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CATALYST FOR FISCHER-TROPSCH SYNTHESIS, METHOD FOR PRODUCING CATALYST FOR FISCHER-TROPSCH SYNTHESIS, AND METHOD FOR PRODUCING HYDROCARBON
CATALYST FOR FISCHER-TROPSCH SYNTHESIS, METHOD FOR PRODUCING CATALYST FOR FISCHER-TROPSCH SYNTHESIS, AND METHOD FOR PRODUCING HYDROCARBON
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机译:用于费托合成的催化剂,用于生产费托合成的催化剂和用于生产烃的方法
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摘要
Provided is a catalyst for Fischer-Tropsch synthesis comprising a reduced product of an unreduced catalyst that contains: a carrier comprising silica and zirconium oxide; and cobalt oxide loaded on the carrier. The hydrogen adsorption amount per unit mass at 100°C is 0.60 ml/g or more. When the hydrogen consumption in the temperature range from the peak top to the peak end point of the main peak resulting from TPR measurement of the unreduced catalyst is denoted by C1 and the hydrogen consumption in the temperature range from the peak top to the peak end point of the main peak resulting from TPR measurement of the reduced product is denoted by C2, the ratio C2/C1 is 0.01-0.13.
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机译:提供了一种用于费-托合成的催化剂,其包含未还原的催化剂的还原产物,其包含:包含二氧化硅和氧化锆的载体;和和氧化钴负载在载体上。 100℃下的每单位质量的氢吸附量为0.60ml / g以上。当通过未还原催化剂的TPR测量得到的在从峰顶到主峰的峰顶点的温度范围内的氢消耗用C1表示时,在从峰顶到峰点的温度范围内的氢消耗由TPR测量还原产物产生的主峰的峰的C 2表示为C 2 / C 1为0.01-0.13。
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