摘要
针对水煤气甲烷化多段绝热反应平衡计算模型,建立了“迭代循环、大小跨步、直接寻优”的数值求解方法,并给出了工业计算实例。
A numerical solution of 'iteration method with large and small step directly searching optimum value 'is set up for the equilibrium model of gas methanation in multistage adiabatic reactor. An application example is also listed.
出处
《化肥设计》
CAS
1997年第6期13-15,共3页
Chemical Fertilizer Design