The invention relates to an improved process to produce low ash clean coal from high ash coal with high recovery of enhanced quality of clean coal, the process comprising forming a slurry of coal fines in organic solvent with a small amount of co-solvent; maintaining said slurry in a reactor at a temperature range of 1OO°C to 240°C and at a pressure range of 1 to 4 gauge (kg/cm2) for a period of about 15 minutes to 4 hours; separating the produced product after withdrawal from the reactor in a separation unit, separation cut size being variable depending on the particle size to be treated including application of the end product, a first part of the separated product being a filtrate or extract and a second part being a reject; washing the reject in an anti solvent by adding second part called reject; drying the reject by a horizontal dryer, said separated reject having high ash content; feeding the extracted part into an evaporator to recover solvents; feeding the concentrated material (bottom product of evaporator) into a vertical dryer to separate coal from solvent, said separated coal having a reduced ash content
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机译:本发明涉及一种由高灰分煤生产低灰分的清洁煤的改进方法,该方法具有高回收率,提高了清洁煤的质量,该方法包括在有机溶剂中用少量助溶剂形成煤细粉的浆液。将所述浆料在反应器中在100℃至240℃的温度范围内和在1至4表压(kg / cm 2)的压力范围内保持约15分钟至4小时的时间;从反应器中取出后,在分离单元中分离出生产的产物,分离切割的尺寸取决于要处理的颗粒大小,包括最终产物的施用,分离产物的第一部分是滤液或提取物,第二部分是被拒绝;加入第二部分废料,在抗溶剂中洗涤废料;用水平干燥机干燥废料,所述分离的废料具有高的灰分含量;将提取的部分送入蒸发器以回收溶剂;将浓缩的物料(蒸发器的底部产物)送入立式干燥机,以将煤与溶剂分离,所述分离的煤具有降低的灰分含量
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