The continuous suspension crystallization process for xylene separation was optimized by calculation of solid-liquid phase equilibrium, material balance and energy balance.
采用混合二甲苯二组分物系的固液相平衡方程及物料衡算和热量衡算方程对混合二甲苯连续悬浮结晶工艺进行模拟计算。
Based on material balance, energy balance and chemical equilibrium, the mathematic model of gasification has been established.
基于物料平衡、能量平衡和化学平衡分析，建立了一种气化数学模型。
Based on material balance, energy balance and chemical equilibrium a mathematical model of high temperature air gasification was established.
建立了一种基于物料平衡、能量平衡和化学平衡分析的气化数学模型。
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