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    高含水低品质细粒煤脱水脱灰协同提质研究

    Research on synergistic quality improvement of dewatering and ash removal of high-water content and low-quality fine coal

    • 摘要: 我国煤炭资源禀赋差,高含水、高含灰的低品质煤炭资源储量巨大,约占原煤储量40%。随着煤炭机械化综采技术的推广,原煤中<6 mm细粒煤含量逐渐超过50%。提出了脱水脱灰协同提质的工艺技术,开展了高含水低品质细粒煤脱水干燥、干法分选提质试验。首先,对6 mm等径颗粒间的液桥演变过程进行了研究,随液桥体积V的提升,最大液桥力可达825.16 μN,液桥断裂距离最大可达1.368 mm,这是因为液桥体积的增大,由初始构型的接触角前进量增大过程中产生的接触角滞后效应导致的。随颗粒分离速度v的增大,最大液桥力可达875.14 μN,最大断裂距离达0.171 mm,这是由于接触角的前进量增大以及液体粘滞性产生的接触角后退过程减缓导致的。其次,通过热风干燥技术探究了高含水细粒煤干燥前后水分含量的变化规律,粒度越大干燥所需时间越长,3~6 mm、0~3 mm颗粒在120 ℃时完全干燥时间分别为60 min和30 min,这是因为粒度越大内部水分迁移路径变长渗透到煤炭表面受到限制,干燥过程速率降低。当干燥温度由80 ℃增大至100 ℃时,水分可由剩余7.18%水分至完全脱除,干燥温度的升高同时提升了外界环境与煤炭的温度梯度,内部水分传质速率提高,因此干燥速率越快。最后,通过振动复合力场干法分选技术对脱水煤样进行脱灰提质试验,当振动频率f为42 Hz、床面气速vA为7.05 m/s时,料层在激振力与气流曳力作用下得到充分松散,料群密度空间分布理想,上下层灰分差异显著。振动频率对产品回收率影响显著,当振动频率为39 Hz时,精煤回收率与产率分别为56.56%、85.28%,灰分为12.54%,颗粒错配现象减少;振动频率f为39 Hz、床面气速vA为8.97 m/s时分离效果达到最佳,灰分离析度SA达到最大值为1.896。该技术适用于西部干旱缺水地区的高含水低品质细粒煤高效提质目的,具有不用水、运维成本低、提质效果显著的优势,为我国低品质细粒煤高效脱水脱灰提供技术储备。

       

      Abstract: The coal resources in China are poorly endowed, with huge reserves of low-quality coal with high water content and high ash content, accounting for about 40% of the original coal reserves. With the promotion of mechanized integrated mining technology, the content of <6 mm fine-grained coal in the raw coal gradually exceeds 50%. The process technology of dewatering and ash removal for synergistic quality improvement was proposed, and the tests of dewatering and drying, dry sorting and quality improvement of fine-grained coal with high water content and low quality were carried out. Firstly, the evolution of the liquid bridge between 6 mm isodiameter particles was investigated. With the increase of the liquid bridge volume V, the maximum liquid bridge force could reach 825.16 μN, and the maximum liquid bridge fracture distance could reach 1.368 mm, which was due to the increase of the liquid bridge volume caused by the contact angle hysteresis effect in the process of contact angle advance increase of the initial configuration. With the increase of particle separation velocity v, the maximum liquid bridge force can reach 875.14 μN, and the maximum fracture distance reaches 0.171 mm, which is due to the increase of the advancing volume of the contact angle as well as the slowing down of the backward process of the contact angle produced by the viscosity of the liquid. Secondly, through the hot air drying technology to explore the high moisture content of fine-grained coal before and after drying the law of change of moisture content, the larger the particle size of the longer drying time required, 3–6 mm, 0–3 mm particles at 120 ℃ complete drying time of 60 min and 30 min, respectively, this is because the larger the particle size of the internal migration path of moisture becomes longer penetration into the surface of the coal is limited, the rate of drying process is reduced. When the drying temperature increases from 80 ℃ to 100 ℃, the moisture content can be removed completely from the remaining 7.18% moisture, the increase in drying temperature at the same time to enhance the temperature gradient between the external environment and the coal, the internal moisture mass transfer rate is increased, so the drying rate is faster. Finally, through the vibration composite force field dry sorting technology on the dewatered coal samples to remove the ash and improve the quality of the test, when the vibration frequency f is 42 Hz, the bed surface gas velocity vA is 7.05 m/s, the material layer in the excitation force and the air flow trailing force under the action of the full loosening, the material density spatial distribution of the material group is ideal, and the upper and lower layers of the ash difference is significant. The vibration frequency has a significant effect on the product recovery rate, when the vibration frequency is 39 Hz, the refined coal recovery rate and yield are 56.56%, 85.28%, the ash content is 12.54%, and the particle mismatch phenomenon is reduced; when the vibration frequency f is 39 Hz and the bed air velocity vA is 8.97 m/s, the separation effect reaches the best, and the ash dissociation degree SA reaches a maximum of 1.896. This technology is suitable for the high water-scarce areas in the western arid and water-scarce regions. This technology is suitable for the purpose of high-efficiency quality improvement of low-quality fine-grained coal with high water content in the arid and water-scarce areas in the west of China, which has the advantages of no water use, low operation and maintenance cost, and remarkable quality improvement effect, and provides technical reserves for the high-efficiency dewatering and de-ash removal of low-quality fine-grained coal in China.

       

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