Performance of a solid particle distribution device used in a multi-bed reactor for calcium carbide production

ZHAO XinLei;QI Juan;MA YiYa;LIU Hui;WEI Wei

Journal of Beijing University of Chemical Technology ›› 2015, Vol. 42 ›› Issue (3) : 28-32.

PDF(769 KB)
Welcome to Journal of Beijing University of Chemical Technology, Today is July 17, 2025
Email Alert  RSS
PDF(769 KB)
Journal of Beijing University of Chemical Technology ›› 2015, Vol. 42 ›› Issue (3) : 28-32.
化学与化学工程

Performance of a solid particle distribution device used in a multi-bed reactor for calcium carbide production

  • ZHAO XinLei;QI Juan;MA YiYa;LIU Hui;WEI Wei
Author information +
History +

Abstract

To meet the needs of reactor design for calcium carbide production by the oxygen fuel method, a solid particle distribution device involving a stirred tank with two different kinds of blades and distribution plates has been designed. A coldmodel experimental system was set up to investigate the influence of different bed heights, rotation speeds of blades, distances from the blade to the distribution plate, and different kinds of particles (glass beads and catalyst particles) on the average mass flux through plate. The results show that the mass flux increases with increasing bed height and rotation speed of the blade, whereas with an increase in distance between the blade and the distribution plates, the mass flux decreases sharply. The glass beads exhibit a larger mass flux than the catalyst particles. Using a flat blade rather than an oblique one or a distribution plate with more holes, leads to far greater mass fluxes.

Cite this article

Download Citations
ZHAO XinLei;QI Juan;MA YiYa;LIU Hui;WEI Wei. Performance of a solid particle distribution device used in a multi-bed reactor for calcium carbide production[J]. Journal of Beijing University of Chemical Technology, 2015, 42(3): 28-32

References

[1]刘振宇, 刘清雅, 李国栋. 一种电石生产方法: 中国, 101327928A [P]. 2008-12-24. 
Liu Z Y, Liu Q Y, Li G D. A method of making calcium carbide: CN, 101327928A [P]. 2008-12-24. (in Chinese)
[2] Shen Y S, Guo B Y, Yu A B, et al. Three dimensional modelling of in furnace coal/coke combustion in a blast furnace [J]. Fuel, 2011, 90(2): 728-738. 
[3]汪家铭. BGL碎煤熔渣气化技术及其工业应用[J]. 化学工业, 2011, 29(7): 34-39. 
Wang J M. BGL pulverized coal slag gasification technology and its industrial applicationJ. Chemical Industry, 2011, 29(7): 34-39. (in Chinese)
[4]刘振宇, 刘清雅, 李国栋. 一种电石生产系统: 中国, 101428799A [P]. 2009-05-13. 
Liu Z Y, Liu Q Y, Li G D. A system of making calcium carbide: CN, 101428799A [P]. 2009-05-13. (in Chinese)
[5]曾剑桥, 黄迪, 刘辉. 复合床电石反应器布料器性能实验[J]. 北京化工大学学报: 自然科学版, 2014, 41(5): 25-30. 
Zeng J Q, Huang D, Liu H. Particle distributing performance of rotational plates in a combinedmoving bed reactor for carbide production[J]. Journal of Beijing University of Chemical Technology: Natural Science, 2014, 41(5): 25-30. (in Chinese)
[6] Llamasa J D, Lesagea F, Wildb G. Radial dispersion in trickle bed reactors: Comparison between sock and dense loadings[J]. Chemical Engineering Science, 2010, 65(1): 538-541. 
[7]张振芳, 王彦灵, 姬天德, 等. 一种鲁奇气化炉布煤搅拌装置: 中国, 201020598213.6[P]. 2010-11-10. 
Zhang Z F, Wang Y L, Ji T D, et al. A churn dasher used in Rutsch gasifier: CN, 201020598213.6[P]. 2010-11-10. (in Chinese)
[8]熊玮, 毕学工, 周勇. 高炉布料过程中焦炭坍塌现象的模型研究[J]. 武汉科技大学学报: 自然科学版, 2007, 30(4): 342-345. 
Xiong W, Bi X G, Zhou Y. A model study of coke layer collapse in charging process in blast furnace[J]. Journal of Wuhan University of Sci & Tech: Natural Science, 2007, 30(4): 342-345. (in Chinese)
PDF(769 KB)

793

Accesses

0

Citation

Detail

Sections
Recommended

/