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基于离散元法的浮选煤粒运动状态研究OA

Research on the movement state of flotation coal particles based on discrete element method

中文摘要英文摘要

细微粒级煤粒与气泡的相互运动由于其微观程度高和复杂性,研究者难以深入阐明其运动状态.通过离散元法构建了不同灰分煤粒在气泡上的模拟程序,模拟了粒级为74 μm~125 μm、灰分含量为14%和85%的煤粒在静水条件下在气泡上的运动状态,并通过自主搭建的煤粒-气泡作用行为观测装置进行了验证实验.模拟结果表明,煤粒在气泡上的运动行为可分为三个阶段:自由沉降阶段、液膜排水阶段(1.速度减缓阶段;2.沿气泡滑移阶段;3.刺破液膜形成三相接触线(three-phase contact line,TPCL)阶段)、沿三相接触线滑动阶段.煤粒以自由沉降末速接近气泡,在接近气泡时由于液膜排水导致速度减缓,其中14%灰分煤粒具有完整的液膜排水过程,其液膜排水时间为1 225 ms,其接近气泡时的速度减缓时间为557 ms,85%灰分煤粒无法形成完整的液膜排水过程,其接近气泡时的速度减缓时间为169 ms.煤粒与气泡接触后速度骤降为最小值后沿表面液膜滑动.滑动过程中,14%灰分煤粒在气泡上刺破液膜,速度发生突变,形成三相接触线并沿气泡滑移,煤粒到达气泡横对称轴时速度达到最大(2.37 mm/s),最终煤粒停留在气泡底部;85%灰分煤粒在液膜上加速滑动,在气泡横对称轴处达到最大速度(8.95 mm/s),煤粒从横对称轴处脱附.实验结果表明,灰分与颗粒的液膜排水时间呈负相关,与滑移速度呈正相关.

The mutual movement between fine coal particles and bubbles is difficult to fully clarify due to its microscopic nature and complexity.In this paper,a simulation program for coal particles with different ash contents moving on bubbles was constructed by the discrete element method.The movement states of coal particles with particle sizes of 74 μm‒125 μm and ash contents of 14%and 85%on bubbles under still water conditions were simulated,and verified by an independently built coal particle-bubble interaction behavior observation device.The simulation results show that the movement behavior of coal particles on bubbles can be divided into three stages:free settling stage,liquid film drainage stage(1.speed reduction stage;2.sliding along the bubble stage;3.rupturing the liquid film to form a three-phase contact line stage),and sliding along the three-phase contact line(TPCL)stage.Coal particles approach the bubble at the terminal velocity of free settling.When approaching the bubble,the speed is reduced due to liquid film drainage.The 14%ash content coal particles have a complete liquid film drainage process,with a liquid film drainage time of 1 225 ms and a speed reduction time of 557 ms when approaching the bubble.The 85%ash content coal particles cannot form a complete liquid film drainage process,and the speed reduction time when approaching the bubble is 169 ms.After contacting the bubble,the speed of the coal particles drops sharply to the minimum and the particles slide along the surface liquid film.During the sliding process,the 14%ash content coal particles rupture the liquid film on the bubble,and the speed changes suddenly,forming a three-phase contact line(TPCL)and sliding along the bubble.The speed reaches the maximum(2.37 mm/s)at the horizontal symmetry axis of the bubble and finally stays at the bottom of the bubble;the 85%ash content coal particles accelerate sliding on the liquid film,reaching the maximum speed(8.95 mm/s)at the horizontal symmetry axis of the bubble and detaching from the horizontal symmetry axis.The test results show that the ash content is negatively correlated with the liquid film drainage time of the particles and positively correlated with the sliding speed.

谢泽钰;张继龙;李涌;王向廷;徐丽红

太原理工大学矿业工程学院,030024 太原||山西省“1331工程”煤泥高效分选工程研究中心,030024 太原太原理工大学矿业工程学院,030024 太原||山西省“1331工程”煤泥高效分选工程研究中心,030024 太原||纽普瑞(山西)科技有限公司,030699 山西晋中太原理工大学矿业工程学院,030024 太原||山西省“1331工程”煤泥高效分选工程研究中心,030024 太原太原理工大学矿业工程学院,030024 太原||山西省“1331工程”煤泥高效分选工程研究中心,030024 太原纽普瑞(山西)科技有限公司,030699 山西晋中

矿业与冶金

细粒级煤浮选离散元法疏水性气泡

fine grained coalflotationdiscrete element methodhydrophilicity and hydro-phobicitybubble

《煤炭转化》 2026 (3)

1-13,13

山西省专利转化专项项目(202202053)、山西省"1331工程"资助项目(2018-5-2)和山西省基础研究计划项目(202203021211142)

10.19726/j.cnki.ebcc.202603001

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