首页> 外国专利> A process flow sheet for pre-treatment of high ash coal to produce clean coal

A process flow sheet for pre-treatment of high ash coal to produce clean coal

机译:用于高灰分煤预处理以生产清洁煤的工艺流程图

摘要

Disclosed is a process to produce low ash clean coal from high ash coal with substantially complete solvent recovery, the process comprising: (i) forming a slurry of coal fines in a solvent mixture of N-Methyl-2-pyrrolidone (NMP) with Ethylenediamine (EDA); (ii) maintaining said slurry in a reactor at a temperature range of 100°C to 240°C and a pressure range of 1 to 4 gauge (kg/cm2) for a period of 15 minutes to 4 hours; (iii) separating the produced sample after withdrawal from the reactor, 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 sample being a filtrate or extract and the second part being a reject; (iv) washing the reject obtained in step (iii) in an anti-solvent (such as water); (v) separating the washed reject obtained in step (iv) by filtration, said separated reject having a high ash content; (vi) feeding the extract obtained in step (iii) into an evaporator to recover 80-85% solvent and to obtain concentrated material; (vii) precipitating the concentrated material obtained in step (vi) into an anti-solvent tank to separate coal from solvent; (viii) separating the precipitated concentrated material of step (vii) by filtration to obtain separated coal, said separated coal having a reduced ash content; (ix) feeding anti-solvent and solvent resulting from step (vii) as a mixture in a distillation column to separate remaining solvent from the anti-solvent for reuse in the process.
机译:公开了一种由高灰分煤生产具有基本完全溶剂回收能力的低灰分清洁煤的方法,该方法包括:(i)在N-甲基-2-吡咯烷酮(NMP)与乙二胺的溶剂混合物中形成煤细粉的浆料。 (EDA); (ii)将所述浆料在反应器中在100℃至240℃的温度范围和1至4表压(kg / cm 2)的压力范围内保持15分钟至4小时的时间; (iii)从反应器中取出后分离生产的样品,分离切割的尺寸取决于要处理的粒径,包括最终产物的施用,分离样品的第一部分是滤液或提取物,第二部分是拒绝(iv)用抗溶剂(例如水)洗涤步骤(iii)中获得的废品; (v)通过过滤分离步骤(iv)中获得的洗涤后的废料,所述分离的废料具有高的灰分含量; (vi)将步骤(iii)中获得的提取物送入蒸发器中以回收80-85%的溶剂并获得浓缩的物质; (vii)将步骤(vi)中获得的浓缩材料沉淀到反溶剂罐中以将煤与溶剂分离; (viii)通过过滤分离步骤(vii)的沉淀的浓缩材料以获得分离的煤,所述分离的煤具有降低的灰分含量; (ix)将步骤(vii)得到的抗溶剂和溶剂作为混合物进料到蒸馏塔中,以从抗溶剂中分离剩余的溶剂以在该方法中重复使用。

著录项

相似文献

  • 专利
  • 外文文献
  • 中文文献
获取专利

客服邮箱:kefu@zhangqiaokeyan.com

京公网安备:11010802029741号 ICP备案号:京ICP备15016152号-6 六维联合信息科技 (北京) 有限公司©版权所有
  • 客服微信

  • 服务号