煤油共炼残渣中多环芳烃的脱除特性研究OA
Research on removal characteristics of PAHs in residue of coal-oil co-processing
为考察45万t/a煤油共炼工业示范装置副产残渣的绿色化应用效果,通过气相色谱法建立多环芳烃(PAHs)的分析检测方法,确定煤油共炼反应体系下残渣中PAHs分布规律,采用聚合改性法进行脱除.考察改性剂、催化剂、体系溶剂、反应温度、反应时间等条件对残渣中PAHs脱除率与苯并[a]芘(BaP)当量脱除率的影响,对比残渣改性前后的关键指标.结果表明:煤油共炼残渣中PAHs含量为18.15 mg/g,包括菲、蒽、荧蒽、芘、苯并[a]蒽、䓛、苯并[b]荧蒽、茚并[1,2,3-cd]芘等16种组分;在30%(试剂与残渣质量比)对苯二甲醛、40%(试剂与残渣质量比)硫酸、甲苯 50 mL、反应温度 80℃、反应时间 4 h条件下,受改性亲电取代、酸性催化、溶剂物理稀释的协同作用,改性后残渣中PAHs不同组分的脱除率最大达到 98.46%,BaP当量脱除率为95.34%;改性后残渣中芳香烃质量分数由 57.50%降低至 33.46%,脂肪烃化合物质量分数由25.24%增加至 37.43%,含氧化合物质量分数增加 9.56%.软化点由 105℃提高至 118℃,针入度减小2.2(50℃,0.1 mm),一定程度提高了残渣的热稳定性与流变性.
To verify the green application effectiveness of by-product residue from a 45×104 t/a coal-oil co-processing industrial demonstration plant,an analysis and detection method for polycyclic aromatic hydrocarbons(PAHs)was established by gas chromatography,and the distribu-tion of PAHs in the residue of the coal-oil co-processing reaction system was determined,and a polymerization modification method was applied to remove PAHs.The influence of the modifier,catalyst,solvent,reaction temperature and time on the removal rate of PAHs and the total equivalent content of BaP in the residue was researched,and key indicators were also compared before and after residue modification.The results show that the content of PAHs in the residue is 18.15 mg/g,includ-ing phenanthrene,anthracene,fluoranthene,pyrene,benzo[a]anthracene,chrysene,benzo[b]fluor-anthene,indeno[1,2,3-cd]pyrene and other 16 components.In the conditions of 30%(mreagent:mresidue)terephthaldehyde,40%(mreagent:mresidue)sulfuric acid,50 mL toluene,a reaction temperature of 80℃and reaction time 4h,the maximum removal rate of PAHs and the total equivalent removal rate of BaP in the modified residue reach 98.46%and 95.34%respectively,due to the synergistic effect of electrophilic substitution of modifier,acidic catalysis of catalyst and physical dilution of solvent.After modification,the content of aromatic hydrocarbon decreases from 57.50%to 33.46%,the content of aliphatic compound and oxygen compounds increases from 25.24%to 37.43%,and oxygen-containing compounds increases by 9.56%.The softening point increases from 105 ℃ to 118 ℃,the penetration degree decreased by 2.2(50℃,0.1 mm),and the thermal stability and rheological prop-erties of the residue are improved to some extent.
黄勇;张晓欠;兰伟伟;康徐伟;刘丹;杜若宇
西北化工研究院有限公司,710000 西安西北化工研究院有限公司,710000 西安西北化工研究院有限公司,710000 西安西北化工研究院有限公司,710000 西安西北化工研究院有限公司,710000 西安西北化工研究院有限公司,710000 西安
化学化工
煤油共炼残渣改性多环芳烃脱除
coal-oil co-processingresiduemodifypolycyclic aromatic hydrocarbonsremoval
《煤炭转化》 2026 (2)
11-20,10
陕西省重点研发计划项目(2025CY-YBXM-490)和陕西延长石油(集团)有限责任公司科技项目(YCSY2025ZS-B-02)
评论