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Hydrogenation of benzene-dicarboxylic acid esters, on a supported catalyst, to the corresponding cyclohexane derivatives with very high selectivity and yields

机译:在负载型催化剂上将苯二羧酸酯加氢成相应的环己烷衍生物,具有很高的选择性和收率

摘要

The hydrogenation of esters of benzene-dicarboxylic acids is carried out on supported catalysts containing a Sub-Group VIIII metal on a macroporous support. A process for the hydrogenation of benzene-dicarboxylic acid ester(s) with hydrogen in presence of a supported catalyst containing Sub-Group VIII metal(s) on a macroporous support. If the ester is dimethyl terephthalate, this excludes hydrogenation on a catalyst containing ruthenium, with or without Sub-Group I, VII or VIII metal(s), on a support with an average pore diameter (APD) of at least 50 nm and a BET surface of not more than 30 m2/g, with an active metal content of 0.01-30 wt.% and a ratio of (active metal surface):(support surface) of less than 0.05, and/or on a catalyst containing 0.01-30 wt.% active metal(s) as above on a support in which 10-50 vol.% of the pores consist of macropores with a diameter of 50-10,000 nm and 50-90 vol.% consist of mesopores with a diameter of 2-50 nm.
机译:苯-二羧酸酯的氢化反应是在大孔载体上的,含有第VIIII族金属的载体上进行的。在大孔载体上,在含有第VIII族金属的负载型催化剂存在下,用氢将苯-二羧酸酯氢化的方法。如果酯是对苯二甲酸二甲酯,则不包括在平均孔径(APD)至少为50 nm的载体上,含有或不含有I,VII或VIII族金属的钌催化剂上的氢化反应。 BET表面不超过30 m 2 / g,活性金属含量为0.01-30 wt。%,(活性金属表面):(支撑表面)之比小于0.05,和/或在在载体上含有0.01-30wt。%的一种或多种活性金属的催化剂,其中10-50vol。%的孔由直径为50-10,000nm的大孔组成,而50-90vol。%的孔由中孔​​组成直径为2-50 nm。

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