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Analysis of Hydrogen Generation through Thermochemical Gasification of Coconut Shell Using Thermodynamic Equilibrium Model Considering Char and Tar

机译:考虑焦炭和焦油的热力学平衡模型分析椰子壳热化学气化制氢

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摘要

This work investigates the potential of coconut shell for air-steam gasification using thermodynamic equilibrium model. A thermodynamic equilibrium model considering tar and realistic char conversion was developed using MATLAB software to predict the product gas composition. After comparing it with experimental results the prediction capability of the model is enhanced by multiplying equilibrium constants with suitable coefficients. The modified model is used to study the effect of key process parameters like temperature, steam to biomass ratio, and equivalence ratio on product gas yield, composition, and heating value of syngas along with gasification efficiency. For a steam to biomass ratio of unity, the maximum mole fraction of hydrogen in the product gas is found to be 36.14% with a lower heating value of 7.49 MJ/Nm3 at a gasification temperature of 1500 K and equivalence ratio of 0.15.
机译:这项工作使用热力学平衡模型研究了椰子壳在空气蒸汽气化中的潜力。使用MATLAB软件开发了一个考虑焦油和实际焦炭转化的热力学平衡模型,以预测产物气体的组成。与实验结果进行比较后,通过将平衡常数乘以合适的系数来增强模型的预测能力。修改后的模型用于研究关键工艺参数(例如温度,蒸汽与生物质之比和当量比)对合成气的产气收率,组成和热值以及气化效率的影响。对于蒸汽与生物质的统一比率,发现气化温度为1500 K时,产物气中氢的最大摩尔分数为36.14%,热值较低,为7.49 MJ / Nm 3 当量比为0.15。

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