石油炼制与化工 ›› 2012, Vol. 43 ›› Issue (2): 46-50.
• 加工工艺 • 上一篇 下一篇
张力,李亚平,徐亚荣,徐新良
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中国石油天然气集团公司合同项目
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摘要: 在催化精馏塔中对FCC汽油催化精馏烷基化硫转移工艺进行考察,采用树脂催化剂,常压、连续操作,适宜的进料方式为下进料方式,回流质量比为2.0。2 016 h连续运行试验表明,催化剂性能稳定,塔顶汽油硫含量在30~40 μg/g之间,硫转移率平均值为91.14%。
关键词: 催化精馏;烷基化 , FCC汽油 , 脱硫
Abstract: Sulfur containing compounds in FCC gasoline could be removed by alkylation with olefins and then enriched in the heavy fraction by distillation. Based on the reaction conditions obtained in laboratory research, catalytic distillation process for alkylation desulfurization of FCC gasoline was investigated by using catalytic distillation tower. Test results showed that with resin catalyst, under atmospheric pressure, bottom feeding mode, reflux mass ratio of 2.0, reaction temperature in the range of 96-117 ℃, test results of 2 016 h continuous operation showed that the sulfur content of gasoline at the top of the tower was in the range of 30-40 μg/g with an average desulfurization rate of 91.14%, the performance of the catalyst was stable.
Key words: catalytic distillation, alktylation, FCC gasoline, desulfurization
张力 李亚平 徐亚荣 徐新良. FCC汽油催化精馏烷基化硫转移工艺研究[J]. 石油炼制与化工, 2012, 43(2): 46-50.
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