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A novel model for evaporator structural design in the multi-effect evaporation plant

机译:多效蒸发厂蒸发器结构设计的一种新型模型

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摘要

In this paper, a novel model called Evaporator Structural Design (ESD) model is introduced. The model not only predicts the three-dimensional distribution of heat transfer coefficient under different operation conditions but also guides the evaporator structural design. The results show that the heat transfer coefficient decreases with the decline of the spray density from 0.08 to 0.015 and with the increase of the tube length from 2 m to 10 m. The heat transfer coefficient exhibits higher values for the evaporation zone than the preheating zone, almost twice or more. Either in the preheating zone or in the evaporation zone, the heat transfer coefficient in different row positions have small differences. A forward-feed MEE (multi-effect evaporation) plant with 14 effects is calculated using the ESD model. Compared with the experimental data, the relative error of the accumulated vapor mass flow rate in each effect ranged between 1% and 8%, that of the evaporator area is about 7%. The ESD model is accurate and convenient in engineering design.
机译:本文介绍了一种名为蒸发器结构设计(ESD)模型的新型模型。该模型不仅预测了在不同操作条件下的传热系数的三维分布,而且引导蒸发器结构设计。结果表明,热传递系数随着喷射密度的下降0.08至0.015,管长度从2米到10μm的增加,输热系数随着0.08至0.015的增加而降低。传热系数对蒸发区具有比预热区更高的值,几乎是两倍以上。在预热区或蒸发区中,不同行位置的传热系数具有很小的差异。使用ESD模型计算具有14个效果的前饲料MEE(多效蒸发)植物。与实验数据相比,每种效果中累积蒸汽质量流速的相对误差范围为1%至8%,蒸发器面积的蒸发区为约7%。 ESD模型准确方便于工程设计。

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