首页> 外文会议>7th Biennial Conference on Engineering Systems Design and Analysis 2004(ESDA 2004) vol.1: Advanced Energy Systems; Advanced Heat Transfer in Engineering Systems; ... >EFFECT OF FLOW MALDISTRIBUTION AND VISCOSITY VARIATIONS ON TRANSIENT RESPONSE OF PLATE HEAT EXCHANGERS - A COMPARISON WITH UNIFORM FLOW AND CONSTANT VISCOSITY MODEL
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EFFECT OF FLOW MALDISTRIBUTION AND VISCOSITY VARIATIONS ON TRANSIENT RESPONSE OF PLATE HEAT EXCHANGERS - A COMPARISON WITH UNIFORM FLOW AND CONSTANT VISCOSITY MODEL

机译:流量分布不均和粘度变化对板式换热器瞬态响应的影响-均匀流和恒定粘度模型的比较

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In this paper, transient response of plate heat exchangers under flow maldistribution and viscosity variations is discussed. This transient response is compared with the response achieved from uniform flow and constant viscosity through the exchanger. Flow maldistribution (unequal flow in channels) is calculated for U and Z types of plate heat exchangers. This flow maldistribution along with viscosity variations, during the growth of the temperature profile in each channel, affect the convective heat transfer coefficient in the transient period of heat transfer, and make it to be different from that of the other channels. These conditions make the transient response of a plate heat exchanger to have some deviations from the uniform flow and constant viscosity model response, which is discussed in this paper. The governing equations of heat transfer are solved using finite difference methods. Frequency response as well as step response of the heat exchanger is implemented as a time dependent initial conditions.
机译:本文讨论了板式换热器在流量分布不均和粘度变化下的瞬态响应。将该瞬态响应与通过交换器的均匀流动和恒定粘度获得的响应进行比较。对于U型和Z型板式换热器,计算流量分配不均(通道中的流量不相等)。在每个通道中温度分布的增长过程中,这种流量分布不均以及粘度变化会影响热传递瞬态期间的对流传热系数,并使其不同于其他通道。这些条件使板式换热器的瞬态响应与均匀流动和恒定粘度模型响应有一些偏差,本文将对此进行讨论。传热控制方程采用有限差分法求解。热交换器的频率响应和阶跃响应被实现为与时间有关的初始条件。

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