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首页   >    矿业工程

焦家金矿全尾砂絮凝浓密试验研究

  • 作者:
  • 何潇亮1,肖崇春1,蔚登峰2,寇云鹏3,陈秋松4,邱剑辉5*

  • 作者单位:
  • (1. 飞翼股份有限公司;2. 山东黄金矿业(莱州)有限公司焦家金矿;3. 山东黄金集团有限公司充填工程实验室; 4. 北京科技大学资源与安全工程学院;5. 中南大学资源与安全工程学院)
  • 基金项目:

  • 国家自然科学基金青年项目(52104156)
  • 详细信息:

  • 作者简介:
  • 何潇亮(1985—),男,工程师,研究方向为矿山充填与矿山机电;E⁃mail:251703699@qq. com
  • PDF下载

Experimental study on flocculation and thickening of ungraded tailings from the Jiaojia Gold Mine

  • English Author:
  • He Xiaoliang¹, Xiao Chongchun¹, Wei Dengfeng², Kou Yunpeng³, Chen Qiusong⁴, Qiu Jianhui5

  • Unit:
  • (1. Feiyi Co., Ltd.; 2. Jiaojia Gold Mine, Shandong Gold Mining(Laizhou)Co., Ltd.; 3. Backfilling Engineering Laboratory of Shandong Gold Group Co., Ltd.; 4. School of Resources and Safety Engineering, University of Science and Technology Beijing; 5. School of Resources and Safety Engineering, Central South University)
  • 摘要
  • 在线预览
  • 参考文献

摘要:

针对焦家金矿全尾砂处理中絮凝剂单耗高、底流浓度不稳定等问题,通过静态絮凝沉降、动态浓密及半工业深锥浓密试验,系统研究了全尾砂絮凝浓密影响规律及优化工艺。结果表明:静态试验中,阴离子型絮凝剂K739在矿浆浓度 12 %、添加量 15 g/t条件下沉降效果最优,底流浓度显著提升,絮凝剂过量会导致絮团蓬松化并增加沉降阻力;动态试验中,处理量为 0.6 t/(m²·h)时,底流浓度达 67.66 %,溢流水含固量低于 200×10-6,延长压缩时间可进一步提高底流浓度;半工业试验验证了处理量与底流浓度的负相关关系,综合考虑溢流水含固量不高于 200×10-6,推荐浓密机处理量为 0.7 t/(m²·h)。通过优化矿浆浓度、絮凝剂用量及处理量,并增加浓密机高度以延长压缩时间,可实现底流浓度 72 %以上的稳定控制,为矿山尾砂膏体充填和资源化利用提供了理论与技术支撑。

关键词:

全尾砂;深锥浓密;絮凝沉降;动态浓密;膏体充填;资源化利用

Abstract:

To address the issues of high unit consumption of flocculant and unstable underflow concentration in thetreatment of ungraded tailings at the Jiaojia Gold Mine, a series of static flocculation-settling tests, dynamic thickeningtests, and semi⁃industrial deep⁃cone thickening tests were conducted to systematically investigate the influencingfactors and optimize the flocculation-thickening process. Results show that in static tests, the anionic flocculant K739produced optimal settling performance at a pulp concentration of 12 % and a dosage of 15 g/t, significantly improvingunderflow concentration. However, overdosing led to loose floc structures and increased settling resistance. In dynamictests, when the treatment rate was 0.6 t/(m²·h), the underflow concentration reached 67.66 %, with the overflow solidcontent below 200×10⁻⁶. Prolonging the compression time further improved the underflow concentration. Semi⁃industrialtests confirmed a negative correlation between treatment rate and underflow concentration. Considering the requirementthat overflow solid content should not exceed 200×10⁻ ⁶ , a recommended thickener throughput of 0.7 t/(m²·h)wasproposed. By optimizing slurry concentration, flocculant dosage, and treatment rate, and by increasing thickener heightto extend compression time, stable underflow concentrations above 72 % can be achieved. This provides both theoreticaland technical support for paste backfilling and resource⁃based utilization of mine tailings.

Keywords:

ungraded tailings; deep⁃cone thickening; flocculation and settling; dynamic thickening; paste backfilling;resource⁃based utilization