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ARTICLE IN PRESS R.Z. Wang, R.G. Oliveira / Progress in Energy and Combustion Science 32 (2006) 424–458 455 [73]. This prototype was designed to operate on fishing boats and uses split heat pipe technology to allow direct utilization of exhaust gases of diesel engines and seawater to, respectively, heat and cool the adsorbers. From the examples presented, it is possible to consider that adsorption systems can be an alter- native to reduce the CO2 emissions and the electricity demand when they are driven by waste heat or solar energy. Although, for a broader utilization, the researches should continue aiming for improvements in heat transfer, reductions of manufacturing costs, and for the formulation of new adsorbent compounds with enhanced adsorp- tion capacity and improved heat and mass transfer properties. Acknowledgements This work was supported by the National Science Fund for Distinguished Young Scholars of China under contract no. 50225621. It is also partly supported by the National Key Fundamental Research Program under contract no. G2000026309, the Teaching and Research Award Program for Outstanding Young Teachers in Higher Education Institutions of MOE, China, and the Shuguang Training Program of Shanghai Education Commission under contract no. 02GG03. The authors thank Elsevier for the kind permis- sion to use Figs. 2–7, 10, 12, 14, 16, 22–24 and 27, from the references 62, 63, 65, 68, 69, 71, 52, 76, 80, 82, 90, 90, 92 and 103, respectively. References [1] Critoph RE. Performance limitations of adsorption cycles for solar cooling. Sol Energy 1988;41(1):21–31. [2] Luo L, Feidt M. Thermodynamics of adsorption cycles: a theoretical study. Heat Transfer Eng 1992;13(4):19–31. [3] Teng Y, Wang RZ, Wu JY. Study of the fundamentals of adsorption systems. Appl Therm Eng 1997;17(4):327–38. [4] Huber U, Stoeckli F, Houriet JP. A generalization of the Dubinin–Radushkevich equation for the filing of hetero- geneous micropore systems in strongly activated carbons. J Colloid Interface Sci 1978;67(2):195–203. [5] Passos FP. Etude des couples charbon actif/methanol et de leur application a la refrigerations solaire [Ph.D.] Lau- sanne: Ecole Polytechnique Federale de Lausanne; 1986. 101p. [6] Guilleminot JJ, Choisier A, Chalfen JB, Nicolas S, Reymoney JL. Heat transfer intensification in fixed bed adsorbers. Heat Recov Syst CHP 1993;13(4):297–300. [7] Mauran S, Prades P, L‘Haridon F. Heat and mass transfer in consolidated reacting beds for thermochemical systems. Heat Recov Syst CHP 1993;13(4):315–9. [8] Critoph RE. Evaluation of alternative refrigerant-adsor- bent pairs for refrigeration cycles. Appl Therm Eng 1996;16(11):891–900. [9] Liu Z, Lu Y, Zhao J. Zeolite-active carbon compound adsorbent and its use in adsorption solar cooling tube. Sol Energy Mater Sol Cells 1998;52:45–53. [10] Guilleminot JJ. From pellet to composite adsorbent bed: evolutions of adsorber technologies. In: Proceedings of fundamentals of adsorption (FOA6), France, 1998. [11] Dellero T, Sarmeo D, Touzain Ph. A chemical heat pump using carbon fibes as additive. Part I: enhancement of thermal conduction. Appl Therm Eng 1999;19(9):991–1000. [12] Dellero T, Touzain Ph. A chemical heat pump using carbon fibes as additive. Part II: study of constraint parameters. Appl Therm Eng 1999;19(9):1001–11. [13] Eun TH, Song HK, Han JH, Lee KH, Kim JN. Enhancement of heat and mass transfer in silica-expanded graphite composite blocks for adsorption heat pumps: Part I. Characterization of the composite blocks. Int J Refrig 2000;23(1):64–73. [14] Han JH, Lee KH, Kim DH, Kim H. Transformation analysis of thermochemical reactor based on thermophysi- cal properties of graphite-MnCl2 complex. Ind Eng Chem Res 2000;39(11):4127–39. [15] Oliveira RG, TamainotTelto Z, Silveira Jr. V. Equilibrium characterisation of carbon C119-ammonia and carbon C119-dimethyl ether pairs and application in adsorption refrigeration design. In: Proceedings of the XVI Brazilian congress of mechanical engineering (COBEM 2001), Brazil, 2001. [16] TamainotTelto Z, Critoph RE. Monolithic carbon for sorption refrigeration and heat pump applications. Appl Therm Eng 2001;21(1):37–52. [17] Aidoun Z, Ternan M. Salt impregnated carbon fibres as the reactive medium in a chemical heat pump: the NH3–CoCl2 system. Appl Therm Eng 2002;22:1163–73. [18] Freni A, Tokarev MM, Restuccia G, Okunev AG, Aristov YI. Thermal conductivity of selective water sorbents under the working conditions of a sorption chiller. Appl Therm Eng 2002;22(14):1631–42. [19] Aidoun Z, Ternan M. The synthesis reaction in a chemical heat pump reactor filled with chloride salt impregnated carbon fibres: the NH3–CoCl2 system. Appl Therm Eng 2002;22:1943–54. [20] Li M, Huang HB, Wang RZ, Wang LL, Cai WD, Yang WM. Experimental study on adsorbent of activated carbon with refrigerant of methanol and ethanol for solar ice maker. Renew Energy 2004;29(15):2235–44. [21] Wang LW, Wang RZ, Wu JY, Wang K. Compound adsorbent for adsorption ice maker on fishing boats. Int J Refrig 2004;27:401–8. [22] Wang K, Wu JY, Wang RZ, Wang LW. Composite adsorbent of CaCl2 and expanded graphite for adsorp- tion ice maker on fishing boats. Int J Refrig 2006;29(2): 199–210. [23] Wang K, Wu JY, Wang RZ, Wang LW. Effective thermal conductivity of expanded graphite-CaCl2 composite ad- sorbent for chemical adsorption chillers. Energy Convers Manage 2006;47(13–14):1902–12.PDF Image | Adsorption refrigeration
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