The effect of cycle boundary conditions and adsorbent grain size on the water sorption dynamics in adsorption chillers

被引:75
作者
Glaznev, I. S. [1 ]
Aristov, Yu I. [1 ]
机构
[1] Boreskov Inst Catalysis, Novosibirsk 630090, Russia
关键词
Heat and mass transfer; Adsorption kinetics; Adsorbent; Transport processes; Adsorption chillers; Large temperature jump method; REAL OPERATING-CONDITIONS; MASS-TRANSFER; HEAT-PUMPS; REFRIGERATION CYCLE; ISOBARIC STAGES; COOLING OUTPUT; SYSTEMS; KINETICS; SORPTION/DESORPTION; TRANSFORMERS;
D O I
10.1016/j.ijheatmasstransfer.2009.12.069
中图分类号
O414.1 [热力学];
学科分类号
摘要
The ann of this work was an experimental study of the temporal evolution of isobaric adsorption uptake (release) for simplest configuration of an adsorbent-heat exchanger unit, namely. a monolayer of loose adsorbent grains located on a metal plate. The study was performed by a large temperature jump method at four various boundary conditions of an adsorptive heat transformation cycle typical for air-conditioning application driven by low temperature heat: T-c = 5 and 10 degrees C, T-c = 30 and 35 degrees C and T-HS = 80 degrees C. The size of the Fuji silica grains was varied from 0.2 to 1.8 mm to investigate its effect on water sorption dynamics. For each boundary set and grain size the experimental kinetic curve could be described by an exponential function up to 80-90% of the equilibrium conversion. Desorption runs are found to be faster than appropriate adsorption runs by a factor of 2.2-35, hence, for optimal durations of the isobaric ad- and desorption phases of the chilling cycle should be selected accordingly. The size R of the adsorbent grains was found to be a powerful tool to manage the dynamics of isobaric water ad-/desorption. For large grains the characteristic time was strongly dependent oil the grain size and proportional to R-2. Much less important appeared to be an impact of the boundary conditions which variation just weakly affected the dimensionless kinetic curves for the four tested cycles. The maximal specific cooling/heating power was proportional to the maximal temperature difference Delta T and the contact area S between the layer and the metal plate. and can exceed 10 kW/kg. The heat transfer coefficient alpha estimated from this power was as large as 100-250 W/(m(2) K) that much exceeds the value commonly used to describe the cycle dynamics. (C) 2010 Elsevier Ltd. All rights reserved.
引用
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页码:1893 / 1898
页数:6
相关论文
共 26 条
[1]  
[Anonymous], ENERGY CONSERV
[2]  
ARISTOV YI, INT J REFRIG UNPUB
[3]   A new methodology of studying the dynamics of water sorption/desorption under real operating conditions of adsorption heat pumps: Experiment [J].
Aristov, Yu. I. ;
Dawoud, B. ;
Glaznev, I. S. ;
Elyas, A. .
INTERNATIONAL JOURNAL OF HEAT AND MASS TRANSFER, 2008, 51 (19-20) :4966-4972
[4]   Kinetics of water adsorption on silica Fuji Davison RD [J].
Aristov, Yuri I. ;
Tokarev, Mikhail M. ;
Freni, Angelo ;
Glaznev, Ivan S. ;
Restuccia, Giovanni .
MICROPOROUS AND MESOPOROUS MATERIALS, 2006, 96 (1-3) :65-71
[5]   Optimal adsorbent for adsorptive heat transformers: Dynamic considerations [J].
Aristov, Yuriy I. .
INTERNATIONAL JOURNAL OF REFRIGERATION-REVUE INTERNATIONALE DU FROID, 2009, 32 (04) :675-686
[6]  
Boelman EC, 1995, ASHRAE TRAN, V101, P358
[7]   Transient modeling of a two-bed silica gel-water adsorption chiller [J].
Chua, HT ;
Ng, KC ;
Wang, W ;
Yap, C ;
Wang, XL .
INTERNATIONAL JOURNAL OF HEAT AND MASS TRANSFER, 2004, 47 (04) :659-669
[8]   Adsorption characteristics of silica gel plus water systems [J].
Chua, HT ;
Ng, KC ;
Chakraborty, A ;
Oo, NM ;
Othman, MA .
JOURNAL OF CHEMICAL AND ENGINEERING DATA, 2002, 47 (05) :1177-1181
[9]  
Crank J., 1979, MATH DIFFUSION, V2nd
[10]   Kinetics of water adsorption/desorption under isobaric stages of adsorption heat transformers: The effect of isobar shape [J].
Glaznev, I. S. ;
Ovoshchnikov, D. S. ;
Aristov, Yu. I. .
INTERNATIONAL JOURNAL OF HEAT AND MASS TRANSFER, 2009, 52 (7-8) :1774-1777