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Gas-phase hydrodechlorination of mixtures of chloromethanes with activated carbon-supported platinum catalysts

机译:氯甲烷与活性炭负载铂催化剂混合物的气相加氢脱氯

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摘要

Platinum catalysts supported on activated carbon (Pt/C) at different metal loadings (0.5-2% Pt) have been tested in the gas-phase hydrodechlorination (HDC) of mixtures of dichloromethane (DCM) and chloroform (TCM), with a total feed concentration of 1000ppmv. Almost complete dechlorination was achieved at 250°C, 1kghmol-1 space time and a H2/CM molar ratio of 25 with the 2% Pt catalyst. At a reaction temperature of 250°C, scarce inhibition in the conversion of both compounds was observed compared to the HDC of the individual chloromethanes. The TOF values for DCM increase with the Pt content, which can be attributed to the higher proportion of the zero-valent species. The selectivity to reaction products suggests a parallel reactions scheme. The catalysts showed a high stability, demonstrated by the unchanged conversion of both chloromethanes upon time on stream in long-term experiments carried out at up to 26h.
机译:在二氯甲烷(DCM)和氯仿(TCM)的混合物的气相加氢脱氯(HDC)中已经测试了在不同金属负载量(0.5-2%Pt)上负载在活性炭(Pt / C)上的铂催化剂进料浓度为1000ppmv。用2%Pt催化剂在250°C,1kghmol-1时空和H2 / CM摩尔比为25的条件下几乎可以完成完全脱氯。与单个氯甲烷的HDC相比,在250°C的反应温度下,观察到两种化合物转化的抑制都很少。 DCM的TOF值随Pt含量的增加而增加,这可以归因于零价物质比例更高。对反应产物的选择性暗示了平行反应方案。在长达26小时的长期实验中,两种氯甲烷的转化率随生产时间的变化而保持不变,表明该催化剂具有很高的稳定性。

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