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The principle and characteristic of continuous multistage fractional crystallization process are introduced.
介绍了连续多级逆流分步结晶过程的原理和特点。
The results show that the PTA crystallization kinetics parameters using optimization and regression can be utilized preferably to the modeling of purified terephthalic acid multistage crystallizer.
研究结果表明，优化回归得到的精对苯二甲酸结晶动力学方程能够较好地模拟PTA连续多级降压蒸发结晶过程。
The obtained data can be used in the simulation of the multistage decompression evaporation crystallization process.
所得数据可以用于粗对苯二甲酸多级降压蒸发结晶过程的模拟。
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