首页> 外文期刊>Fuel >Methane steam reforming modeling in a palladium membrane reactor
【24h】

Methane steam reforming modeling in a palladium membrane reactor

机译:钯膜反应器中甲烷蒸汽重整模型

获取原文
获取原文并翻译 | 示例
           

摘要

A mathematical model of a membrane reactor used for methane steam reforming was developed to simulate and compare the maximum yields and operating conditions in the reactor with that in a conventional fixed bed reactor. Results show that the membrane reactor resents higher methane conversion yield and can be operated under milder conditions than the fixed bed reactor, and that membrane thickness is the most important construction parameter for membrane reactor success. Control of the H_2:CO ratio is possible in the membrane reactor making this technology more suitable for production of syngas to be used in gas-to-liquid processes (GTL).
机译:建立了用于甲烷蒸汽重整的膜反应器的数学模型,以模拟和比较反应器与常规固定床反应器中的最大产率和操作条件。结果表明,与固定床反应器相比,膜反应器具有更高的甲烷转化率,并且可以在较温和的条件下运行,并且膜厚度是膜反应器成功的最重要的构造参数。可以在膜反应器中控制H_2:CO的比例,从而使该技术更适合生产用于气液工艺(GTL)的合成气。

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