化工学报 ›› 2012, Vol. 63 ›› Issue (5): 1643-1650.DOI: 10.3969/j.issn.0438-1157.2012.05.045

• 材料化学工程与纳米技术 • 上一篇    下一篇

SiO2/S涂层与硫磷抑制剂对轻石脑油裂解结焦的影响

王志远1,徐宏1,栾小建1,周建新2,颜磊1   

  1. 1化学工程联合国家重点实验室,华东理工大学机械与动力工程学院;2南京工业大学机械与动力工程学院
  • 收稿日期:2011-07-15 修回日期:2012-01-08 出版日期:2012-05-05 发布日期:2012-05-05
  • 通讯作者: 徐宏

Effects of SiO2/S coating and sulfur phosphorous inhibitor on coking in light naphtha cracking

WANG Zhiyuan1,XU Hong1,LUAN Xiaojian1,ZHOU Jianxin2,YAN Lei1   

  1. 1State Key Laboratory of Chemical Engineering,School of Mechanical and Power Engineering,East China University of Science and Technology;2School of Mechanical and Power Engineering,Nanjing University of Technology
  • Received:2011-07-15 Revised:2012-01-08 Online:2012-05-05 Published:2012-05-05

关键词: 退役HP40裂解炉管, 结焦, 硫磷抑焦剂, 抑焦SiO2/S涂层, 焦炭结构

Abstract: Coking tests were carried out on the inner surface of after-service HP40 cracking tube at 850℃ with naphtha as feed,and the anti-coking properties of anti-coking SiO2/S coating and sulfur phosphorous coking inhibitor were investigated.The effect of SiO2/S coating and sulfur phosphorous coking inhibitor on coke formation was studied.Scanning electron microscopy (SEM),X-ray energy dispersion spectrometry (EDS)and X-ray diffraction (XRD)were used to characterize the morphology and structure of the inner surface of after-service HP40 cracking tube and the morphology of coke on the surface.The structure of coke was analyzed by TGA,elemental analysis and Raman spectroscopy.The results showed that the changes of the inner surface conditions of after-service HP40 cracking tube led to accelerated catalytic coking. When the mass fraction of sulfur phosphorous inhibitor was 200 μg·g-1,coke deposition was reduced by 69%.SiO2/S coating could inhibit catalytic coking,and coke was mainly deposited in the spalled SiO2/S coating region.Coke formation was reduced by 65% for SiO2/S coating only.When the combination of sulfur phosphorous coking inhibitor and SiO2/S coating was applied,the interference of HS radicals,originating from sulfur phosphorous inhibitor decomposition,with the heterogeneous noncatalytic mechanism in the cracking via radical termination and hydrogen abstraction reactions resulted in an optimum mass concentration of sulfur phosphorous coking inhibitor.The combination of sulfur phosphorous coking inhibitor at the mass concentration of 50 μg·g-1 plus SiO2/S coating would result in a decrease in coke formation up to 97%.Coke deposited on the inner surface of after-service HP40 cracking tube had a highly condensed structure with a high boiling point and a low graphitization degree.The use of SiO2/S coating and sulfur phosphorous inhibitor led to a decrease in the graphitization degree of the coke to a certain extent.

Key words: after-service HP40 cracking tube;coking, sulfur phosphorous coking inhibitor;anti-coking , SiO2/S coating;structure of cokes

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