Enhancing the Amount of Cold Produced and Saving of the Required Input Heat using Two Different Adsorbents together in the Adsorption Ice Production AIP System
Abstract - 78
PDF

Keywords

Adsorption refrigeration machine, adsorption ice production (AIP) system, different adsorbents activated carbon and silica gel, sorption reactor, thermal analysis.

How to Cite

1.
Majd Ali, Salman Ajib, Christian Karcher. Enhancing the Amount of Cold Produced and Saving of the Required Input Heat using Two Different Adsorbents together in the Adsorption Ice Production AIP System. Glob. J. Energ. Technol. Res. Updat. [Internet]. 2017 Jun. 21 [cited 2024 Jul. 26];4(1):9-25. Available from: https://avantipublishers.com/index.php/gjetru/article/view/776

Abstract

 A theoretical investigation of the thermal performance (coefficient of performance COP and specific cooling power SCP) of a two bed Adsorption Ice Production AIP system based on the Silica gel-methanol as adsorbent-refrigerant in the first bed and activated carbon-methanol in the second bed is presented in this paper. Two fined-tube heat exchangers were designed (named SG-bed and AC-bed) in order to generate the same desorbed refrigerant amount of 1 kgmeth and to contain two different adsorbents. The mass transfer limitations from both the two beds and the heat transfer ability between the particles of adsorbents and heat exchanger fins are taken into account in the simulated model based on the linear driving force LDF model. To desorb 1 kgmeth from the SG-bed and AC-bed a cycle simulation computer program of the AIP system was developed to investigate the effect of desorption temperature Tdes, adsorption temperature Tads and the effect of difference of the required desorption/adsorption time on the system performance and on the amount of the ice produced per cycle mice. In the present simulations, the variation of the heat source temperature from 65 to 100 oC and chilled water temperature from 15 oC to 25 oC are taken. The results showed, that the AIP system attains a coefficient of performance COP of 66 % when the AC-bed is working and attains of 44 % when the SG-bed is working. The amount of the ice produced from the system estimated to 6kg per cycle (3 kg is produced from each of bed), but the Qin input energy required to activate the AC-bed has been saved by 46 % compared with that required to activate the SG-bed. Although each of the adsorbent beds was filled with different amount of the sorption material, it is found that the mass of the sorption materials inside the both beds has no effect on the cycle time but has important effect on the specific cooling power SCP. The cycle time is strongly dependent on driven temperature of heat exchange fluid, the design of the heat exchanger and the mass transfer coefficient of sorption material Dso. An experimental set up is planned to be built to make validation of the simulation results.
https://doi.org/10.15377/2409-5818.2017.04.01.2
PDF

References

Fernandes MS, Brites GJVN, Costa JJ, Gaspar AR and Costa VAF. Review and future trends of solar adsorption refrigeration systems. Renew Sust Energy Rev 2014; 39: 102-123. https://doi.org/10.1016/j.rser.2014.07.081

Douss N and Meunier F. Experimental study of cascading adsorption cycles. Chem Eng Sci 1989; 44 (2): 225-235. https://doi.org/10.1016/0009-2509(89)85060-2

Chua HT, Ng KC, Malek A, Kashiwagi T, Akisawa A, Saha BB. Modeling the performance of two-bed silica Gel-water adsorption chillers. Int J Refrig 1999; 22: 194-204. https://doi.org/10.1016/S0140-7007(98)00063-2

Gregg SJ, Sing KSW. Adsorption, surface area and porosity. 2nd ed. Academic press, London 1982.

Rezk ARM. Theoretical and experimental investigation of silica gel-water adsorption. 2012. A thesis submitted of the university of Birmingham for the degree of Doctor of Philosophy.

Amir S, Majid B. Assessment of adsorber bed designs in waste-heat driven adsorption cooling system for vehicle air conditioning and refrigeration. Renew Sust Energy Rev 2014; 30: 440-451. https://doi.org/10.1016/j.rser.2013.10.031

Gong LX, Wang RZ, Xia ZZ, Lu ZS. Experimental study on an adsorption chiller employing lithium chloride in silica gel and methanol. Int J Refrig 2012; 35: 1950-1957. https://doi.org/10.1016/j.ijrefrig.2012.06.013

Wang RZ, Oliveira RG. Adsorption refrigeration an efficient way to make good use of waste heat and solar energy. International sorption heat pump conference, June 22-24, 2005; Denver, Co, USA.

