BGL气化炉新型建模方法及优化分析

Xiaoxue Guo, Liangqi Chen, Xiaolong Zhu,Quancong Zhang,Zhikai Cao,Hua Zhou

CHINESE SCIENCE BULLETIN-CHINESE(2021)

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Abstract
充分考虑碎煤加压熔渣气化(British Gas Lurgi,BGL)炉内的流动特性,将BGL气化炉分为并流段和逆流段,并依此建立了BGL气化炉的一维稳态机理模型.并利用该模型模拟了以烟煤为原料的某工业BGL气化炉,模拟结果与工业实测值误差小于2%,从而验证该模型的正确性.然后在所得到模型的基础上探讨了氧煤比及汽煤比对气化性能的影响.研究表明,氧煤比对碳转化率以及蒸汽分解率的影响较大,随着氧煤比增加,碳转化率增大,蒸汽分解率先增大后减小,当氧煤比为0.47时,蒸汽分解率最大;汽煤比增大有利于水煤气变换反应,但该反应受化学平衡限制,当气化剂充足时,蒸汽的消耗量将小于其增加量,随着汽煤比增大蒸汽分解率逐渐降低.
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Key words
BGL (British Gas Lurgi) gasifier, concurrent-flow, countercurrent-flow, mathematical model, oxygen-to-coal ratio, steam-to-coal ratio
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