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Modeling of Thermochemical Conversion of Glycerol: Pyrolysis and H_2O and CO_2 Gasification

机译:甘油热化学转化的模型:热解和H_2O和CO_2气化

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Glycerol is the byproduct of biodiesel production. Biodiesel has been considered a strong alternative candidate to petro diesel. Stoichiometrically, one mole of glycerol is generated during the conversion of one mole of triglyceride feedstock or per three produced moles of biodiesel. This an equivalent to 10-15% byproduct volume/mass. The biodiesel production has observed a huge jump in production, being preserved as a renewable, sustainable and near CO2 neutral source. This is driven by advances in technology of 1st generation biomass lipid harvesting and advancement of 3rd generation breeding and maximizing algae lipids and their extraction. Therefore, a sound solution for velarizing the glycerol byproduct is becoming a necessity before it is viewed as waste burden. Currently, the glycerol market is saturated and substantial production can lead to an economic imbalance. Therefore, satisfying the energy needs following thermochemical conversion of glycerol into clean syngas fuel is a more favorable and dual solution to the problem, i.e. reducing process waste and generating clean fuel. In this work, the process metrics in using Glycerol as feedstock for the production of syngas fuel is evaluated under pyrolysis then gasification under steam (H2O(g)) and CO2 moderators. Process metrics are assessed using the syngas mole fractions and their normalized value termed as the cold gasification efficiency. The analysis followed equilibrium modeling based on Gibbs Energy Minimization and under sweeping reaction temperatures. The model is validated against experimental literature. Result of glycerol pyrolysis achieved a maximum of 83% at 0.43 CO and 0.57 H-2 mole fraction. Glycerol gasification under steam moderator resulted in a slightly higher efficiency of 84% and 0.20 CO and 0.55 H-2 mole fractions, while under CO2 moderator resulted in a lower efficiency of 80% and 0.40 CO and 0.30 H-2 mole fractions. This emphasizes the technical feasibility of thermochemical conversion of glycerol into clean syngas and closes the loop of biodiesel production towards zero byproduct process.
机译:甘油是生物柴油生产的副产品。生物柴油被认为是石油柴油的有力替代品。从化学计量上讲,在一摩尔甘油三酸酯原料的转化过程中或每三摩尔生产的生物柴油转化过程中会生成一摩尔甘油。这相当于10-15%的副产品量/质量。生物柴油的产量有了巨大的飞跃,被保留为可再生,可持续和接近二氧化碳中性的来源。这是由第一代生物质脂质收获技术的进步以及第三代育种的进步以及藻类脂质及其提取的最大化所推动的。因此,在将其视为废料负担之前,需要一种用于润滑甘油副产物的良好溶液。当前,甘油市场已经饱和,大量生产会导致经济失衡。因此,在将甘油热化学转化成清洁的合成气燃料之后满足能量需求是该问题的更有利和双重解决方案,即减少工艺浪费并产生清洁燃料。在这项工作中,使用甘油作为原料生产合成气燃料的过程指标是在热解,然后在蒸汽(H2O(g))和CO2调节剂气化的条件下进行评估的。使用合成气摩尔分数及其标准化值(称为冷气化效率)评估工艺指标。该分析遵循基于吉布斯能量最小化的平衡模型,且反应温度较高。该模型已根据实验文献进行了验证。甘油热解的结果在0.43 CO和0.57 H-2摩尔分数下最大达到83%。在蒸汽调节剂下甘油气化产生的效率略高,分别为84%和0.20 CO和0.55 H-2摩尔分数,而在CO2调节剂下产生的效率较低,分别为80%和0.40 CO和0.30 H-2摩尔分数。这强调了将甘油热化学转化为清洁合成气的技术可行性,并封闭了生物柴油生产向零副产物工艺发展的环路。

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