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    • 83. 发明授权
    • Hydrodealkylation process with promoted group vib metals and promoters
    • 具有促进族VIB金属和促进剂的水解方法
    • US3760023A
    • 1973-09-18
    • US3760023D
    • 1971-04-26
    • ASHLAND OIL INC
    • KOVACH SPATRICK RKMECAK R
    • B01J23/24C07C4/18B01J11/06C07C3/58
    • B01J23/24C07C4/18C07C2521/04C07C2523/02C07C2523/04C07C2523/12C07C2523/24
    • A process for the hydrodealkylation of alkyl-substituted aromatic hydrocarbons, including contacting the alkyl-substituted aromatic hydrocarbons with a catalyst comprising a metal of Group VIB of the Periodic System, such as chromium, molybdenum, and tungsten, and mixtures thereof, in an amount of about 5 to 15 per cent by weight of the finished catalyst, and a promoter selected from the group consisting of alkali metals, alkaline earth metals, rare earth metals, and mixtures thereof, such as potassium, rubidium, cesium, calcium, strontium, barium, cerium, thorium, etc., in an amount between about 1 to 10 percent by weight of the finished catalyst, at a temperature of about 1,050* to 1,200*F, a pressure of about 100 to 1,000 psig., a liquid hourly space velocity of about 0.1 to 5, and a hydrogento-hydrocarbon mole ratio between about 3 and 15 to 1.
    • 烷基取代芳烃的加氢脱烷基化方法,包括使烷基取代的芳族烃与包含周期性体系的VIB族金属如铬,钼和钨的催化剂及其混合物的催化剂,其量为 约5至15重量%的成品催化剂,以及选自碱金属,碱土金属,稀土金属及其混合物的助催化剂,例如钾,铷,铯,钙,锶, 钡,铈,钍等,其量为成品催化剂重量的约1-10%,温度为约1050°至1200°F,压力为约100至1,000psig,液体小时 空间速度为约0.1至5,氢与烃的摩尔比为约3至15比1。
    • 84. 发明授权
    • Hydrodealkylation process with catalyst of group vib metals promoted by tin oxide or lead oxide
    • 用氧化锡或铅氧化物促进的VIB族金属催化剂的氢化方法
    • US3679768A
    • 1972-07-25
    • US3679768D
    • 1968-10-22
    • ASHLAND OIL INC
    • KMECAK RONALD AKOVACH STEPHEN MPATRICK RALPH E
    • B01J21/06B01J23/14B01J23/26C07C4/18C07C3/58B01J11/06
    • B01J21/06B01J23/14B01J23/26C07C4/18C07C2521/04C07C2523/02C07C2523/04C07C2523/10C07C2523/24C07C2523/40C07C2523/74
    • A process for the hydrodealkylation of alkyl-substituted aromatic hydrocarbons, including contacting the alkyl-substituted aromatic hydrocarbons with a catalyst comprising a metal of Group VIB of the Periodic System, such as chromium, molybdenum and tungsten, in an amount from about 5 to 15 percent by weight based on the finished catalyst and a promoter comprising a metal of Group IVA of the Periodic System, such as tin and lead, in an amount between about 1 to 15 percent by weight of the final catalyst, both deposited on an inert oxide support, such as gamma aluminas, silica-alumina, magnesia-alumina, etc., at a temperature of about 1,050* to 1,200* F, a pressure of about 100 to 1,000 psig., a liquid hourly space velocity of about 0.1 to 5 and a hydrogen-to-hydrocarbon mole ratio between about 3 and 15 to 1. A second promoting agent selected from the Group consisting of alkali metals, alkaline earth metals, and rare earth metals, such as potassium, rubidium, cesium, calcium, strontium, barium, cerium, thorium, etc., may also be deposited on the carrier.
    • 烷基取代的芳烃的加氢脱烷基化方法,包括使烷基取代的芳族烃与包含周期系的第VIB族金属如铬,钼和钨的金属的催化剂接触,其量为约5至15 基于成品催化剂的重量百分比和包含周期性体系的IVA族金属的助催化剂,例如锡和铅,其量为最终催化剂的约1至15重量%,均沉积在惰性氧化物上 载体,例如γ氧化铝,二氧化硅 - 氧化铝,氧化镁 - 氧化铝等,温度约为1050°-1200°F,压力为约100-1000psig,液时空速为约0.1至5 氢和烃的摩尔比为约3至15:1。选自碱金属,碱土金属和稀土金属如钾,铷,铯,钙,锶的第二促进剂 铁,钡,铈,钍等也可以沉积在载体上。