首页> 外国专利> MINERAL COAL LIQUEFACTION PROCESS OF SHORT-TERM RESISTANCE INCLUDING CATALYTIC HYDROGENATION

MINERAL COAL LIQUEFACTION PROCESS OF SHORT-TERM RESISTANCE INCLUDING CATALYTIC HYDROGENATION

机译:包括加氢反应在内的短期抗矿性煤液化过程

摘要

Normally solid dissolved coal product and a distillate liquid product are produced by continuously passing a feed slurry comprising raw feed coal and a recycle solvent oil and/or slurry together with hydrogen to a preheating-reaction zone (26, alone, or 26 together with 42), the hydrogen pressure in the preheating-reaction zone being at least 1500 psig (105 kg/cm2), reacting the slurry in the preheating-reaction zone (26, or 26 with 42) at a temperature in the range of between about 455 DEG and about 500 DEG C. to dissolve the coal to form normally liquid coal and normally solid dissolved coal. A total slurry residence time is maintained in the reaction zone ranging from a finite value from about 0 to about 0.2 hour, and reaction effluent is continuously and directly contacted with a quenching fluid (40, 68) to substantially immediately reduce the temperature of the reaction effluent to below 425 DEG C. to substantially inhibit polymerization so that the yield of insoluble organic matter comprises less than 9 weight percent of said feed coal on a moisture-free basis. The reaction is performed under conditions of temperature, hydrogen pressure and residence time such that the quantity of distillate liquid boiling within the range C5-454 DEG C. is an amount at least equal to that obtainable by performing the process under the same condition except for a longer total slurry residence time, e.g., 0.3 hour. Solvent boiling range liquid is separated from the reaction effluent (83) and recycled as process solvent (16). The amount of solvent boiling range liquid is sufficient to provide at least 80 weight percent of that required to maintain the process in overall solvent balance.
机译:通常,通过将包含原料煤和循环溶剂油和/或浆料以及氢气的原料浆连续输送到预热反应区(单独的26或26与42一起的26)来生产固溶煤产品和液态液体产品。 ),预热反应区中的氢气压力至少为1500 psig(105 kg / cm2),使预热反应区(26,或26与42之间)中的浆液在约455至455之间的温度下反应在约500℃和约500℃下使煤溶解以形成通常为液态的煤和通常为固态的溶解的煤。在反应区中总浆料停留时间保持在约0至约0.2小时的有限值范围内,并且反应流出物连续且直接与淬灭流体(40、68)接触以基本上立即降低反应温度。排出到低于425℃以基本上抑制聚合反应,以不含水量计,不溶性有机物的产量占所述进料煤的少于9%(重量)。反应是在温度,氢气压力和停留时间的条件下进行的,以使沸点在C5-454℃范围内的馏出液的量至少等于通过在相同条件下进行该方法可获得的量。更长的总浆料停留时间,例如0.3小时。从反应流出物(83)中分离出溶剂沸程液体,并作为工艺溶剂(16)再循环。溶剂沸程液体的量足以提供维持该方法在整体溶剂平衡中所需量的至少80重量%。

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