Kinetics of water sorption on a CaCl2-in-silica-gel-pores sorbent:: The effects of the pellet size and temperature

被引:10
作者
Aristov, Yu. I. [1 ]
Glaznev, I. S.
Freni, A.
Restuccia, G.
机构
[1] Russian Acad Sci, Boreskov Inst Catalysis, Siberian Branch, Novosibirsk 630090, Russia
[2] CNR, Inst Tecnol Avanzate Energia Nicola Giordano, Messina, Italy
基金
俄罗斯基础研究基金会;
关键词
D O I
10.1134/S002315840605017X
中图分类号
O64 [物理化学(理论化学)、化学物理学];
学科分类号
070304 ; 081704 ;
摘要
Kinetics of water vapor sorption on the CaCl2-in-KSK-pores composite (SWS-1L) have been studied at T = 33-69 degrees C and vapor pressures of 8-70 mbar for pellet sizes of 2R(pel) = 0.355-0.425, 0.71-0.85, and 1.2-1.4 mm. Sorption has been measured under isothermal conditions on a thermobalance by abruptly raising the vapor pressure in the measurement cell by a small value and then maintaining the new pressure. In the initial portion of the kinetic curves, the amount of sorbed water (Delta m) increases in proportion to the sorption time (t) to the power 1/2. From the slope of the Delta m versus t(1/2) curve, it is possible to derive the sorption rate constant k(D) = D-eff/R-pel(2) and the effective diffusivity D-eff. The latter is independent of R-pel for 2R(pel) >= 0.71 mm. The rate of water sorption on smaller (0.355- to 0.425-mm) pellets grows less rapidly, apparently because of the effect of the heat of sorption. The effective diffusivity is determined by the local slope of the water vapor sorption isotherm for SWS-1L. Applying an appropriate correction enables one to calculate the effective diffusivity for water vapor in the sorbent pores, which appears to be D-e = (0.35 +/- 0.17) x 10(-6) m(2)/s. This value is approximately 10 times smaller than the Knudsen water diffusion coefficient calculated for a single cylindrical pore with a size equal to the average pore size of the composite. Two possible causes of this discrepancy are discussed, specifically, an increase in the pore tortuosity because of the presence of the salt and the interaction between water and the salt.
引用
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页码:770 / 775
页数:6
相关论文
共 13 条
[1]  
[Anonymous], 1992, DIFFUSION ZEOLITES O
[2]   Selective water sorbents for multiple applications .1. CaCl2 confined in mesopores of silica gel: Sorption properties [J].
Aristov, YI ;
Tokarev, M ;
Cacciola, G ;
Restuccia, G .
REACTION KINETICS AND CATALYSIS LETTERS, 1996, 59 (02) :325-333
[3]   A family of new working materials for solid sorption air conditioning systems [J].
Aristov, YI ;
Restuccia, G ;
Cacciola, G ;
Parmon, VN .
APPLIED THERMAL ENGINEERING, 2002, 22 (02) :191-204
[4]  
Crank J., 1956, The Mathematics of Diffusion
[5]   Experimental study on the kinetics of water vapor sorption on selective water sorbents, silica gel and alumina under typical operating conditions of sorption heat pumps [J].
Dawoud, B ;
Aristov, Y .
INTERNATIONAL JOURNAL OF HEAT AND MASS TRANSFER, 2003, 46 (02) :273-281
[6]  
DAWOUD B, 2003, P 5 MINSK INT SEM HE, P306
[7]  
DEBOUR JH, 1953, DYNAMIC NATURE ADSOR
[8]  
KAERGER J, 1975, CHEM ENG SCI, V30, P893
[9]   ANALYSIS OF THERMAL EFFECTS IN ADSORPTION RATE MEASUREMENTS [J].
LEE, LK ;
RUTHVEN, DM .
JOURNAL OF THE CHEMICAL SOCIETY-FARADAY TRANSACTIONS I, 1979, 75 :2406-2422
[10]   Selective water sorbent for solid sorption chiller: experimental results and modelling [J].
Restuccia, G ;
Freni, A ;
Vasta, S ;
Aristov, Y .
INTERNATIONAL JOURNAL OF REFRIGERATION-REVUE INTERNATIONALE DU FROID, 2004, 27 (03) :284-293