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C207铜基催化剂常压甲醇分解反应动力学(Ⅱ)催化剂效率因子正交配置解 被引量:2

Reaction Kinetics of Methanol Decomposition over C207 Cu-Based Catalyst (Ⅱ) Orthogonal Collocation Solution for Effectiveness Factor
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摘要 在内循环无梯度反应器中常压下测定了工业颗粒C207催化剂甲醇分解反应宏观速率,测定了催化剂孔径分布和曲节因子,获得了催化剂效率因子的实测值。探讨了计算催化剂效率因子的甲醇单组分模型和多组分模型的正交配置解,颗粒催化剂存在中心平衡死区。在相同反应条件下,催化剂效率因子模型计算值与实测值的相对误差的绝对值的平均值在11%以内,结果表明计算模型是可行的。 The global reaction rates of methanol decomposition over ψ5×5mm cylindrical pellets of C207 Cu-based catalyst under atmospheric pressure in an internal recycle gradientless reactor, the pore size distribution and the tortuosity factor of catalyst were measured. The effectiveness factors obtained experimentally are between 0.1938 and 0.5226. The single component model and multicomponent model for catalyst effectiveness factor are presented and solved by the orthogonal collocation method. The dead zone of center equilibrium exists in pellets. The average of absolute value of relative deviations between experimental values and model calculated values of effectiveness factor is less than 11 per cent. The models are feasible for the calculation of catalyst effectiveness factor.
出处 《高校化学工程学报》 EI CAS CSCD 1991年第4期327-333,共7页 Journal of Chemical Engineering of Chinese Universities
基金 高等学校博士学科点专项科研基金
关键词 铜基催化剂 甲醇分解 正交配置法 Methanol decomposition Effectiveness factor Orthogonal collocation method
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  • 1Jeannette A,Johan W, Tapio S, et al. Interaction of kinetics and internal diffusion in complex catalytic three-phase reactions: Activity and selectivity in citral hydrogenation [J]. Chem Eng Sci,2006,61(2):814-822.
  • 2Zhan X D, Burtron H D. Assessment of internal diffusion limitation on Fischer-Tropsch product distribution [J]. Applied Catalysis, 2002,234 : 149-161.
  • 3Wakao N,Smith J M. Diffusion in catalyst pellets [J]. Chem Eng Sci, 1962,27(2) : 825-831.
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  • 5Cheng Chengyuan, Chen Dasheng, Ying Weiyong. Kinetics study of one-step synthesis of DME from syngas[C]//The 8th Word Congress of Chemical Engineering. Montreal,Cana da:MeGill-Queen's University Press,2009.
  • 6Brown C E,Bennett C O. Methanol synthesis catalysis in an internally recycled reactor [J]. AIChE Journal, 1970,16 (6) : 817-823.
  • 7Cheng Chengyuan, Chen Dasheng, Ying Weiyong. Kinetics study of one-step synthesis of DME from syngas[C]//The 8th Word Congress of Chemical Engineering. Montreal,Cana da:MeGill-Queen's University Press,2009.
  • 8房鼎业,姚佩芳,朱炳辰.甲醇生产技术进展[M].上海:华东化工学院出版社,1990:129—144.
  • 9Jeannette A,Johan W, Tapio S, et al. Interaction of kinetics and internal diffusion in complex catalytic three-phase reactions: Activity and selectivity in citral hydrogenation [J]. Chem Eng Sci,2006,61(2):814-822.
  • 10Zhan X D, Burtron H D. Assessment of internal diffusion limitation on Fischer-Tropsch product distribution [J]. Applied Catalysis, 2002,234 : 149-161.

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