INFLUENCE OF VAPOR AND CRYSTAL FORMATION PROCESSES ON HEAT EXCHANGE IN FILM VAPORATORS

O. Koshelnik, V. Pavlova, T. Pugacheva, O. Kruglyakova, O. Dolobovska
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Abstract

Evaporators for changing the concentration of solutions have a different design, depending on the type of processed substance. Significant energy consumption in such equipment is associated with the need for removing large quantity of liquid phase. Multiple-effect evaporators are used to reduce the energy consumption of the evaporation process, but such equipment is quite expensive. Evaporators with secondary vapor heat reusing that operate in film mode can be an alternative to multi-effect evaporators. This equipment can operate efficiently across minimal temperature differences due to secondary vapor compressors. The disadvantage of this device is strict requirements for impurities in solutions. Impurities create deposits (incrustations) of various substances on the heat transfer surfaces, which worsens the operating conditions. If crystallizing solutions are used in evaporators with reusing of secondary vapor heat, then one of the ways to reduce the rate of heating surfaces incrustation is to add a solid phase to the initial solution. A mathematical model is proposed to describe the processes of heat and mass transfer during the film flow of crystallizing solutions, which are accompanied by a change in the physical characteristics of the solution and the formation of deposits. The model considers a three-phase liquid suspension with a varying phase content. Two stages of vaporization including vaporization on the surface of the liquid and on the surface of heat exchange are presented. The mathematical model involves the equations of continuity, energy and heat transfer, as well as the equations of motion of a three-phase flow with a changing phase content for both stages of vaporization, taking into account that solid phase turbulizes the flow and intensifies the heat transfer process. This mathematical model makes it possible to study the effect of the solid phase on heat transfer processes and the rate of incrustation in evaporators with reuse of secondary vapor heat.
蒸汽和晶体形成过程对薄膜蒸发器热交换的影响
用于改变溶液浓度的蒸发器有不同的设计,这取决于所处理物质的类型。在这种设备中,显著的能源消耗与需要去除大量的液相有关。多效蒸发器用于降低蒸发过程的能耗,但这种设备相当昂贵。具有二次蒸汽热再利用的蒸发器在薄膜模式下运行,可以替代多效蒸发器。由于二级蒸汽压缩机,该设备可以在最小的温差下有效运行。该装置的缺点是对溶液中的杂质要求严格。杂质在传热表面上形成各种物质的沉积(结块),使操作条件恶化。如果在蒸发器中使用二次蒸汽热再利用的结晶溶液,那么减少受热面结垢率的方法之一是在初始溶液中加入固相。提出了一个数学模型来描述结晶溶液在膜流过程中的传热传质过程,该过程伴随着溶液物理特性的变化和沉积物的形成。该模型考虑具有不同相含量的三相液体悬浮液。提出了液体表面汽化和换热表面汽化两个汽化阶段。数学模型考虑到固相对流动的湍流作用和传热过程的加剧,包括连续方程、能量方程和传热方程,以及汽化两阶段相含量变化的三相流动的运动方程。该数学模型可以研究二次蒸汽热回用时,固相对传热过程的影响和蒸发器结垢率的影响。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
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