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    • 10. 发明授权
    • Process for preparation of anthraquinones and fluorenones
    • 制备蒽醌和芴酮的方法
    • US4822527A
    • 1989-04-18
    • US134839
    • 1987-12-14
    • David E. JamesNeal R. Nowicki
    • David E. JamesNeal R. Nowicki
    • C07C50/18C07C45/00
    • C07C50/18Y02P20/584
    • A process is disclosed for producing cyclized aromatic compounds by the liquid-phase air oxidation of 2-methyl-substituted biphenyls and diphenylmethanes in an acetic acid medium in the presence of a cobalt-manganese-bromine catalyst or a zirconium-cobalt-manganese-bromine catalyst wherein the mole ratio of cobalt-to-manganese is about 1.0:0.1 to about 1.0:10.0 and the ratio of zirconium-to-cobalt is about 0.005:1.0 to about 0.20:1.0, and mole ratio of bromine to total metals of said cobalt-manganese-bromine catalyst or zirconium-cobalt-manganese-bromine catalyst is from about 0.2:1.0 to about 20.0:1.0, which process comprises conducting the reaction in a batch process at a temperature of from 75.degree. C. to about 250.degree. C. at a pressure of from 1 to 100 atmospheres, or continuously in two stages comprising a first-stage reaction at a temperature of about 75.degree. C. to about 200.degree. C. and a second-stage reaction at a temperature of about 150.degree. C. to about 250.degree. C. and recycling the cobalt-manganese catalyst or the zircnium-cobalt-manganese catalyst by oxalate precipitation of the catalyst at temperatures of about 110.degree. C. to about 200.degree. C. prior to the separation of mother liquor and using about 0.25 to about 2.5 moles of oxalic acid per mole of cobalt and manganese or mole of zirconium-cobalt-manganese and continuously recycling the recovered catalyst metals to the oxidation stages. The products of this novel process, anthraquinones and fluorenones, are useful for the manufacture of dyestuffs and pharmaceuticals.
    • 公开了在钴锰溴催化剂或锆 - 钴 - 锰 - 溴存在下,通过在乙酸介质中通过2-甲基取代的联苯和二苯基甲烷的液相空气氧化来生产环化芳族化合物的方法 催化剂,其中钴与锰的摩尔比为约1.0:0.1至约1.0:10.0,锆与钴的摩尔比为约0.005:1.0至约0.20:1.0,溴与总金属的摩尔比为 所述钴 - 锰 - 溴催化剂或锆 - 钴 - 锰 - 溴催化剂的量为约0.2:1.0至约20.0:1.0,该方法包括在75℃至约250℃的间歇过程中进行反应 在1〜100个大气压的压力下,或者在约75℃至约200℃的温度下包括第一阶段反应的两个阶段的连续两个阶段,以及在约 150℃至约250℃并回收 钴锰催化剂或锆 - 钴 - 锰催化剂,在母液分离之前,在约110℃至约200℃的温度下草酸盐沉淀催化剂,并使用约0.25至约2.5摩尔的草酸 每摩尔钴和锰或摩尔的锆 - 钴 - 锰,并将回收的催化剂金属连续循环到氧化阶段。 该新方法的产物,蒽醌和芴酮可用于制造染料和药物。