加氢脱硫
煤焦油
开裂
汽油
柴油
化学
过程(计算)
煤
催化作用
tar(计算)
化学工程
分数(化学)
废物管理
制浆造纸工业
有机化学
工程类
计算机科学
程序设计语言
操作系统
作者
Menglong Niu,Zhaoyang Song,Liuyi Pan,Yongli Yan,Ning Liu,Dong Li,Wenhong Li
出处
期刊:Energy & Fuels
[American Chemical Society]
日期:2020-11-10
卷期号:34 (11): 13614-13624
被引量:17
标识
DOI:10.1021/acs.energyfuels.0c02096
摘要
For coal tar hydrotreating technology, the combination of hydrofining and hydrocracking is a valuable research topic. Therefore, this paper will discuss this topic by comparing three different hydrogenation processes, which include hydrofining (process A); catalyst gradation of hydrofining and hydrocracking (process B); and hydrocracking of diesel fraction produced by hydrofining (process C). The research methods are mainly divided into three parts: product composition analysis, product properties analysis, and reaction kinetics analysis. The study reached the following conclusions: First, the combination of hydrofining and hydrocracking can get better quality gasoline and diesel oil. Second, process C has many advantages over process B and process A. The carbon number and hydrogen number of process C products are more concentrated. In process C, alkaline nitrogen is separated from coal tar in the form of ammonia with water or gas, so process C can effectively improve the service life of hydrocracking catalyst. Third, compared with the two catalysts graded and packed in the reactor, the two-stage hydrogenation method is more convenient in adjusting the ratio of gasoline to diesel oil. Finally, process C is recommended to complete the hydrogenation of coal tar through the analysis of the product composition, reaction path, and reaction kinetics.
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