ,  Takeo Ono ,  Sachio Asaoka ,  Munekazu Nakamura

    IPC分类号： B01J21/00 ,  B01J23/74 ,  B01J23/85 ,  B01J23/882 ,  B01J23/887 ,  B01J35/00 ,  B01J35/10 ,  C10G45/04 ,  C10G47/10 ,  C10G55/06 ,  C10G65/04 ,  C10G65/12

    CPC分类号： B01J23/882 ,  B01J23/85 ,  B01J23/8872 ,  B01J35/10 ,  B01J35/002 ,  B01J35/1019 ,  B01J35/1061 ,  B01J35/108 ,  C10G2300/107

    摘要： A catalyst for hydrotreating a heavy hydrocarbon oil containing asphaltenes comprises a porous carrier composed of one or more inorganic oxides of at least one element selected from among those of Groups II, III and IV of the Periodic Table, and at least one catalytic metal component composited with the carrier. The metal of the catalytic metal component is selected from among those of Groups VB, VIB, VIII and IB of the Periodic Table. The catalyst contains about 1 to 30% by weight of such catalytic metal component and has the following pore characteristics with regard to its pores having a diameter of 75 .ANG. or more: an average pore diameter APD of about 180 to 500 .ANG., a total pore volume PV, expressed in cc/g, being equal to or greater than a value X ##EQU1## the volume of pores with a diameter of about 180 to 500 .ANG. being at least about 0.2 cc/g, the volume of pores with a diameter of at least 1,500 .ANG. being not greater than about 0.03 cc/g, and a total surface area being at least about 60 m.sup.2 /g. The catalyst has an average catalyst diameter ACD, expressed in millimeters, of not greater than a value of the formula, ACD=(APD/100).sup.0.5. Disclosed also are a method of preparing such a catalyst, and a process for hydrotreating a heavy hydrocarbon oil containing asphaltenes in the presence of such a catalyst.

    摘要翻译： 用于加氢处理含有沥青质的重烃油的催化剂包括由一种或多种选自元素周期表II，III和IV族中的至少一种元素的一种或多种无机氧化物组成的多孔载体，以及至少一种催化金属组分 与承运人。 催化金属组分的金属选自元素周期表的VB，VIB，VIII和IB族。 该催化剂含有约1至30重量％的这种催化金属组分，并且对于其直径为75埃或更高的孔具有以下孔特性：平均孔径APD为约180至500安培姆，总孔 体积PV以cc / g表示，等于或大于直径为约180至500的孔的体积至少约0.2cc / g，具有直径的孔的体积 至少1500安培角不大于约0.03cc / g，总表面积为至少约60m 2 / g。 催化剂的平均催化剂直径ACD（以毫米表示）不大于式的值ACD =（APD / 100）0.5。 还公开了制备这种催化剂的方法，以及在这种催化剂存在下，对含有沥青质的重质烃油进行加氢处理的方法。