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The Simulation of Multicomponent Mixtures Condensation in Plate Condensers

机译:板式冷凝器中多组分混合物冷凝的模拟

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摘要

The application of plate heat exchangers for the condensation of multicomponent mixtures requires reliable, well-grounded methods of calculation, A numerical simulation using semi-empirical equations of heat and mass transfer performance along the surface of plate condensers was carried out for different multicomponent mixtures with noncondensable components. The plates with cross-corrugated patterns for plate condensers were used. The simulation was done for four different types of corrugated plates of industrially manufactured plate heat exchangers. The results of the simulation are in a good accordance with experimental data obtained during long-time experiments for a pilot plant at the pharmaceutical factory in Kharkiv. It is shown that the enhancement of heat and mass transfer in a plate condenser for the case of a four-component mixture gives the possibility of decreasing by 1.8-2 times the necessary heat transfer surface area comparatively with shell-and-tube unit for the same process parameters.
机译:板式换热器用于多组分混合物冷凝的应用需要可靠的,可靠的计算方法。针对不同的多组分混合物,使用沿板式冷凝器表面传热和传质性能的半经验方程式进行了数值模拟。不可凝结的成分。使用具有用于板式冷凝器的交叉波纹图案的板。对工业制造的板式热交换器的四种不同类型的波纹板进行了仿真。模拟的结果与哈尔科夫制药厂中试工厂的长期实验获得的实验数据非常吻合。结果表明,对于四组分混合物,平板式冷凝器中传热和传质的增强使得与管壳式换热器相比,所需的传热表面积减少了1.8-2倍。相同的工艺参数。

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