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    • 3. 发明授权
    • High performance VPO catalyst and process of preparation thereof
    • 高性能VPO催化剂及其制备方法
    • US5773382A
    • 1998-06-30
    • US775938
    • 1997-01-03
    • Scott F. MitchellRobert A. KeppelMichael J. Mummey
    • Scott F. MitchellRobert A. KeppelMichael J. Mummey
    • C07D307/60B01J27/198B01J35/00B01J35/10B01J37/00B01J37/08C07B61/00C07C51/21C07C51/215C07C51/25
    • C07C51/252B01J23/002B01J27/198B01J37/0018C07C51/215C07C51/25B01J2523/00B01J35/0026B01J35/1014B01J35/108B01J37/08
    • An activated porous phosphorus/vanadium oxide catalyst adapted for the catalytic oxidation of a hydrocarbon to produce a carboxylic acid anhydride. The catalyst comprises a shaped body having a volume of at least about 0.02 cc, a phosphorus content of between about 1.05 and about 1.20, a B.E.T. surface area of at least about 15 m.sup.2 /g, an average vanadium oxidation state of between about 4.06 and about 4.3, a total pore volume of at least about 0.15 cc/g, a normalized apparent shaped body density of between about 1.0 and about 2.0 g/cc, and a crush strength of at least about 4 pounds. At least about 20% of the pore volume of the catalyst is constituted of pores having a diameter between about 0.1 and about 3.3 .mu.M, and at least about 40% of the pore volume is constituted of pores having a diameter of less than about 0.1 .mu.M. The catalyst is prepared by mixing a particulate phosphorus/vanadium oxide precursor with a pore modification agent to produce a modified catalyst precursor composition, forming the modified precursor composition into a predetermined shape, and removing the pore modification agent substantially at a temperature below 300.degree. C., preferably using air as a stripping gas.
    • 一种活化的多孔磷/氧化钒催化剂,适于催化氧化烃以产生羧酸酐。 催化剂包括具有至少约0.02cc的体积,约1.05至约1.20的磷含量的成形体,B.E.T. 表面积至少约15m 2 / g,平均钒氧化态在约4.06与约4.3之间,总孔体积至少约0.15cc / g,归一化表观体密度在约1.0至约2.0之间 g / cc,压碎强度至少约4磅。 催化剂的孔体积的至少约20%由直径在约0.1至约3.3μm之间的孔构成,并且至少约40%的孔体积由直径小于约0.1的孔构成 通过将颗粒状磷/钒氧化物前体与孔改性剂混合以制备改性催化剂前体组合物,将改性前体组合物形成预定形状并基本上在低于下述温度下除去孔改性剂来制备催化剂 300℃,优选使用空气作为汽提气体。
    • 5. 发明授权
    • High productivity process for the production of maleic anhydride
    • 用于生产马来酸酐的高生产率工艺
    • US6005121A
    • 1999-12-21
    • US58029
    • 1998-04-10
    • Jerry R. EbnerRobert A. KeppelMichael J. Mummey
    • Jerry R. EbnerRobert A. KeppelMichael J. Mummey
    • B01J8/06B01J27/198B01J35/02C07C51/215C07C51/54C07C57/145C07D307/60
    • C07C51/215B01J23/002B01J27/198B01J35/026B01J8/06B01J8/067B01J2208/00026B01J2208/00044B01J2208/0007B01J2208/00212B01J2208/00539B01J2208/00548B01J2523/00
    • An improved process for the manufacture of maleic anhydride by catalytic oxidation of a nonaromatic hydrocarbon having at least four carbon atoms in a straight chain, in which a gas containing oxygen and hydrocarbon is passed through a fixed catalyst bed in a tubular reactor. The activity of the catalyst bed is graded in such manner that the reactor can be operated at an initial (feed gas) hydrocarbon concentration of over 1.5% by volume, an integrated average temperature difference between gas and cooling fluid of at least about 15.degree. C. over that portion of the bed in which the gas temperature exceeds the cooling fluid temperature, and a productivity of at least about 5.0 lbs. maleic anhydride per hour, without the temperature difference between the gas and the cooling fluid exceeding 80.degree. C. at any point in the catalyst bed during the course of the reaction. Preferably, the catalyst activity and the gas permeability of the bed vary in the direction of gas flow so that both the catalyst activity and the pressure drop per unit distance are lower in a critical region, where the combination of temperature and hydrocarbon concentration could otherwise cause the reaction to proceed at an excessive rate, than they are in a region of low temperature and low hydrocarbon concentration. Significant and unexpected improvement in reactor performance is achieved by the combination of a graded catalyst charge and incorporation of a catalyst modifying organophosphorus compound in the hydrocarbon feed.
