首页> 外文会议>Annual Loss Prevention Symposium; 20060424-27; Orlando,FL(US) >Enhanced Natural Gas and Methane Conversion intoMethanol in a Membrane Driven Reactor(Experimental Modeling and Simulative Comparisonwith Fixed Catalytic Reactors)
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Enhanced Natural Gas and Methane Conversion intoMethanol in a Membrane Driven Reactor(Experimental Modeling and Simulative Comparisonwith Fixed Catalytic Reactors)

机译:膜驱动反应器中天然气和甲烷转化为甲醇的增强(与固定催化反应器进行实验建模和模拟比较)

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Modeling and simulative comparison of catalytic permreactors (membrane drivenrnreactors) with fixed plug flow reactors (fixed catalytic reactors) is performed usingrnnumerical analysis techniques, for the synthesis gas (syngas) and methanol productionrnprocesses from methane and natural gas feedstocks. Experimental fixed catalytic reactorsrnare utilized to derive kinetic data for the catalytic methane-steam reforming and the waterrngas shift reactions using combined optimization-integration techniques. Experiments arernalso performed with catalytic membrane reactor modules (permreactors) for comparisonrnpurposes with the fixed catalytic reactors (the syngas to methanol process). The massrnand pressure balances of these reactors were solved numerically to provide the profiles ofrnpartial pressures or molar flowrates or fractional conversions and yields of each speciesrnalong the reactor axial length. Several other reactor parameters were varied in the numerical model to obtain the respective variation of conversion and yield at the reactorrnexit. Such parameters are the reactor temperature and pressure, space time, and reactorrndimensions. The developed numerical reactor models can be also used to predict thernreactors operation at different running conditions in order to increase the syngas andrnmethanol product yield.rnThe methane reforming and shift reactions under analysis are of special interest inrnsyngas and methanol generation and utilization processes. Utilization of improvedrnreactors and reaction systems for methanol production from natural gas is of highrnimportance in the recent fuel, gas, and transportation fuels industry. Methanol is a keyrnfuel and can be directly produced from the synthesis gas which is coming out from therncatalytic reforming of methane or natural gas as described in this paper. Use of methanolrnis mainly in transportation fuels, chemical synthesis, and as fuel in direct methanol fuelrncells (DMFC).rnHydrogen is also a main product from the reforming and related conversionrnreactions. Other hydrogen and syngas utilization processes include feed forrnelectrochemical fuel cells, hydrogen assisted combustion systems, hydrogen richrnhydrotreating of heavy oils, distillates and asphaltenes, chemical synthesis ofrnhydrogenated products (e.g., methanol and olefins).
机译:使用数值分析技术,对甲烷和天然气原料的合成气(合成气)和甲醇生产过程,使用固定活塞流反应器(固定催化反应器)进行了催化渗透反应器(膜驱动反应器)的建模和模拟比较。利用实验性固定催化反应器,利用组合的优化集成技术,获得了催化甲烷蒸汽重整和水煤气变换反应的动力学数据。还使用催化膜反应器模块(渗透反应器)进行了实验,以与固定催化反应器(合成气制甲醇工艺)进行比较。对这些反应器的质量和压力平衡进行了数值求解,以提供整个反应器轴向长度上的分压或摩尔流量或分数转化率和每种物质的产率的分布图。在数值模型中改变其他几个反应器参数以获得反应器出口处转化率和产率的各自变化。这些参数是反应器温度和压力,时空和反应器尺寸。所开发的数值反应器模型还可用于预测不同运行条件下反应器的运行情况,以提高合成气和甲醇产品的产率。分析中的甲烷重整和转化反应对于合成气和甲醇的产生和利用过程特别重要。在最近的燃料,天然气和运输燃料工业中,利用改进的反应器和反应系统从天然气生产甲醇非常重要。如本文所述,甲醇是一种关键燃料,可以直接从甲烷或天然气的催化重整过程中产生的合成气中生产。甲醇主要用于运输燃料,化学合成以及作为直接甲醇燃料电池(DMFC)中的燃料。氢也是重整和相关转化反应的主要产物。其他的氢气和合成气利用过程包括供气式电化学燃料电池,氢气辅助燃烧系统,重油,馏出物和沥青质的富氢加氢处理,氢化产物(如甲醇和烯烃)的化学合成。

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