期刊文献+

细粒全尾动态压密与静态压密机理 被引量:17

Dynamic compaction and static compaction mechanism of fine unclassified tailings
原文传递
导出
摘要 采用自制深锥模型进行尾矿浓缩实验,研究了全尾在动态与静态条件下的压密效果.当转速为0.05~0.80 r.min^(-1)时尾矿的极限质量分数范围为67.41%~70.73%,而同等条件下静态压密时尾矿的极限质量分数只有55.82%.静态压密主要依靠重力作用;而动态压密时颗粒更加紧密,导水杆形成的通道使多余的水向上移动.理论挤密模型可以反映全尾压密过程,静态压密行为对应于简单立体结构,动态压密行为对应锥体结构.理论计算的两种模型产生的单位高度沉降量为29.32%,实验结果为28.81%,与理论沉降量相差0.51%. Compassion experiments of tailings were carried out with a self-made deep cone model, and the compaction effects were investigated under the conditions of dynamic compaction and static compaction. When the rotational speed is 0.05 to 0.80 r·min-1, the limit mass fraction of tailings is in the range of 67.41% to 70.73%; under the same conditions, it is only 55.82% for static compaction. Dynamic compaction has a higher compaction because excess water can move up through the water-guiding rod, but static compaction mainly relies on the gravity. The extrusion process of tailings can be simulated by theoretical extrusion models: the static compaction behavior corresponds to a simple spatial structure, while a cone structure for the dynamic compaction behavior. The theoretical value of unit sedimentation height calculated by the two kinds of models is 29.32%, and the test result is 28.81%, 0.51% lower than the theoretical value.
出处 《北京科技大学学报》 EI CAS CSCD 北大核心 2013年第5期566-571,共6页 Journal of University of Science and Technology Beijing
基金 "十二五"国家科技支撑计划资助项目(2012BAB08B02) 国家自然科学基金重点资助项目(50934002) 国家自然科学基金资助项目(51074013 51104011) 长江学者和创新团队发展计划资助项目(IRT0950)
关键词 采矿 尾矿 压密 数学模型 浓密机 mining tailings compaction mathematical models thickeners
作者简介 通信作者,E—mail:wuaixiang@126.com
  • 相关文献

参考文献12

二级参考文献45

  • 1季振万,宋悦杰.高效浓密技术的发展及应用[J].铀矿冶,1995,14(2):89-97. 被引量:9
  • 2刘安平,倪文,张祖刚.梅山尾矿絮凝深锥浓缩试验研究[J].金属矿山,2005,34(10):30-32. 被引量:16
  • 3勾金玲,赵福刚.高效深锥浓密机在梅山选厂的应用[J].矿业快报,2007,23(3):70-72. 被引量:15
  • 4缪林昌.非饱和土的本构模型研究[J].岩土力学,2007,28(5):855-860. 被引量:34
  • 5Sivakugan N, Rankine R M, Rankine K J, et al. Geotechnical considerations in mine backfilling in Australia. J Cleaner Prod, 2006, 14(12) :1168.
  • 6Usher S P, Scales Peter J. Steady state thickener modelling from the compressive yield stress and hindered settling function. Chem Eng J, 2005, 15(8) : 253.
  • 7Burger R, Damasceno J J R, Karlsenl K H. A mathematical model for batch and continuous thickening of flocculated suspensions in vessels with varying cross-section, lnt J Miner Process, 2004, 73 (9) : 183.
  • 8Tiller F M, Chen W. Limiting operating conditions for continuous thickeners. Chem Eng Sci, 1988, 43(7) : 1695.
  • 9Besra L, Sengupta D K, Roy S K, et al. Influence of polymer adsorption and conformation on flocculation and dewatering of kaolin suspension. Sep Purif Technol, 2004, 37(3) : 231.
  • 10Yu X, Somasundaran P. Kinetics of polymer conformational changes and its role in flocculation. J Colloid Interface Sci, 1996, 3(2) : 770.

共引文献215

同被引文献122

引证文献17

二级引证文献105

相关作者

内容加载中请稍等...

相关机构

内容加载中请稍等...

相关主题

内容加载中请稍等...

浏览历史

内容加载中请稍等...
;
使用帮助 返回顶部