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Preparation of Light Fuel Fractions from Heavy Vacuum Gas Oil by Thermal Cracking Reaction

机译:通过热裂化反应制备来自重质真空瓦斯油的轻燃料级分

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摘要

This work deals with thermal cracking of heavy vacuum gas oil which produced from the top of vacuum distillation unit at Al- DURA refinery, by continuous process. An experimental laboratory plant scale was constructed in laboratories of chemical engineering department, Al-Nahrain University and Baghdad University. The thermal cracking process was carried out at temperature ranges between 460-560oC and atmospheric pressure with liquid hourly space velocity (LHSV) equal to 15hr-1.The liquid product from thermal cracking unit was distilled by atmospheric distillation device according to ASTM D-86 in order to achieve two fractions, below 220oC as a gasoline fraction and above 220oC as light cycle oil (LCO).The first fraction which was below 220oC was fractionated to light fractions (gasoline, kerosene and gas oil) by atmospheric distillation device. The fractions (gasoline, kerosene and gas oil) were distilled by atmospheric distillation device in order to obtained distillation curve for these fractions. Physical properties were recorded for these cuts to compare it with standard property test, in order to studying the possibilities of industrial uses. The maximum conversion of heavy vacuum gas oil was obtained by this process equal to 82 wt. % of feed at 540oC.
机译:这项工作涉及重质真空燃气油的热裂纹,通过连续工艺,从Al-Dura炼油厂的真空蒸馏装置顶部产生。实验实验室植物规模是在化学工程系,al-nahrain大学和巴格达大学的实验室中构建的。在460-560oC和大气压的温度范围内进行热裂化过程,液小时空间速度(LHSV)等于15HR-1。根据ASTM D-86,通过大气蒸馏装置蒸馏来自热裂化单元的液体产物为了实现两个级分,低于220℃,作为汽油馏分,高于220℃作为光循环油(LCO)。通过大气蒸馏装置将低于220℃的第一部分低于220℃(汽油,煤油和瓦斯油)。通过大气蒸馏装置蒸馏馏分(汽油,煤油和瓦斯油),以获得这些级分的蒸馏曲线。为这些切割记录了物理性质,以将其与标准性能测试进行比较,以研究工业用途的可能性。通过该方法获得重质真空瓦斯油的最大转化等于82重量%。 540℃的饲料%。

著录项

  • 作者

    Saleem Mohammed Obyed;

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  • 年度 2017
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  • 原文格式 PDF
  • 正文语种 eng
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