k-ε湍流模型下静电除尘器强化饱和多孔试样的传热

Q3 Engineering
Suwimon Saneewong Na Ayuttaya
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引用次数: 1

摘要

在k-ε湍流模型中,数值研究了静电除尘器过程对饱和多孔样品强化传热的影响。水进入试验段的条件是入口温度为30℃(303 K),入口速度为1 ~ 2.5 m/s。电压和时间分别在0 ~ 30kv和0 ~ 1s之间变化。饱和多孔样品初始温度为10℃(283 K),第一、第二样品均设置为半圆形。数值结果表明,在采用静电除尘器过程中,水渠内的电场和电势区出现并集中。高电压会增加水道内的扰动和湍流。最大流场区出现在饱和多孔样区上方,最大速度场随进口速度和电压的增大而增大。高压时最大压力增大,但高进口速度时压力略有增大。有电除尘器过程的涡度曲线比没有电除尘器过程的涡度曲线更集中。因此,在进口速度、电压和时间较大的情况下,温度轮廓线比其他情况更容易受到干扰。此外,水的热量在样品内部传递,因此多孔样品内部的温度逐渐升高。饱和前孔样品的流体流速大于后孔样品。因此,流体可以穿过样品并在样品内移动,并在两个饱和多孔样品内引起温度升高。最后,通道内的流体流动增强了样品内部的换热,因此通道内的流体流速诱导了样品内部的局部换热系数。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
Heat transfer enhancement on saturated porous samples using electrostatic precipitator process in k-ε turbulent model
An influence of the electrostatic precipitator process was numerically investigated for heat transfer enhancement on saturated porous samples in a k-ε turbulent model. The condition of the water entering a test section was the inlet temperature was 30 oC (303 K), and inlet velocity was tested in the range of 1 – 2.5 m/s. The electrical voltage and time varied between 0 – 30 kV and 0 – 1 s, respectively. The initial temperature of saturated porous samples was 10 oC (283 K), and both first and second samples were set in semicircle shapes. The numerical results within the water channel showed that the electric field and electric potential zone appeared and were concentrated when using the electrostatic precipitator process. The high electric voltage could increase disturbance and turbulence within the water channel. The maximum flow field zone appeared above the saturated porous sample area, and the maximum velocity field increased with the inlet velocity and electrical voltage. The maximum pressure was increased to the high voltages, but the pressure was marginally increased with high inlet velocity. The vorticity contour for an electrostatic precipitator process was more concentrated than without the electrostatic precipitator process. Therefore, the temperature contour line in case of high inlet velocity, electrical voltage, and time can be more disturbing than the other cases. In addition, heat from the water was transferred within the sample, so the temperature within the porous sample gradually increased. The fluid velocity within the front porous sample was more within the saturated porous samples than within the porous back sample. Therefore, the flow could move through and within the samples and induce temperature within both saturated porous samples. Finally, the heat transfer within samples was enhanced by fluid flow in the water channel, so the local heat transfer coefficient within samples was induced by the fluid velocity in the water channel.
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