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Epoxidation of propylene using supported titanium silicalite catalysts

机译:负载型钛硅沸石催化剂对丙烯的环氧化

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摘要

The propylene epoxidation using supported titanium silicalite TS-1 catalyst was systematically investigated in a fixed bed reactor. Different supports such as SiO_2 and Al_2O_3 were used and two molding methods were adopted to prepare the catalyst. Strip TS-1 catalyst of 1 mm X 2 mm dimensions is obtained by the extruding method. Use of SiO_2 as the support rather than Al_2O_3 is better becau7se the latter has strong acidity that promotes the side reaction of propylene oxide (PO) with the solvent. With the decrease of the amount of TS-1 in TS-1/SiO_2, the PO selectivity increases. The lamina TS-1 catalyst, the core of which is an inert ball used as the support and the shell of which is a TS-1 lamina of 0.1-0.2 mm, exhibits better performance than the strip TS-1 catalyst owing to its shorter diffusion path for reaction heat, raw material and product. The lamina TS-1 catalyst was used in the fioxed bed reactor for about 200 h. The results indicate that it is a promising catalyst in propylene epoxidation. The effect of aluminum impurity was also investigated. It has been shown adcid sites originating from framework aluinum can catalyze the side reaction and a small amount of base can inhibit it. In conclusion, diffusion and theconcentration of acid sites are the two main factors influencing the performance of titanium silicalite catalyst in propylene epoxidation.
机译:在固定床反应器中系统地研究了使用负载型钛硅沸石TS-1催化剂进行的丙烯环氧化。使用了不同的载体如SiO_2和Al_2O_3,并采用两种成型方法制备了催化剂。通过挤出方法获得1mm×2mm尺寸的条状TS-1催化剂。使用SiO_2作为载体而不是Al_2O_3更好,因为后者具有强酸性,可促进环氧丙烷(PO)与溶剂的副反应。随着TS-1 / SiO_2中TS-1含量的减少,PO选择性增加。 TS-1薄层催化剂的核心是用作支撑体的惰性球,壳是0.1-0.2 mm的TS-1薄层,由于其较短,因此比带状TS-1催化剂具有更好的性能反应热,原料和产品的扩散路径。薄层TS-1催化剂在固定床反应器中使用约200小时。结果表明,它是丙烯环氧化的一种有前途的催化剂。还研究了铝杂质的影响。业已显示,源自骨架铝的腺苷酸位点可以催化副反应,而少量的碱可以抑制副反应。总之,酸位的扩散和浓度是影响钛硅沸石催化剂在丙烯环氧化反应中性能的两个主要因素。

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