Optimal reaction conditions were: temperature 490530 ℃,WHSV 0.250.5 h-1 and system pressure 0.1 MPa. Under such conditions,45%49% light aromatics,25%28% LPG and 2.0%2.5% hydrogen could be obtained.
中试结果表明:液化石油气中烯烃含量越高,芳烃收率就越高,反应的放热效应就越大;在反应温度490~530℃、进料重时空速0.25~0.5 h-1和系统压力0.1 MPa等工艺条件下,能得到45%~49%的轻质芳烃、25%~28%的液化石油气和2.0%~2.5%的氢气。
参考来源 - 液化石油气制芳烃工艺技术的研究开发·2,447,543篇论文数据，部分数据来源于NoteExpress
The impact of process parameters on aromatics saturation reaction of FCC light cycle oil over RN-10 hydrotreating catalyst was studied.
用催化剂RN-10研究了催化裂化柴油加氢深度脱芳烃工艺参数对芳烃加氢饱和反应的影响。
Feedstock demands meeting hydrocarbon steam reforming process including impurity contents of olefins, aromatics, sulfur, arsenic and chloride, as well as dry point of light fraction were introduced.
介绍烃类水蒸气转化制氢工艺对原料的要求，加烯烃、 芳烃、硫、砷和氯等杂质的含量，以及轻油的干点等。
In this paper, a study of light alkane of oil field as raw materials, production process of light alkane aromatization catalysis BTX aromatics was discussed.
本文主要研究了以油田低碳烷烃为原料，通过低碳烷烃芳构化催化反应生产芳烃btx的工艺过程。
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