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将三维非平衡混合池模型作了适当简化，并对烃类物系和非理想溶液进行了模拟计算，模拟结果与生产实测数据和文献报道值十分接近。
The three-dimensional non-equilibrium mixing cell model is simplified appropriately, and the hydrocarbon system and non-ideal solution are simulated. The simulation results are close to the measured data and reported values in the literature.