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作 者:鞠雪艳[1] 张锐[1] 习远兵[1] 任亮[1] 赵杰[1] Ju Xueyan;Zhang Rui;Xi Yuanbing;Ren Liang;Zhao Jie(SINOPEC Research Institute of Petroleum Processing,Beijing 100083)
机构地区:[1]中国石化石油化工科学研究院,北京100083
出 处:《石油炼制与化工》2022年第6期6-11,共6页Petroleum Processing and Petrochemicals
基 金:中国石油化工股份有限公司合同项目(120051-1)。
摘 要:利用催化裂化柴油(LCO)密度较高且富含芳烃的性质特点,开展了以LCO为原料生产高密度喷气燃料的工艺研究。结果表明,以LCO为原料,采用高芳烃饱和活性的NiMoW/Al_(2)O_(3)加氢精制催化剂,在适当的工艺条件下进行超深度加氢饱和,可使LCO中芳烃质量分数降低至5%以下。进一步通过气相色谱-质谱(GC-MS)方法进行详细的烃类分析,可明确各烃类的分布规律并考察富集单环、二环及三环环烷烃的馏分,确定全馏分LCO加氢生产高密度喷气燃料时理想的终馏点为270~280℃,在此分馏温度下可得到冰点低于-47℃、密度(20℃)大于0.835 g cm^(3)的高密度喷气燃料组分。Based on the characteristics of high density and rich aromatics of FCC light cycle oil(LCO),the process technology of producing high-density jet fuel from the whole fraction of LCO was studied.The results show that the mass fraction of aromatics can be reduced to less than 5%by using NiMoW/Al_(2)O_(3) hydrofining catalyst with high aromatics saturation activity through ultra-deep hydrogenation saturation under proper process conditions.Further detailed hydrocarbon analysis by gas chromatography-mass spectrometry(GC-MS)can clarify the distribution of hydrocarbons and investigate the fractions enriched with monocyclic,bicyclic and tricyclic cycloalkanes.The final boiling point of ideal fraction was 270-280℃when the full fraction LCO was hydrogenated to produce high density jet fuel.Freezing point of high-density jet fuel component is lower than-47℃and density(20℃)is greater than 0.835 g cm^(3).
分 类 号:TE626.23[石油与天然气工程—油气加工工程]
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