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    煤气化细渣氯化热平衡分析

    Thermal equilibrium analysis of chlorination of coal gasification fine slag

    • 摘要: 我国能源结构特点为富煤、贫油、少气,煤炭资源在我国能源结构中占据主体地位。煤气化技术可实现煤炭资源绿色化利用,但同时煤气化技术会产生大量残渣,一方面堆存造成土地资源的污染和浪费,另一方面其中储存的元素无法实现再次利用。现有的煤气化渣资源化工艺大都面临煤气化渣中炭–灰相互制约的问题,而氯化法可实现煤气化渣中炭–灰协同利用。利用HSC 6.0计算了榆林地区煤气化细渣中氧化物在不同CO生成几率下的ΔGθ,同时探究了煤气化细渣反应热Q与CO生成几率η和配氧量O%的关系。热力学计算结果表明:煤气化细渣中氧化物碳热氯化反应可以发生,同时随着η的变化,调整氯氧比有助于维持体系的热平衡,促进反应的连续发生。

       

      Abstract: China’s energy infrastructure is characterized by a coal abundance, oil scarcity, and limited natural gas. Coal resources dominate the country’s energy landscape. However, while coal gasification technology can enable the green utilization of these resources, it also generates substantial residue. Storing this residue poses environmental risks due to potential pollution and results in the wastage of valuable land. Additionally, these stored residues contain valuable elements that cannot be reused. A significant challenge in the current resource utilization processes of coal gasification slag is the mutual restriction between carbon and ash content in the slag. HSC 6.0 was used to calculate the Gibbs free energy of oxides in coal gasification fine slag from the Yulin region, considering different CO formation probabilities. The relationship between the reaction heat (Q) of coal gasification fine slag, CO formation probability (η), and oxygen content (O%) was also examined. The thermodynamic calculations suggest that the chlorination reaction of oxides in coal gasification fine slag is feasible. By adjusting the chlorine-to-oxygen ratio in conjunction with variations in η, it is possible to maintain the system’s thermal equilibrium and ensure the sustained progression of the reaction.

       

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