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Process for conversion of paraffinic feedstocks obtained from the biomass of middle distillate bases employing at least one IZM-2 zeolite-based catalyst
Process for conversion of paraffinic feedstocks obtained from the biomass of middle distillate bases employing at least one IZM-2 zeolite-based catalyst
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机译:使用至少一种IZM-2沸石基催化剂转化由中间馏分油基质的生物质获得的链烷烃原料的方法
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摘要
The invention relates to a process for conversion of a paraffinic feedstock that has a number of carbon atoms of between 9 and 25, whereby said paraffinic feedstock is produced starting from renewable resources, employing a catalyst that comprises at least one hydrogenating-dehydrogenating metal that is selected from the group that is formed by the metals of group VIB and group VIII of the periodic table, taken by themselves or in a mixture, and a substrate that comprises at least one IZM-2 zeolite and at least one binder, with said process being carried out at a temperature of between 150 and 500° C., at a pressure of between 0.1 MPa and 15 MPa, at an hourly volumetric flow rate of between 0.1 and 10 h−1, and in the presence of a total quantity of hydrogen mixed with the feedstock such that the hydrogen/feedstock ratio is between 70 and 2,000 Nm3/m3 of feedstock.
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机译:本发明涉及具有9至25个碳原子数的链烷烃原料的转化方法,其中所述链烷烃原料由可再生资源开始使用,该催化剂使用包含至少一种加氢-脱氢金属的催化剂。选自由周期表中第VIB族和第VIII族金属本身或以混合物形式形成的组,以及包含至少一种IZM-2沸石和至少一种粘结剂的基质,所述方法在150至500°C的温度,0.1 MPa至15 MPa的压力,每小时0.1至10 h -1 Sup>的体积流量下进行氢气与原料混合的总量,使得氢气/原料比介于70和2,000 Nm 3 Sup> / m 3 Sup>之间。
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