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PROSES UNTUK HIDROCRACKING MINYAK DISTILAT BERAT DENGAN TAKANAN MENENGAH

机译:中压重质分散油的加氢裂化过程

摘要

The present invention relates to a process for producing middle distillates by hydrocracking a heavy distillate oil under middle pressure in which a hydrofining catalyst and a hydrocracking catalyst are used in series and once-through operation. The once-through volume conversion to 350 °C products is up to 80 vol.%. The yield and selectivity of middle distillates are greater than 40 wt.% and less than 50 wt.%, respectively. The process is particularly suited to treat heavy distillate oil having the nitrogen content of up to 1500 ppmw, the sulfur content of up to 3.5 wt.% and dry point of the boiling range of higher than 500 °C to produce the feed for reforming process jet fuel, the low sulfur content diesel, the feed for catalytic cracker and the feed for producing ethylene.
机译:本发明涉及通过在中压下将重馏分油加氢裂化来生产中间馏分的方法,其中将加氢精制催化剂和加氢裂化催化剂串联和一次通过使用。一次性将体积转换为350°C的产品的体积百分比最高为80%。中间馏分的产率和选择性分别大于40重量%和小于50重量%。该方法特别适合处理氮含量最高为1500 ppmw,硫含量最高为3.5 wt。%,沸点干燥点高于500°C的重质馏分油,以生产用于重整过程的原料喷气燃料,低硫柴油,催化裂化装置的进料和乙烯的进料。

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