劣质柴油高效加氢裂化生产重石脑油

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引用格式:,等.劣质柴油高效加氢裂化生产重石脑油[J].当代化工,2026,55(4):1004-1008.

FAN Siqiang, ZHANG Bo, ZHOU Qinzhen, et al. Production of Heavy Naphtha from Inferior Diesel through High-Efficiency Hydrocracking[J]. Contemporary Chemical Industry, 2026, 55(4): 1004-1008.

1 , 2 ,周钦镇 2 ,刘锐 3

(1. , 116405;

2. , 510000;

3. , 710065)

中图分类号:TQ032.4

文献标志码:A

文章编号:1671-0460(2026)04-1004-05

Production of Heavy Naphtha from Inferior Diesel through High-Efficiency Hydrocracking

FAN Siqiang 1, ZHANG Bo 2, ZHOU Qinzhen 2, LIU Rui 3

Sinopec (Dalian) Research Institute of Petroleum and Petrochemicals Co., Ltd., Dalian Liaoning 116405, China;

2. Sinopec Guangzhou Petrochemical Company, Guangzhou Guangdong 510000, China;

3. College of Chemistry and Chemical Engineering, Xi'an Shiyou University, Xi'an Shaanxi 710065, China)

Abstract: To expand the sources of heavy naphtha raw materials and achieve the high-value utilization of low-quality diesel, the process conditions and product distribution patterns for hydrogenation cracking of distillate diesel mixed with fluidized bed diesel to produce heavy naphtha were systematically studied. By comparing the two operation modes of "constant reaction depth" and "constant reaction temperature", the influence of the blending ratio of fluidized bed diesel (10% - 50%) on the properties of raw materials, process conditions, product distribution and product quality was investigated. The results showed that fluidized bed diesel was rich in nitrogen compounds and polycyclic aromatic hydrocarbons. As the blending ratio increased, the density of the mixed raw materials rose, the total nitrogen content significantly increased, and the processing difficulty significantly increased. Under the condition of constant reaction depth, moderately increasing the reaction temperature could effectively maintain the stable yield of heavy naphtha, and the mass fraction of cycloalkanes and aromatics (N + A) increased from 33.30% to 39.50%; while under the condition of constant reaction temperature, high blending ratio led to insufficient denitration, a significant decrease in the yield of light/heavy naphtha, and a sharp increase in the yield of unconverted oil, indicating that the reaction depth was seriously insufficient. Controlling the blending ratio of fluidized bed diesel to be between 30% - 40% and matching it with corresponding strictness, could ensure the conversion efficiency and improve the quality of heavy naphtha.

Keywords: Straight-run diesel; Hydrocracking; Fluidized bed diesel; Blending ratio; Reducing oil production and increasing chemical production; Selectivity; Production

在化工原料需求日益增加与全球能源结构变化愈演愈烈的趋势下,重石脑油作为蒸汽裂解制乙烯、催化重整制芳烃的核心原料,如何实现其低成本高

效生产已成为石化领域的迫切难题[1-2]。(剩余9091字)

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