减压蒸馏
煤焦油
分馏
分数(化学)
煤
tar(计算)
柴油
废物管理
燃料油
蒸馏
破坏性蒸馏
炼油厂
化学
干法蒸馏
催化裂化
材料科学
开裂
碳化
有机化学
工程类
吸附
程序设计语言
计算机科学
作者
Wahyu Ratnaningsih,SUKANDAR SUKANDAR,Deana Wahyuningrum
出处
期刊:IOP conference series
[IOP Publishing]
日期:2021-06-01
卷期号:802 (1): 012039-012039
被引量:6
标识
DOI:10.1088/1755-1315/802/1/012039
摘要
Abstract Coal tar is a hazardous and toxic waste, a by-product of coal gasification processes. Coal tar is a waste produced in industrial fields such as steel, power plant, and the cement industry. As a potential fuel source for its component, utilization of coal tar by catalytic cracking into fuel source and its separation using fractional vacuum distillation is conducted. Pyrolysis of low-temperature coal tar (LTCT) was carried out using catalyst activated natural zeolite by 2:10 ratio at various temperature. The middle oil (180-260°C) fraction was distilled through fractional vacuum distillation using Vigroux column fraction and analyzed using gas chromatography-mass spectroscopy (GC-MS). In this study, the rate constant (k) of middle oil recovery was increased with the increase of temperature and reduced pressure. The calorific value, the density, the kinematic viscosity, the flashpoint, the pour point, and the sulfur content of the middle oil complied with diesel oil type 2 specifications. Still, it did not meet the specification for density specifications. The main components of the middle oil fraction were naphthalenes and their derivatives. The results indicated that the raw LTCT could be considerably upgraded through catalytic cracking, obtaining fuel oil fraction.
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