新型两段粗煤泥分选旋流器在曙光选煤厂的应用Application of new two-stage separating cyclone for coarse slime in Shuguang coal preparation plant
王进;
WANG Jin;Shuguang Mining Group Co. ,Ltd.;
摘要(Abstract):
通过筛分试验和浮沉试验分析了曙光选煤厂粗煤泥性质,说明原煤中粗粒级含量较高,+0.250 mm产率达到52.25%,应选择适宜的粗煤泥分选设备对其分选回收;当精煤灰分≤11.0%时,曙光选煤厂粗煤泥属中等可选煤。针对曙光选煤厂重介旋流器分选精度低,介耗偏高等问题,以新型两段粗煤泥分选旋流器为核心设备,构建了粗煤泥分选体系,形成预先脱泥、粗煤泥单独分选与常规重介、浮选相衔接的工艺流程,完善了分选工艺。改造后,选煤厂原煤处理量由235 t/h提至285t/h,年处理原煤能力由120万t提至150万t;介耗由改造前的2.4 kg/t降至2.0 kg/t。每年增加精煤销售额1.14亿元,节省介质费用75万元,节省电费11.25万元。改造后曙光选煤厂工艺流程更加合理,生产调节更具灵活性,产品质量稳步提升,实现了降低介耗,增加原煤处理量的目标。
Analyse the coarse coal slime natures in Shuguang coal preparation plant through screening test and float-and-sink analysis.The results show that coarse grained content in feed coal is high and the yield of + 0. 250 mm size fraction reach up to 52. 25 percent.These coarse slime should be disposed with appropriate separation equipment. Requirement of concentrate ash is below11. 0 percent,coarse coal slime is medium washability. To improve the accuracy of dense medium cyclone and reduce medium consumption,build a system for coarse coal separation alone taking new two-stage separating cyclone with muti-products as core device. Build the formation of coarse coal slime separation system,the preliminary desliming,coarse coal slime separation and conventional medium alone,flotation of corresponding technological process,perfect the sorting process,which perfect the separating technology. After modification,the raw coal treatment capacity increase from 235 t / h to 285 t / h,so the total treatment capacity each year increase from 1. 2 × 106tons to 1. 5 × 106tons.The medium consumption decrease from 2. 4 kg / t to 2. 0 kg / t. The plant saves medium cost 7. 5 × 105yuan,energy cost 11. 25 × 105yuan,increase clean coal sales volume 1. 14 × 108yuan per year. After transformation,the technological process becomes more perfect and flexible,the product quality steadily improve,the medium consumption decrease.
关键词(KeyWords):
分选旋流器;粗煤泥;可选性;介耗;工艺流程
separating cyclone;coarse slime;washability;medium consumption;technological process
基金项目(Foundation):
作者(Authors):
王进;
WANG Jin;Shuguang Mining Group Co. ,Ltd.;
DOI: 10.13226/j.issn.1006-6772.2014.02.003
参考文献(References):
- [1]谢广元.选矿学[M].徐州:中国矿业大学出版社,2001.
- [2]戴少康.选煤工艺设计的思路与方法[M].北京:煤炭工业出版社,2003.
- [3]李志勇,叶鹤,徐胜.预先脱泥无压给料重介质旋流器高效分选新工艺[J].煤炭加工与综合利用,2008(5):1-3.
- [4]高伟,刘磊,乔鹏,等.泉店选煤厂工艺系统的改造[J].洁净煤技术,2013,19(3):34-37,41.
- [5]王正书,周学东.粗煤泥分选工艺在安家岭选煤厂的应用[J].洁净煤技术,2012,18(3):7-9.
- [6]庞亮.粗煤泥分选工艺技术进展与展望[J].山东煤炭科技,2008(6):152-153.
- [7]韩恒旺,李炳才,訾涛,等.粗煤泥分选设备及分选工艺研究[J].洁净煤技术,2011,17(2):12-14.
- [8]于进喜,刘文礼,姚嘉胤,等.粗煤泥分选设备及其特点对比分析[J].煤炭科学技术,2010,38(7):114-117.
- [9]刘强.TBS分选机在余吾选煤厂的应用[J].洁净煤技术,2013,19(6):17-20.
- [10]刘爱荣,樊民强.聚丙烯酰胺对水介质旋流器分选性能的影响规律研究[J].太原理工大学学报,2014,45(1):62-64,75.
- [11]樊民强,董连平,杨宏丽,等.煤泥旋流重选柱:中国,200910073853.7[P].2009-12-02.
- [12]崔广文,郭启凯,宋国阳,等.三锥水介分选旋流器在粗煤泥分选中的应用[J].洁净煤技术,2013,19(1):1-4,26.
- [13]董连平,樊民强.大锥角水介质旋流器的应用研究[J].煤炭科学技术,2004,32(11):40-43.
- [14]姜利群,俞少功.水介质旋流器动力学模型的研究[J].中国矿业大学学报,1994,23(4):115-121.
- [15]杨晓锋,樊民强.新型粗煤泥两段旋流器分选试验研究[J].煤炭科学技术,2013,41(S1):373-375,378.
- [16]董连平.水介质旋流器结构参数研究与工业应用[D].太原:太原理工大学,2004.
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