Simulation of Single-stage Silica Gel-Water Adsorption Refrigeration Cycle with Vapor Recovery Process

2003 ◽  
Vol 2003.13 (0) ◽  
pp. 306-309
Author(s):  
Akira AKAHIRA ◽  
K. C. Amanul Alam ◽  
Atsushi AKISAWA ◽  
Takao KASHIWAGI
2002 ◽  
Vol 2002.12 (0) ◽  
pp. 533-536
Author(s):  
Akira AKAHIRA ◽  
K. C. Amanul Alam ◽  
Yoshinori HAMAMOTO ◽  
Atsushi AKISAWA ◽  
Takao KASHIWAGI

2002 ◽  
Vol 124 (3) ◽  
pp. 283-290 ◽  
Author(s):  
T. F. Qu ◽  
W. Wang ◽  
R. Z. Wang

Mass recovery can play an important role to better the performance of adsorption refrigeration cycles. Cooling capacity can be significantly increased with mass recovery process. The coefficient of performance (COP) of the activated carbon/ammonia adsorption refrigeration cycle might be increased or decreased with mass recovery process due to different working conditions. The advantage is that its COP is not sensitive to the variation of heat capacity of adsorber metal and condensing and evaporating temperature. The cycle with mass and heat recovery has a relatively high COP.


2014 ◽  
Vol 30 ◽  
pp. 85-104 ◽  
Author(s):  
Dechang Wang ◽  
Jipeng Zhang ◽  
Xiaoliang Tian ◽  
Dawei Liu ◽  
K. Sumathy

2000 ◽  
Author(s):  
B. B. Saha ◽  
K. C. A. Alam ◽  
A. Akisawa ◽  
T. Kashiwagi ◽  
K. C. Ng ◽  
...  

Abstract Over the past two decades there have been considerable efforts to use adsorption (solid/vapor) for cooling and heat pump applications, but intensified efforts were initiated only since the imposition of international restrictions on the production and use of CFCs (chlorofluorocarbons) and HCFCs (hydrochlorofluorocarbons). Closed-type, conventional adsorption refrigeration and heat pump systems have an increasing market share in Japan. In this paper, a two-stage non-regenerative, silica gel-water adsorption chiller design is outlined. Experimental measurements are performed on a prototype of a 3.5 kW rated cooling capacity adsorption heat pump in order to determine its performance under different operating temperatures (hot, cooling and chilled water). The chiller performance is analyzed in terms of cooling capacity and coefficient of performance (COP). The main innovative feature in the two-stage adsorption chiller is the ability to utilize low-temperature waste heat (∼55°C) as the driving source with a cooling source of 30°C. The technological difficulty inherent in operating a thermally activated cycle with such a small regenerating temperature lift (temperature difference between heat source and heat sink inlets) is overcome by use of a two-stage cycle.


Energies ◽  
2010 ◽  
Vol 3 (11) ◽  
pp. 1704-1720 ◽  
Author(s):  
Marlinda ◽  
Aep Saepul Uyun ◽  
Takahiko Miyazaki ◽  
Yuki Ueda ◽  
Atsushi Akisawa

2022 ◽  
Vol 2160 (1) ◽  
pp. 012032
Author(s):  
Hongxuan Li ◽  
Tonghua Zou ◽  
Qingling Hui ◽  
Ting Li ◽  
Walter Mittelbach

Abstract In recent years, adsorption refrigeration technology has attracted wide attention from experts and scholars at home and abroad due to its environmental friendliness and energy saving advantages. In order to study the effectiveness of adsorption refrigeration technology to recover low-grade energy, a silica gel-water adsorption refrigeration system was proposed, which can effectively utilize low-grade energy such as industrial waste heat. The structure and composition of the system are introduced. The operation performance of the unit is tested under different working conditions by orthogonal experimental method, and the experimental results are analyzed. The effects of hot water temperature and flow, chilled water temperature and flow on the refrigeration capacity and COP value of the system are obtained. The experimental results show that under the low-temperature heat source of 55-75°C, the cooling capacity of the system can reach 5.3-12 and the COP value can reach 0.36-0.56. Under the same hot water temperature difference, the cooling capacity and COP value of the system increase rapidly under the condition of changing the hot water temperature at low temperature, indicating that increasing the heat source temperature at low temperature has a greater impact on the system performance. Through the analysis of primary and secondary effects, it is concluded that the inlet temperature of hot water is the main factor affecting the refrigeration capacity and COP value of the system.


Energy ◽  
1997 ◽  
Vol 22 (4) ◽  
pp. 437-447 ◽  
Author(s):  
Bidyut B. Saha ◽  
Atsushi Akisawa ◽  
Takao Kashiwagi

2014 ◽  
Vol 113 ◽  
pp. 734-741 ◽  
Author(s):  
Dechang Wang ◽  
Jipeng Zhang ◽  
Qirong Yang ◽  
Na Li ◽  
K. Sumathy

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