Making adsorptive chillers faster by a proper choice of adsorption isobar shape: Comparison of optimal and real adsorbents

This paper addresses the first quantitative evaluation of the effect of adsorbent isobar shape on the dynamics of AC (adsorptive chiller) cycle. The numerical and experimental studies of this effect have been performed to answer the question “Which practical enhancement of the AC specific cooling power may be expected when one would use an adsorbent with the optimal isobar shape instead of a real adsorbent typical for AC?”. The reference (real) adsorbent is SWS-1L (mesoporous silica gel modified by CaCl2) that was proven to be efficient in AC units driven by waste or renewable heat. The optimal adsorbent is found to provide shorter AC cycles as compared with the real one so that the SCP increases by a factor of 1.5 that is of certain practical importance. In a broader sense, this original approach can be further used to specify requirements for selecting known adsorbents as well as tailoring a new generation of adsorbents optimal for a variety of practically interesting AC cycles.

[1]  A. Freni,et al.  Reallocation of adsorption and desorption times for optimisation of cooling cycles , 2012 .

[2]  Biplab Choudhury,et al.  Study on a solar heat driven dual-mode adsorption chiller , 2013 .

[3]  Leonard L. Vasiliev,et al.  Heat pipes in modern heat exchangers , 2005 .

[4]  I. S. Glaznev,et al.  Kinetics of water adsorption/desorption under isobaric stages of adsorption heat transformers: The effect of isobar shape , 2009 .

[5]  J. S. Spevack,et al.  Heat Conversion Systems , 1993 .

[6]  Yuri I. Aristov,et al.  Adsorption chilling driven by low temperature heat: New adsorbent and cycle optimization , 2012 .

[7]  Yuri I. Aristov,et al.  Modelling of isobaric stages of adsorption cooling cycle: An optimal shape of adsorption isobar , 2013 .

[8]  Bidyut Baran Saha,et al.  Towards an optimal performance of adsorption chillers: Reallocation of adsorption/desorption cycle times , 2013 .

[9]  E. Proverbio,et al.  Zeolite coated copper foams for heat pumping applications , 2006 .

[10]  Yuri I. Aristov,et al.  A new methodology of studying the dynamics of water sorption/desorption under real operating conditions of adsorption heat pumps : Modelling of coupled heat and mass transfer in a single adsorbent grain , 2008 .

[11]  Y. Çengel,et al.  Thermodynamics : An Engineering Approach , 1989 .

[12]  Ruzhu Wang,et al.  A REVIEW OF THERMALLY ACTIVATED COOLING TECHNOLOGIES FOR COMBINED COOLING, HEATING AND POWER SYSTEMS , 2011 .

[13]  Yuri I. Aristov,et al.  Adsorptive transformation of heat: Principles of construction of adsorbents database , 2012 .

[14]  Yuri I. Aristov,et al.  Composites ‘salt inside porous matrix’ for adsorption heat transformation: a current state-of-the-art and new trends , 2012 .

[15]  Ruzhu Wang,et al.  Progress in the development of solid–gas sorption refrigeration thermodynamic cycle driven by low-grade thermal energy , 2014 .

[16]  Yuri I. Aristov,et al.  The effect of cycle boundary conditions and adsorbent grain size on the water sorption dynamics in adsorption chillers , 2010 .

[17]  Yuri I. Aristov,et al.  Synthesis and water sorption properties of a new composite “CaCl2 confined into SBA-15 pores” , 2010 .

[18]  Yuri I. Aristov,et al.  Dynamic study of adsorbers by a new gravimetric version of the Large Temperature Jump method , 2014 .

[19]  L. W. Wang,et al.  Sorption thermal storage for solar energy , 2013 .

[20]  Andrea Frazzica,et al.  Influence of the management strategy and operating conditions on the performance of an adsorption ch , 2011 .

[21]  R. E. Critoph Performance limitations of adsorption cycles for solar cooling , 1988 .

[22]  Yu. I. Aristov,et al.  Universal relation between the boundary temperatures of a basic cycle of sorption heat machines , 2008 .

[23]  Yuri I. Aristov Experimental and numerical study of adsorptive chiller dynamics: Loose grains configuration , 2013 .