    • 通过在直链中具有至少四个碳原子的非芳族烃的催化氧化制备马来酐的改进方法,其中含有氧和烃的气体通过管式反应器中的固定催化剂床。 催化剂床的活性以这样的方式分级,使得反应器可以以超过1.5体积%的初始(进料气体)烃浓度操作,气体和冷却流体之间的一体化平均温差为至少约15℃ 在其中气体温度超过冷却流体温度的床的那部分上,并且生产率至少约为5.0磅。 马来酸酐/小时,在反应过程中,在催化剂床中的任何点处,气体和冷却流体之间的温差不超过80℃。 优选地,床的催化剂活性和气体渗透性在气流方向上变化,使得催化剂活性和每单位距离的压降在临界区域较低,其中温度和烃浓度的组合可能会导致 反应以比低温和低碳氢化合物浓度的区域高的速度进行。 反应器性能的显着和意想不到的改进通过将分级催化剂装料和在烃进料中掺入催化剂改性有机磷化合物的组合来实现。
    • 8. 发明授权
    • High performance VPO catalyst and process of preparation thereof
    • 高性能VPO催化剂及其制备方法
    • US5641722A
    • 1997-06-24
    • US306489
    • 1994-09-15
    • Scott F. MitchellRobert A. KeppelMichael J. Mummey
    • Scott F. MitchellRobert A. KeppelMichael J. Mummey
    • C07D307/60B01J27/198B01J35/00B01J35/10B01J37/00B01J37/08C07B61/00C07C51/21C07C51/215C07C51/25
    • C07C51/252B01J23/002B01J27/198B01J37/0018C07C51/215C07C51/25B01J2523/00B01J35/0026B01J35/1014B01J35/108B01J37/08
    • An activated porous phosphorus/vanadium oxide catalyst adapted for the catalytic oxidation of a hydrocarbon to produce a carboxylic acid anhydride. The catalyst comprises a shaped body having a volume of at least about 0.02 cc, a phosphorus content of between about 1.05 and about 1.20, a B.E.T. surface area of at least about 15 m.sup.2 /g, an average vanadium oxidation state of between about 4.06 and about 4.3, a total pore volume of at least about 0.15 cc/g, a normalized apparent shaped body density of between about 1.0 and about 2.0 g/cc, and a crush strength of at least about 4 pounds. At least about 20% of the pore volume of the catalyst is constituted of pores having a diameter between about 0.1 and about 3.3 .mu.M, and at least about 40% of the pore volume is constituted of pores having a diameter of less than about 0.1 .mu.M. The catalyst is prepared by mixing a particulate phosphorus/vanadium oxide precursor with a pore modification agent to produce a modified catalyst precursor composition, forming the modified precursor composition into a predetermined shape, and removing the pore modification agent substantially at a temperature below 300.degree. C., preferably using air as a stripping gas.
    • 一种活化的多孔磷/氧化钒催化剂,适于催化氧化烃以产生羧酸酐。 催化剂包括具有至少约0.02cc的体积,约1.05至约1.20的磷含量的成形体,B.E.T. 表面积至少约15m 2 / g,平均钒氧化态在约4.06与约4.3之间,总孔体积至少约0.15cc / g,归一化表观体密度在约1.0至约2.0之间 g / cc,压碎强度至少约4磅。 催化剂的孔体积的至少约20%由直径在约0.1至约3.3μm之间的孔构成,并且至少约40%的孔体积由直径小于约0.1的孔构成 通过将颗粒状磷/钒氧化物前体与孔改性剂混合以制备改性催化剂前体组合物,将改性前体组合物形成预定形状并基本上在低于下述温度下除去孔改性剂来制备催化剂 300℃,优选使用空气作为汽提气体。