煤炭工程 ›› 2026, Vol. 58 ›› Issue (4): 204-212.doi: 10.11799/ce202604024

• 研究探讨 • 上一篇    下一篇

超高压条件下细粒煤的脱水渗流特性研究

何俩勇,马晓敏,郝小贝,董晓明,樊玉萍,董宪姝   

  1. 1.太原理工大学 矿业工程学院,山西 太原 030024

    2.潞安化工集团余吾煤业有限责任公司,山西 长治 046101

    3.北京中煤煤炭洗选技术有限公司,河北 雄安 070001

  • 收稿日期:2025-10-31 修回日期:2025-12-22 出版日期:2026-04-10 发布日期:2026-05-12
  • 通讯作者: 马晓敏 E-mail:ma_xiaomin@126.com

Dewatering seepage characteristics of fine coal under ultra-high pressure #br#

  • Received:2025-10-31 Revised:2025-12-22 Online:2026-04-10 Published:2026-05-12

摘要:

为揭示细粒煤在超高压压滤脱水过程中的渗流规律及药剂调控机理,以平顶山矿区细粒煤为研究对象,开展了不同压力阶段(0~5MPa)及药剂作用(CPAMSDBS)下的压滤脱水试验。结果表明,试验煤样粒度细、比表面积大、孔径集中于微米级(<5μm),导致其滤饼具有高比阻和强吸附特性,是难脱水的主要原因。压力对滤饼厚度的减小作用在不同体系中具有高度的一致性,均遵循“初始快速压缩、中压非线性过渡、高压线性压实”的阶段性规律。药剂的加入显著强化了滤饼的压缩效应,其影响程度排序为:CPAM>SDBS>不加药。试验数据显示:在2.5MPa条件下,CPAM浓度为40g/t时脱水效果最优,滤饼含水率降至21.3%;SDBS 则通过降低界面张力改善脱水效果,在1000g/t时含水率最低(23.9%)。在初始阶段(0~0.6MPa),CPAM与SDBS分别使压缩速率较不加药组提高25%和30%;进入高压阶段(2.5~5.0MPa)后,CPAM组效果最佳,滤饼厚度从19.85mm降至8.95mm,最终含水率低至22.16%,而SDBS组及不加药组在高压段的变形量则相对受限。

Abstract:

To reveal the seepage laws and agent regulation mechanisms of fine-grained coal during high-pressure filter-press dewatering, this study takes fine-grained coal from the Pingdingshan Mining Area as the research object, and systematically conducts filter-press dewatering experiments under different pressure stages (0-5MPa) and agent conditioning (CPAM and SDBS). The results show that the fine-grained coal from Pingdingshan has fine particle size, large specific surface area, and pore size concentrated in the micron range (<5μm), leading to high specific resistance and strong adsorption characteristics of the filter cake, which are the main reasons for difficult dewatering. The effect of pressure on reducing filter cake thickness is highly consistent across different systems, all following the phasic law of "initial rapid compression, medium-pressure nonlinear transition, and high-pressure linear compaction". The addition of agents significantly enhances the compression effect of the filter cake, with the order of influence intensity being: CPAM > SDBS > no agent. Experimental data indicate that under the condition of 2.5MPa, the dewatering effect is optimal when the CPAM concentration is 40g/t, with the filter cake moisture content decreasing to 21.3%; SDBS improves the dewatering effect by reducing interfacial tension, achieving the lowest moisture content (23.9%) at a concentration of 1000g/t. In the initial stage (0–0.6MPa), CPAM and SDBS increase the compression rate by 25% and 30% respectively compared with the no-agent group; after entering the high-pressure stage (2.5–5MPa), the CPAM group exhibits the best effect, with the filter cake thickness decreasing from 19.85mm to 8.95mm and the final moisture content as low as 22.16%, while the deformation of the SDBS group and the no-agent group is relatively limited in the high-pressure stage.

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