首页> 外文会议>World hydrogen energy conference >Analysis of Liquid Hydrogen Production from Methane and Landfill Gas
【24h】

Analysis of Liquid Hydrogen Production from Methane and Landfill Gas

机译:甲烷和垃圾填埋气体液氢生产分析

获取原文

摘要

Several process flowsheets were conceived and analyzed, using Aspen Technology'sHYSYS?chemical process simulator for the production of liquid hydrogen from methaneand landfill gas. Hydrogen (H2) was produced by the autothermal pyrolysis of methane(CH4). The energy required for CH4 pyrolysis was derived from its partial combustion.The outlet stream of the autothermal reactor is a gaseous mixture containing CH4, H2, carbonmonoxide (CO), carbon dioxide (CO2) and water. This stream was separated into itscomponents by cryogenic distillation. The portion containing CH4 and CO passed through ahigh temperature gas conditioning reactor (HTGCR) or a low temperature gas conditioningreactor (LTGCR). The recycled stream was then mixed with the main stream from theautothermal methane pyrolysis reactor and redirected to the separation process. Fiveflowsheet scenarios were conceived and analyzed.The extent of H2 recovery from these processes were as high as 99.99% with hydrogen purityat 99.9999% level. The feedstock methane and landfill gases were utilized at 99.99% level.These processes generate high-purity carbon dioxide in liquid form that can be collected andsold or easily sequestered. The total process efficiencies calculated exceeded 81% and 79%for methane and landfill gas, respectively. The highest exergy efficiency was about 57%(for methane) and 51% (for landfill gas); assuming 10% heat loss from the process and 30%cryogenic refrigeration process efficiency. The ratio of CO2 to H2 produced in these processesvaried in the range of 3.027 to 4.219 (g/g).
机译:使用Aspen Technology'Shysys进行了构思和分析了几个过程流程,用于制造来自甲基填埋气体的液体氢气的化学过程模拟器。通过甲烷(CH 4)的自热热解产生氢气(H2)。 CH 4热解所需的能量源自其部分燃烧。自热反应器的出口流是含有CH 4,H 2,碳氧化碳(CO),二氧化碳(CO 2)和水的气态混合物。通过低温蒸馏将该物流分成其组分。含有CH 4和Co的部分通过A高温气体调节反应器(HTGCR)或低温气体调节反应器(LTZCR)。然后将再循环物流与来自瑟温甲烷热解反应器的主流混合并重定向到分离过程。构思和分析了五个流程的情景。这些过程的H2恢复程度高达99.99%,氢气pureityat 99.9999%水平。原料甲烷和垃圾填埋气体在99.99%水平下使用。这些方法在可以收集的液体形式中产生高纯度二氧化碳,可以收集和易于隔离。计算的总处理效率分别超过甲烷和垃圾填埋气体的81%和79%。最高的效率约为57%(对于甲烷)和51%(适用于垃圾填埋气);假设从过程中的10%热量损失和30%的低温制冷过程效率。这些过程中产生的CO 2至H 2的比率在3.027至4.219(g / g)的范围内。

著录项

相似文献

  • 外文文献
  • 中文文献
  • 专利
获取原文

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