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Study on preparation of fuel oil from waste cooking oil and process of catalytic reforming

机译:废食用油制取燃料油及催化重整工艺研究

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Fuel oil was prepared from waste cooking oil by catalytic cracking and catalytic reforming processes. The preparation of reforming catalyst and the process of catalytic reforming have been investigated. The conditions of the preparation of reforming catalyst were as follow: ZSM-5/H38 zeolite was using as the catalytic carrier, calcination temperature was 550°C and lanthanum oxide content was 6%. Reforming catalyst was used to catalyze the catalytic reforming reaction at 360°C. The results showed that the alkene in fuel oil decreased with the light components increased, the total yield of fuel oil was 84.41%. The proportion of gasoline, diesel oil, heavy oil, non-condensable gas and residue in the product were 9.76%, 69.84%, 4.81%, 11.74% and 3.85%, respectively.
机译:由废食用油通过催化裂化和催化重整工艺制备燃料油。研究了重整催化剂的制备和催化重整的过程。重整催化剂的制备条件如下:以ZSM-5 / H38沸石为催化剂载体,煅烧温度为550℃,氧化镧含量为6%。重整催化剂用于在360℃下催化重整反应。结果表明,随着轻组分的增加,燃料油中的烯烃含量降低,燃料油的总收率为84.41%。产品中汽油,柴油,重油,不凝性气体和残渣的比例分别为9.76%,69.84%,4.81%,11.74%和3.85%。

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