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螺旋折流板换热器壳程传热和压降的实验研究 被引量:1
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作者 曹日 钱才富 +4 位作者 孙海阳 张智 赵福臣 杨开源 王凤君 《北京化工大学学报(自然科学版)》 CAS CSCD 北大核心 2011年第5期111-115,共5页
实验研究了螺旋折流板换热器的传热性能和壳程压力降,并与传统的弓形折流板换热器进行比较。结果发现如果螺旋折流板螺旋角过小(小于15°),螺旋折流板换热器壳程压力降可能会超过普通弓形折流板换热器;螺旋角增大(大于15°),螺... 实验研究了螺旋折流板换热器的传热性能和壳程压力降,并与传统的弓形折流板换热器进行比较。结果发现如果螺旋折流板螺旋角过小(小于15°),螺旋折流板换热器壳程压力降可能会超过普通弓形折流板换热器;螺旋角增大(大于15°),螺旋折流板换热器壳程传热系数会下降。综合考虑螺旋折流板换热器的壳程压力降和壳程传热系数,螺旋折流板螺旋角不能过大,也不能过小,所以在工程设计中,螺旋角一般应取在6°~12°之间。 展开更多
关键词 螺旋折流板 换热器性能实验 压力降 传热系数
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The Effects of Voltage and Suction Line Heat Exchanger on a Domestic Refrigerator's Performance
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作者 Xerri Stefan Farrugia Mario 《Journal of Energy and Power Engineering》 2016年第10期606-614,共9页
This experimental analysis shows the measured reduction in energy consumption as well as the effects of voltage on cycle temperatures, pressures, flow rates and also compressor speed (revolutions per minute). The do... This experimental analysis shows the measured reduction in energy consumption as well as the effects of voltage on cycle temperatures, pressures, flow rates and also compressor speed (revolutions per minute). The domestic refrigerator used R134a as refrigerant. Two energy consumption procedures were adapted from the JIS and ISO standards. The biggest difference between two standards is that the fridge is not opened in the ISO test while it is opened a number of times in the JIS test. The tests were carried out between 190 V and 250 V in steps of 10 V. The reduction in energy consumption was of 49.78 W-h per day or 6.27% of the total consumption. The experiments also showed that the voltage drop resulted in only a small rpm drop which in turn did not result in a noticeable refrigerant flow-rate change. Consequently the temperatures and pressures were not affected. 展开更多
关键词 REFRIGERATION voltage optimization energy consumption capillary-tube/suction-line heat exchanger.
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Performance of an R410a Filled Loop Heat Pipe Heat Exchanger
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作者 K.S. Ong 《Journal of Energy and Power Engineering》 2011年第1期1-9,共9页
A simple theoretical model of a heat pipe heat exchanger (HPHE) based on the ε-NTU method is presented. An iterative computer program was developed to predict the overall effectiveness of a counter-flow air-air loo... A simple theoretical model of a heat pipe heat exchanger (HPHE) based on the ε-NTU method is presented. An iterative computer program was developed to predict the overall effectiveness of a counter-flow air-air loop heat pipe heat exchanger (LHPHE). A thermal resistance network approach for a single thermosyphon was first considered to determine the overall heat transfer coefficients and the NTU's for the evaporator and condenser sections. The model incorporated previously determined evaporating and condensing coefficients. The overall effectiveness of the 6, 4 and 2 row LHPHE was then predicted. The theoretical overall effectiveness was compared with experimental data obtained from a R410a filled LHPHE. The experimental overall effectiveness results compared very well with the simulated values, The results showed that the 6 row arrangement performed better than the 4 or 2 row arrangement in the experiment. 展开更多
关键词 Loop heat pipe heat exchanger R410A multiple rows effectiveness-NTU model overall effectiveness.
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