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Simultaneous desulfurization and isomerization of sulfur containing n-pentane fractions over Pt/H-mordenite catalyst

机译:Pt / H-丝光沸石催化剂同时进行含硫正戊烷馏分的同时脱硫和异构化

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A new field of the catalytic application of Pt/H-mordenite catalysts is presented for production of gasoline blending components having high octane number and reduced sulfur content (<10-50 ppm) required for satisfying environmental and human health regulations. Experiments were carried out over catalysts containing 0.3-1.0% platinum on H-mordenite of various acidity and on Pt, Pd/H-Y zeolite. The n-pentane fractions containing 61-184 ppm sulfur in the form of COS, CS_2, beside Me-, Et-, i-Pr-thiol were converted at 200-280°C, 30-40 bar, 0.8-2.0 h~(-1) liquid hourly space velocity and hydrogen to hydrocarbon mole ratios of 1:1-2:1. Under optimum process parameters the concentration of all sulfur compounds in the product was less than 1-2 ppm using the catalyst containing 0.6% platinum, preserving its strong metal function. During hydrodesulfurization the isomerization of n-pentane took place simultaneously with high conversion and selectivity approaching the thermodynamic equilibrium to 85-98%.
机译:提出了Pt / H-丝光沸石催化剂的催化应用的新领域,用于生产具有高辛烷值和降低的硫含量(<10-50 ppm)的汽油共混组分,以满足环境和人类健康法规的要求。在各种酸度的H-丝光沸石和Pt,Pd / H-Y沸石上对含0.3-1.0%铂的催化剂进行了实验。在200-280°C,30-40 bar,0.8-2.0 h〜的温度下,将含有61-184 ppm硫的COS,CS_2形式的正戊烷馏分转化为Me-,Et-,i-Pr-硫醇。 (-1)液体时空速度和氢与烃的摩尔比为1:1-2:1。在最佳工艺参数下,使用含0.6%铂的催化剂,产品中所有硫化合物的浓度均小于1-2 ppm,从而保留了其强大的金属功能。在加氢脱硫过程中,正戊烷的异构化同时发生,同时高转化率和选择性接近热力学平衡,达到85-98%。

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