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Experimental investigation of a multi-stage air-steam gasification process for hydrogen enriched gas production

机译:多级空气蒸汽气化工艺生产富氢气体的实验研究

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To achieve hydrogen-rich and low-tar producer gas, multi-stage air-blown and air-steam gasification processes were studied in this research. Results showed that the tar content from multi-stage air-blown and air-steam gasification were lower, compared to the average value of that from downdraft gasification. In the cases of air supplies of 80, 1001min~(-1) and 100, 1001min~(-1) with steam, hydrogen yields were increased by 40.71 and 41.62%, respectively, compared to that without steam. These were about 1.6 times of hydrogen flow rate of the base case (S/B = 0). However, it was found that too much steam added to the process was disadvantageous. The equilibrium model was also applied to predict the hydrogen production and the composition of producer gas obtained from the multi-stage air-blown and air-steam gasification processes. The predicted result showed a better match for the case of multi-stage air-blown gasification process. Copyright.
机译:为了获得富氢和低焦油的生产气,在本研究中研究了多级风吹和空气蒸汽气化工艺。结果表明,多级风吹气化和空气蒸汽气化的焦油含量均低于下吹气化的平均值。在有蒸汽的80、1001min〜(-1)和100、1001min〜(-1)的供气情况下,与没有蒸汽相比,氢气的产率分别增加了40.71%和41.62%。这是基本情况下氢气流速的1.6倍(S / B = 0)。但是,发现向该过程中加入过多的蒸汽是不利的。平衡模型还用于预测氢气的产生和从多级风吹和空气蒸汽气化过程中获得的生产气的组成。预测结果显示出与多级气吹气化工艺情况更好的匹配。版权。

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