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Catalytic cracking process for production of diesel from vegetable oils

机译:由植物油生产柴油的催化裂化工艺

摘要

"The process of catalytic cracking for the production of diesel from vegetable oils. The present invention includes a process for cracking termocatalu00edtico, for the production of diesel fuel from vegetable oils, in refineries which have a minimum of two reactors of FCC.At least one of the reactors processes heavy gas oil or residue in conventional conditions while at least one of the reactors processing vegetable oils under conditions suitable for the production of diesel oil. The process uses the same catalyst used in the process of fluid catalytic cracking, which, at the same time, processes the conventional load.The process transforms raw materials with a high calorific value of fuel hydrocarbons and exhibits excellent efficiency for obtaining products with high purity and does not present the formation of glycerol, a by-product of the process of transesterificau00e7u00e2o.The diesel oil produced through the said process has superior quality, presents a cetane number higher than 40, because the cracking reactions occur at low temperatures and the products obtained are less oxidised, and hence more pure than the products obtained through the technology. Existing.
机译:由植物油生产柴油的催化裂化方法。本发明包括在至少具有两个FCC反应器的炼油厂中裂化白果酚的方法,以由植物油生产柴油。至少有一个反应器在常规条件下处理重质瓦斯油或渣油,而至少一个反应器在适合于生产柴油的条件下处理植物油。该方法可转换具有高热值的燃料碳氢化合物的原料,并且在获得高纯度产品方面显示出优异的效率,并且不会形成甘油的副产物。通过上述方法生产的柴油具有优良的品质,十六烷值更高, 40年代,因为裂化反应在低温下发生,并且获得的产物氧化程度较低,因此比通过该技术获得的产物纯度更高。现有。

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