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气固磁场流态化分选细粒煤 被引量:6

Fine coal particles separation by air-solid magnetic fluidization
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摘要 利用研制的横流式气固磁稳定流化床,以0.074~0.045 mm粒级磁铁矿粉和磁珠作为高密度和低密度分选介质,对6.0~0.5 mm细粒煤进行连续分选试验。结果表明:当处于稳定流化时,磁场气固流化床比普通气固流化床具有更宽的稳定操作气速范围;外加磁场使磁性颗粒沿磁力线形成平行磁链,增大了床层空隙率,形成了分布均匀的通道,气体通过时不会产生气泡,由此形成了稳定的散式气固磁场流化床;高密度分选和低密度分选的可能偏差分别为0.085,0.075 g/cm3。 Continuous separation tests of fine coal particles of 6. 0-0. 5 mm were done by a crossflow air-solid magneti- cally stabilized fluidized bed ( MSFB ), which used 0. 074-0. 045 mm magnetite powder and magnetite beads as medi- um of high and low density separation respectively. The results show that the range of steadily operational air velocity in air-solid magnetically fluidized beds is broader than that in standard air-solid fluidized beds when they are at stable fluidization. External magnetic field compels the magnetic grains to form parallel magnetic chains following the magnet- ic induction lines, which enlarge the bed voidage and form the uniform air channels. Air bubbles cannot be produced when the air flows through the channels, thus stable and particulate air-solid magnetically fluidized beds coming into being. The possible deviation of high and low density separation are 0. 085 and 0. 075 g/cm3 respectively.
出处 《煤炭学报》 EI CAS CSCD 北大核心 2012年第9期1586-1590,共5页 Journal of China Coal Society
基金 国家自然科学基金资助项目(51134022) 国家重点基础研究发展计划(973)资助项目(2012CB214904) 中央高校基本科研业务费专项资金资助项目(2010QNB11)
关键词 磁场流化床 细粒煤分选 流化特性 磁链 magnetically fluidized beds fine coal separation fluidization characteristics magnetic chains
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  • 1Oshitani J, Tani K, Takase K, et al. Dry coal cleaning by utilizing fluidized bed medium separation (FBMS) [ A 1. Proceedings of the SCEJ Symposium on Fluidization C ]. Japan ,2003:425-430.
  • 2Van Houwelingen J A, De Jong T P R. Dry cleaning of coal : review, fundamentals and opportunities [ J ]. Geologica Belgica, 2004,7 ( 3/ 4) :335-343.
  • 3Choung J, Mak C, Xu Z. Fine coal beneficiation using an air dense medium fluidized bed [ J]. International Journal of Coal Preparation and Utilization, 2006,26 ( 1 ) : 1 - 15.
  • 4Sahu A K, Biswal S K, Parida A. Development of air dense medium fluidized bed technology for dry benefieiation of coal : a review E J I- International Journal of Coal Preparation and Utilization, 2009,29 (4) :216-241.
  • 5Zhao Y M, Tang L G, Luo Z F, et al. Experimental and numerical simulation studies of the fluidization characteristics of a separa- ting gas-solid fluidized bed[ J]. Fuel Processing Technology,2010, 91 (12) :1819-1825.
  • 6Luo Z F, Zhu J F, Tang L G, et al. Fluidization characteristics of magnetite powder after hydrophobic surface modification [ J ].International Journal of Mineral Processing,2010,94 ( 3/4 ) : 166 - 171.
  • 7骆振福,陈尚龙,赵跃民,陈增强,唐利刚.基于马尔可夫理论的气固分选流化床密度的预测[J].煤炭学报,2011,36(1):105-109. 被引量:10
  • 8Yang Xuliang Zhao Yuemin Luo Zhenfu Chen Zengqiang Song Shulei.Effects of sintered metal distributor on fluidization quality of the air dense medium fluidized bed[J].Mining Science and Technology,2011,21(5):681-685. 被引量:4
  • 9骆振福,Maoming FAN,陈清如,赵跃民,梁春成,陶秀祥,陈增强.振动参数对流化床分选性能的影响[J].中国矿业大学学报,2006,35(2):209-213. 被引量:20
  • 10骆振福,Maoming FAN,赵跃民,陶秀祥,陈增强.物料在振动力场流化床中的分离[J].中国矿业大学学报,2007,36(1):27-32. 被引量:15

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