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Comparison of ginger oil conversion over MFI, BEA, and FAU

机译:MFI,BEA和FAU上姜油转化率的比较

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摘要

The catalytic cracking of ginger oil in a fixed-bed tubular reactor with a weight hourly space velocity 1.0 h~(-1) at temperatures ranging from 300 °C to 450 °C has been accomplished over zeolites MFI, BEA, and FAU having different SiO_2/Al_2O_3 ratios. Gasoline fraction yields have been observed along with liquid, gas, and coke yields. Trends in the various yields have been correlated to zeolite structure, SiO_2/Al_2O_3 ratio, and reaction conditions where possible.
机译:MFI,BEA和FAU沸石在固定床管式反应器中以300h至450°C的重时空速为1.0 h〜(-1)催化裂化姜油SiO_2 / Al_2O_3比。已观察到汽油馏分的产率以及液体,气体和焦炭的产率。各种产率的趋势已与沸石结构,SiO_2 / Al_2O_3的比例以及可能的反应条件相关。

著录项

  • 来源
    《Fuel》 |2012年第2012期|p.469-475|共7页
  • 作者单位

    Department of Chemical Engineering, University of Tulsa, Tulsa, OK 74114, USA;

    Department of Chemical Engineering, University of Tulsa, Tulsa, OK 74114, USA;

    Department of Chemical Engineering, University of Tulsa, Tulsa, OK 74114, USA;

    Department of Chemical Engineering, University of Tulsa, Tulsa, OK 74114, USA;

  • 收录信息 美国《科学引文索引》(SCI);美国《工程索引》(EI);
  • 原文格式 PDF
  • 正文语种 eng
  • 中图分类
  • 关键词

    ginger oil; catalytic cracking; BEA; FAU; MFI;

    机译:姜油催化裂化;东亚银行FAU;小额信贷机构;

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