煤炭工程 ›› 2026, Vol. 58 ›› Issue (6): 214-221.doi: 10.11799/ce202606027

• 研究探讨 • 上一篇    下一篇

月桂酸甲酯诱导疏水团聚强化细粒低阶煤浮选机理研究

郝 赫,王治帅,卓启明,焦小淼,车森宇,王泽楠   

  1. 1. 内蒙古双欣矿业有限公司,内蒙古 鄂尔多斯 454000

    2. 威海市海王科技有限公司,山东 威海 264203

    3. 中国矿业大学(北京)化学与环境工程学院,北京 100083

    4. 煤炭科学研究总院有限公司,北京 100013

  • 收稿日期:2026-01-11 修回日期:2026-03-25 出版日期:2026-06-15 发布日期:2026-06-24
  • 通讯作者: 卓启明 E-mail:zhuoqiming92@126.com

Enhancement of fine low-rank coal flotation by methyl laurate-induced hydrophobic agglomeration and its mechanism #br#

  • Received:2026-01-11 Revised:2026-03-25 Online:2026-06-15 Published:2026-06-24

摘要:

针对高灰细粒低阶煤浮选回收困难的问题,本文提出并验证了一种基于酯类捕收剂诱导的疏水团聚-浮选工艺。以内蒙古东胜矿区煤泥为对象,比较了正十二烷与月桂酸甲酯两类捕收剂的改性与团聚行为,考察了预搅拌转速对团聚-浮选效果的影响。结合接触角测定、FTIRXPS等表征手段,揭示了酯类捕收剂在煤表面的选择性吸附机理。主要结果如下:原煤接触角为28.1°;加入正十二烷后接触角增至41.9°,经疏水团聚处理后提升至48.7°;月桂酸甲酯处理后接触角达50.7°,经疏水团聚后进一步提升至56.6°。浮选性能方面,在用量范围1000~4000g/t内,十二烷使精煤产率由19.87%增至27.12%,而月桂酸甲酯使产率由41.11%增至58.78%;在以月桂酸甲酯进行预搅拌诱导团聚时,转速2000r/min 可使精煤产率达64.02%(灰分约20%);采用月桂酸甲酯∶十二烷=13的复合药剂时,产率为61.73%,能兼顾效果与成本。FTIR显示,月桂酸甲酯处理后, 煤中自缔合羟基相对面积显著下降;XPS分析表明,经月桂酸甲酯处理后,C1sC—O比例降至15.01%O1sC—O比例亦明显下降,表明酯类捕收剂优先与羟基等含氧位点发生弱氢键/偶极相互作用。

Abstract:

To address the poor flotation recovery of high–ash fine low–rank coal, this study proposes and validates a hydrophobic agglomeration–flotation process induced by an ester–type collector. Coal slime from the Dongsheng mining area, Inner Mongolia, was used as the research object to comparatively investigate the surface modification and agglomeration behaviors of n–dodecane and methyl laurate, as well as the effect of preconditioning agitation speed on agglomeration–flotation performance. In combination with contact angle measurements, Fourier transform infrared spectroscopy (FTIR), and X–ray photoelectron spectroscopy (XPS), the selective adsorption mechanism of the ester–type collector on the coal surface was elucidated. The results show that the contact angle of the raw coal was only 28.1°; after treatment with n–dodecane, it increased to 41.9° and further to 48.7° following hydrophobic agglomeration, whereas treatment with methyl laurate increased the contact angle to 50.7°, which was further enhanced to 56.6° after hydrophobic agglomeration. In terms of flotation performance, within a dosage range of 1000–4000 g/t, the clean coal yield increased from 19.87% to 27.12% with n–dodecane, while it increased from 41.11% to 58.78% with methyl laurate. When hydrophobic agglomeration was induced by preconditioning with methyl laurate, a stirring speed of 2000 r/min resulted in a clean coal yield of 64.02% with an ash content of approximately 20%. Moreover, the use of a composite reagent system with a methyl laurate to n–dodecane mass ratio of 1:3 achieved a clean coal yield of 61.73%, thereby balancing flotation performance and reagent cost. FTIR analysis revealed a significant reduction in the relative proportion of self–associated hydroxyl groups after methyl laurate treatment, while XPS analysis showed that the proportion of C–O species in the C 1s spectrum decreased to 15.01%, accompanied by a pronounced decrease in C–O species in the O 1s spectrum, indicating that ester–type collectors preferentially interact with oxygen–containing sites such as hydroxyl groups via weak hydrogen bonding and/or dipole–dipole interactions.

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