Heat and Mass Transfer Intensification in Solid Sorption Systems

1998 ◽  
Vol 5 (2) ◽  
pp. 111-125 ◽  
Author(s):  
L. E. Kanonchik ◽  
Leonid L. Vasiliev, Jr. ◽  
Valery A. Babenko
Atomic Energy ◽  
2018 ◽  
Vol 123 (3) ◽  
pp. 154-158 ◽  
Author(s):  
N. D. Agafonova ◽  
M. Yu. Egorov ◽  
V. V. Sergeev ◽  
M. A. Gotovskii ◽  
P. A. Kruglikov ◽  
...  

2012 ◽  
Vol 20 (01) ◽  
pp. 1130001 ◽  
Author(s):  
J. K. KIPLAGAT ◽  
R. Z. WANG ◽  
T. X. LI ◽  
R. G. OLIVEIRA

Solid gas sorption systems driven by heat have gained much attention due to their energy conservation and environmental benefits. These sorption machines can be driven by waste heat or renewable energy source such as solar energy, and can utilize natural working fluids with no GWP and ODP, such as water, methanol, and ammonia. However, poor heat transfer process and slow diffusion rate of the refrigeration gas in the adsorber have been identified as the main drawbacks limiting the cooling density performance, and consequently, commercialization of sorption machines. This paper provides a review of techniques that have been applied to enhance heat and mass transfer in solid gas sorption systems. These techniques mainly include the use of materials with high thermal conductivity, consolidation of adsorbents, and the use of specially designed heat exchangers in the adsorbers. The effect of these methods on the coefficient of performance and the specific cooling power is also discussed.


Author(s):  
R. Z. Wang ◽  
Z. Z. Xia ◽  
L. W. Wang ◽  
Z. S. Lu ◽  
S. L. Li ◽  
...  

Adsorption refrigeration and heat pump systems have been considered as very important means for the efficient use of low grade thermal energy in the temperature range of 60–150°C. Sorption systems are merely heat exchanger based thermodynamic systems, and therefore a good design to optimize heat and mass transfer with reaction or sorption processes is very important for high performance of the systems. Studies on heat and mass transfer enhancement in adsorption beds have been done extensively. Notable techniques is whereby the adsorbent bed is fitted with finned heat exchanger embedded with adsorbent particles, or the adsorbent particles may be compressed and solidified and then coupled with finned tube or plate heat exchangers. The use of expanded graphite seems to be an effective method to improve both heat and mass transfer in the reaction bed. Studies have also shows the need to enhance the heat transfer in adsorption bed to match with the heat transfer of thermal fluids. Use of heat pipes and good thermal loop design could yield higher thermal performances of a sorption system, when coupled with adsorption beds to provide heating and cooling to the beds. A novel design with passive evaporation, known as rising film evaporation coupled with a gravity heat pipe was introduced for high cooling output. It has also been shown that heat and mass recovery in the internal sorption systems is critical, and novel arrangement of thermal fluid and refrigerant may result in high performance sorption systems. Based upon the above researches, various sorption systems have been developed, and high efficient performances have been reached. Typical sorption systems include (1) A silica gel-water adsorption water chillier with a COP about 0.55 when powered with 80°C hot water, (2) A CaCl2-ammonia adsorption refrigerator with a COP over 0.3 at −20 °C when powered with 120 °C water vapor, which has a specific cooling power about 600 W/kg-adsorbent. The above mentioned systems have shown that solid sorption systems have become market potential products, and low grade thermal energy, which is usually considered as waste heat, could be utilized to provide high grade cooling. This paper gives details of high efficient solid sorption systems recently developed, their heat transfer design, thermodynamic system coupling, and performance test results. Some examples of low grade thermal powered cooling systems are also presented.


2008 ◽  
Vol 51 (21-22) ◽  
pp. 5175-5181 ◽  
Author(s):  
V.E. Nakoryakov ◽  
N.I. Grigoryeva ◽  
N.S. Bufetov ◽  
R.A. Dekhtyar

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