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胜利渣油族组分热转化动力学 被引量:2

KINETIC INVESTIGATION OF THERMOLYSIS FOR FOUR SUBFRACTIONS FROM SHENGLI VACCUUM RESIDUE
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摘要 采用动态热分析方法在线性升温速率为6.20K/min及惰性报气流率为100 cm^3/min的条件下考察了胜利渣油四个族组分的热转化行为.结果表明,其热转化活性变化顺序为:饱和分>芳香分>胶质>沥青质.四组分中饱和分可生成少量焦炭,芳香分的生焦率高于前者,胶质及沥青质是焦炭的主要来源.在723K时,两者的生焦率分别为29.0%及44.1%.在热转化过程的两个温度区间内,可利用两个独立的一级动力学模型对实验数据进行拟合.借助线性回归分析,确定了四组分在两个温区内的动力学参数. The behaviors of thermolysis of four subfractions (saturate, aromatic, resin and asphaltene) from Shengli vacuum residue were investigated under the conditions of heating rate of 6. 20 K/min and inert gas flow rate of 100 cm3/min in a thermogravimetric analyzer system. The order of change in thermolysis activity from large to small is as follows: saturate, aromatic, resin, asphaltene. The quantity of coke formed from saturate is small and smaller than that from aromatic in thermolysis. Coke formation is mainly from resin and asphaltene. At a temperature of 723 K. the coke formation rate from resin and asphaltene were 29. 0% and 44. 1% respectively. The experimental data were fitted well with two independent first-order kinetic models in two temperature regions during thermolysis. The kinetic parameters of thermolysis for four subfractions in two temperature regions were obtained using the least square regression.
出处 《石油大学学报(自然科学版)》 CSCD 1992年第4期61-65,共5页 Journal of the University of Petroleum,China(Edition of Natural Science)
基金 本课题系中国石化总公司科研基金及山东省自然科学基金.
关键词 渣油 热转化 动力学 焦炭 Residue Subfraction: Thermolysis Kinetics
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  • 1翁惠新,孙绍庄,江洪波.催化重整集总动力学模型(Ⅰ)模型的建立[J].化工学报,1994,45(4):407-412. 被引量:33
  • 2刘晨光,周家顺,阙国和,梁文杰,朱亚杰.孤岛渣油在分散型催化剂存在下加氢裂化反应动力学的研究I.裂化反应的六集总动力学模型[J].燃料化学学报,1994,22(1):28-36. 被引量:8
  • 3周晓龙,陈绍洲,常可怡.残渣油族组分热转化性能的研究[J].华东理工大学学报(自然科学版),1995,21(6):654-658. 被引量:4
  • 4COXSON P G, BISCHOFF K B. Lumping strategy 1 Introductory techniques and applications of cluster analysis[J]. Ind Eng Chem Res, 1987, 26(6): 1239- 1248.
  • 5COXSON P G, BISCHOFF K B. Lumping strategy 2 A system theoretic approach[J]. Ind Eng Chem Res, 1987, 26(10): 2151-2157.
  • 6JAMES W, PRATER C D. Advances in catalysis[C]. V13 New York: Academic Press, 1962: 203-392.
  • 7沙颖逊 邓先梁 凌珑 等.催化裂化集总动力学模型的初步工业验证.石油炼制,1987,(5):42-48.
  • 8YANG J T, CHEN J R. Kinetics behavior for the nonisothermal coking of four chinese vacuum residual [J]. Fuel Science & Technology International, 1993, 11 (7) : 909-921.
  • 9WEEKMAN V M J R, NACE DM. Kinetics of catalytic cracking selectivity in fixed, moving, and fluid bed reactors[J]. AIChEJournal, 1970, 16(3): 397-404.
  • 10LEE L S, CHEN Y W. Four-lump kinetic model for fluid catalytic cracking process [J]. Canada Journal Chemical Engineering, 1989, 67(8): 615-619.

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