摘要
对应用在加氢裂化装置的轻油型改造的标准公司的催化剂进行了对比和总结。结果表明,标准公司的精制催化剂和裂化催化剂的温度匹配好,精制和裂化催化剂的反应温度比较低,标准公司的裂化剂可以至少两个生产周期(6年)不用再生,轻油(重石脑和航煤)收率大幅度上升,轻油收率可以达到52%~60.68%。
The catalysts of Criterion company applied in the light oil type reformation of the hydrocracking unit were compared and summarized. The results showed that the use temperatures of the refining catalyst and the cracking catalyst of Criterion company were well matched, and the reaction temperature of the refining catalyst and cracking catalyst was relatively lower. The cracking catalyst of Criterion company can be used for at least two production cycles(6 years) without regeneration, light oil(heavy naphtha and jet fuel)yield can be increased significantly and reach 52%~60.68%.
引文
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