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Modelling of a reverse-flow partial oxidation reactor for synthesis gas production from gasifier product gas.

机译:用于从气化炉产物气生产合成气的逆流部分氧化反应器的建模。

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摘要

Biomass gasification followed by fuel synthesis is one of the alternatives for producing liquid fuels and chemicalsfrom biomass feedstocks. The gas produced by gasification contains CO, H2, H2O, CO2, light hydrocarbons and tars. Thelight hydrocarbons can account for as much as 50% of the total energy content of the gas, depending on the type of gasifier,operating conditions and feedstock. The gas also contains catalyst poisons such as sulphur, in the form of H2S and COS. Thispaper presents simulations of a reverse-flow partial-oxidation reformer that converts the light hydrocarbons into more synthesisgas, while achieving efficiencies approaching that of conventional catalytic processes. Variations in parameters such as pressure,amount of oxidant and steam-to-carbon ratio were also investigated. Simulations of the reforming of natural gas were includedfor comparison. The results show the benefits of using reverse-flow operation with lean gases such as gasifier product gas.
机译:生物质气化然后进行燃料合成是从生​​物质原料生产液体燃料和化学品的替代方法之一。气化产生的气体包含CO,H2,H2O,CO2,轻烃和焦油。取决于气化炉的类型,操作条件和原料,轻烃可占气体总能量的50%。该气体还包含H2S和COS形式的催化剂毒物,例如硫,本文提供了模拟的逆流部分氧化重整器,该重整器将轻烃转化为更多的合成气,同时达到了接近传统催化过程的效率。还研究了压力,氧化剂量和水蒸气碳比等参数的变化。为了比较,还包括了天然气重整的模拟。结果显示了对稀薄气体(如气化炉产物气)使用逆流操作的好处。

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