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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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Capillary-Tube Model and Experiment of Multiphase Flow in Capillary Fringes
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作者 武晓峰 唐杰 吕贤弼 《Tsinghua Science and Technology》 SCIE EI CAS 2002年第6期584-590,共7页
Contamination of soil and groundwater by organic substances is causing more and more problems worldwide. Analysis of the movement and distribution of nonaqueous phase liquids (NAPLs) in subsurface domain is critical ... Contamination of soil and groundwater by organic substances is causing more and more problems worldwide. Analysis of the movement and distribution of nonaqueous phase liquids (NAPLs) in subsurface domain is critical for contaminant remediation. Two-dimensional experiments were conducted in a transparent plexiglass trough (105.0 KGcm×70.0 cm×1.5 cm) to simulate the release and redistribution of gasoline and kerosene in porous media. The results show that before the contaminant distribution reaches equilibrium, the movement of light NAPLs (LNAPLs) can be divided into four sub-stages. After the contaminant front reaches the upper boundary of the capillary fringe, contaminant movement along the upper boundary of the capillary fringe is the primary transport process. Most of the contaminants then move into the capillary fringe except for the residual part. One-dimensional and two-dimensional capillary tube models were developed to analyze the movement of LNAPLs in the capillary fringe. 展开更多
关键词 capillary-tube multiphase flow nonaqueous phase liquid (NAPL) light nonaqueous phase liquid (LNAPL)
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