Solmus I, Yamali C, Kaftanoglu B, Baker D, Caglar A. Adsorption properties of a nature zeolite-water pair for use in adsorption cooling cycles. Applied Energy 2010; 87: 2062- 2067. https://doi.org/10.1016/j.apenergy.2009.11.027

Oertel K, Fischer M. Adsorption cooling system for cold storage using methanol/silicagel. Appl Thermal Eng 1998; 18: 773-786. https://doi.org/10.1016/S1359-4311(97)00107-5

Ogueke NV, Anyanwu EE. The performance analysis of a solid adsorption solar refrigerator during collector cool-down and refrigerant evaporation/re-adsorption phases. J Proc Mech Eng 2009; 223 (1): 11-19. https://doi.org/10.1243/09544089JPME217

Khan MZI, Sultan S, Akisawa A, Kashiwagi T. Numerical simulation of advanced adsorption refrigeration chiller with mass recovery. J Navel Arch Marine Eng 2006; 3: 59-67.

Cho SH, Kim JN. Modeling of a silica gel/water adsorption cooling system. Energy 1992; 17 (9): 829-839. https://doi.org/10.1016/0360-5442(92)90101-5

Qasem NAA, El-Shaarawi MAI. Thermal analysis and modeling study of an activated carbon solar adsorption icemaker: Dhahran case study. Energy Conversion and Management 2015; 100: 310-323. https://doi.org/10.1016/j.enconman.2015.04.054

Liu Y, Leong KC. The effect of operating conditions on the performance of zeolite/water adsorption cooling systems. Appl Thermal Eng 2005; 25: 1403-1418. https://doi.org/10.1016/j.applthermaleng.2004.09.013

Hassan HZ. Energy analysis and performance evaluation of the adsorption refrigeration system. ISRN Mechanical Engineering, Article ID 704340 (2013) 1-14.

Jribi S, Miyazaki T, Saha BB. Koyama S. Transient simulation of finned tube type adsorber employing activated carbonethanol as adsorbent refrigerant pair. ICR 2015, August 16 - 22 - Yokohama, Japan.

Goodwin RD. Methanol Thermodynamic Properties from 176 to 673 K at pressures to 700 bar. Thermophysics Division, National Engineering Laboratory, National Bureau of Standards, Colorado 80303 (1987).

Li M, Wang RZ. Heat and mass transfer in a flat plate solar solid adsorption refrigeration ice maker. Renewable Energy 2003; 28: 613-622. https://doi.org/10.1016/S0960-1481(02)00094-0

Gong LX, Wang RZ, Xia ZZ, Lu ZS. Experimental study on an adsorption chiller employing lithium chloride in silica gel and methanol. Int J Refrig 2012; 35: 1950-1957. https://doi.org/10.1016/j.ijrefrig.2012.06.013

El-Sharkawy II. Study on adsorption of methanol onto carbon based adsorbents. Int J Refrig 2009; 32: 1579-1586. https://doi.org/10.1016/j.ijrefrig.2009.06.011

Ng KC, Chua HT, Chung CY, Loke CH, Kashiwagi T, Akisawa A, Saha BB. Experimental investigation of the silica gel-water adsorption isotherm characteristics. Appl Thermal Eng 2001; 21: 1631-1642. https://doi.org/10.1016/S1359-4311(01)00039-4

Hasan HZ, Mohamad AA, Alyousef Y and Al-Ansary HA. A review on the equation of state for the working pairs used in adsorption cooling systems. Renew Sust Energy Rev 2015; 45: 600-608. https://doi.org/10.1016/j.rser.2015.02.008

Wang LW, Wang RZ and Oliveira RG. A review on adsorption working pairs for refrigeration. Renew Sust Energy Rev 2009; 13 (3): 518-534. https://doi.org/10.1016/j.rser.2007.12.002

Srivastava NC and Eames IW. A review of adsorbents and adsorbates in solid-vapour adsorption heat pump systems. Appl Thermal Eng 1998; 18: 707-714. https://doi.org/10.1016/S1359-4311(97)00106-3

Ali M and Ajib S. Energy analysis and modeling study of combined activated carbon-silica gel/methanol adsorption ice production system. Glob J Energ Technol Res Updat 2016; 3; 1-22. https://doi.org/10.15377/2409-5818.2016.03.01.1

All the published articles are licensed under the terms of the Creative Commons Attribution Non-Commercial License (CC BY-NC 4.0) which permits unrestricted, non-commercial use, distribution and reproduction in any medium, provided the work is properly cited.