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Biomass to Fuels: Impact of Reaction Medium and Heating Rate

机译:生物质对燃料的影响:反应介质和加热速率的影响

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We have recently reported on the impact of CO2 on biomass gasification and its ability to more effectively gasifynbiomass than steam. Continuing this investigation has led to understanding the impact of heating rates andndifferent reaction environments. This article presents the results from the gasification of various biomass feedstocks.nHeating rates were varied from 1 to 1008C minu00011 to ballistic rates (*5008C minu00011). Gasification medianinvestigated include H2O=N2, CO2, CO2=N2=H2O, and O2=N2. Global activation energies for pyrolysis werenfound to be significantly higher than for gasification, whereas those for the grasses were significantly lower thannthe woods, possibly indicating a catalytic effect during pyrolysis of the high mineral content herbaceous feedstocks.nCO2 pyrolysis (110–4508C) activation energy values for lignin, cellulose, and biomass were 22–49, 202–n230, and 28–72 kJ molu00011, respectively, and CO2 gasification (500–7008C) values for lignin and biomass weren12–38 and 9–57 kJ molu00011, although cellulose did not exhibit significant mass loss in the gasification interval 500–n7008C. Using a least squares fit on the rate of mass loss fraction, the global decomposition reaction duringnpyrolysis for lignin in either medium was found to be third order, whereas that for cellulose was first order andnfor the various biomass samples either first or second order. The most significant difference in biomass processingnin CO2, when compared with steam gasification, occurred above 7508C where nearly all of the biomassnwas converted to volatiles with less than 2% ash remaining after CO2 gasification. Only when pure CO2 wasnused as the gasification medium under a slow heating rate did complete processing of the components to volatilenproducts occur. Gas chromatography analysis has shown the effect of CO2 on product distribution. Data arenpresented focusing on the relation between gasification medium, feedstock selection, and major chemical speciesnevolution.sustainable systems engineering;
机译:我们最近报道了二氧化碳对生物质气化的影响及其比蒸汽更有效地气化生物质的能力。继续进行这项研究已使人们了解了升温速率和不同反应环境的影响。本文介绍了各种生物质原料气化的结果。加热速率从1到1008C minu00011到弹道速率(* 5008C minu00011)不等。研究的气化中位数包括H2O = N2,CO2,CO2 = N2 = H2O和O2 = N2。未发现热解的总活化能明显高于气化的活化能,而草的总活化能显着低于木材,这可能表明高矿物质含量的草料在热解过程中具有催化作用。nCO2热解(110-4508C)活化能值木质素,纤维素和生物量分别为22–49、202–n230和28–72 kJ molu00011,木质素和生物质的CO2气化(500–7008C)值分别为12–38和9–57 kJ molu00011,尽管纤维素在500–n7008C的气化间隔内未表现出明显的质量损失。使用质量损失率的最小二乘拟合,发现在两种介质中木质素在热解过程中的整体分解反应是三级的,而对于纤维素,纤维素的分解反应是一阶的,而对于各种生物质样品的整体分解反应是一阶或二阶的。与蒸汽气化相比,CO2中生物量加工过程中最显着的差异发生在7508°C以上,在该温度下,几乎所有生物质都转化为挥发物,而CO2气化后残留的灰分少于2%。只有当在缓慢的加热速率下将纯净的CO2用作气化介质时,才发生将组分完全加工成挥发性产物的过程。气相色谱分析表明二氧化碳对产品分布的影响。呈现的数据侧重于气化介质,原料选择和主要化学物种演化之间的关系。

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