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Steady-State Investigation of Carbon-Based Adsorbent–Adsorbate Pairs for Heat Transformation Application

Author

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  • Faizan Shabir

    (Department of Agricultural Engineering, Bahauddin Zakariya University, Multan 60800, Pakistan
    Department of Agricultural Engineering, Khwaja Fareed University of Engineering & Information Technology, Rahim Yar Khan 64200, Pakistan)

  • Muhammad Sultan

    (Department of Agricultural Engineering, Bahauddin Zakariya University, Multan 60800, Pakistan)

  • Yasir Niaz

    (Department of Agricultural Engineering, Khwaja Fareed University of Engineering & Information Technology, Rahim Yar Khan 64200, Pakistan)

  • Muhammad Usman

    (Institute for Water Resources and Water Supply, Hamburg University of Technology, Am Schwarzenberg-Campus 3, 20173 Hamburg, Germany)

  • Sobhy M. Ibrahim

    (Department of Biochemistry, College of Science, King Saud University, P.O. Box 2455, Riyadh 11451, Saudi Arabia)

  • Yongqiang Feng

    (School of Energy and Power Engineering, Jiangsu University, Zhenjiang 212013, China)

  • Bukke Kiran Naik

    (Department of Mechanical Engineering, National Institute of Technology Rourkela, Odisha 769008, India)

  • Abdul Nasir

    (Department of Structures and Environmental Engineering, University of Agriculture, Faisalabad 38000, Pakistan)

  • Imran Ali

    (Department of Environmental Science and Engineering, College of Chemistry and Environmental Engineering, Shenzhen University, Shenzhen 518060, China)

Abstract

In this study, the ideal adsorption cycle behavior of eight activated carbon and refrigerant pairs is evaluated. The selected pairs are KOH6-PR/ethanol, WPT-AC/ethanol, Maxsorb-III/methanol, Maxsorb-III/CO 2 , Maxsorb-III/n-butane, Maxsorb-III/R-134a, SAC-2/R32 and Maxsorb-III/R507a. The following cooling performance parameters are evaluated for all pairs: specific cooling energy (SCE), concentration difference (ΔW) and coefficient of performance (COP) of ideal adsorption cooling and refrigeration cycles. The evaporator temperatures for the applications of adsorption cooling and refrigeration are selected as 7 and −5 °C, respectively. It is found that the Maxsorb-III/methanol pair has shown the highest specific cooling energy and coefficient of performance in a wide range of desorption temperatures; i.e., for the adsorption cooling cycle it has SCE and COP of 639.83 kJ/kg and 0.803, respectively, with desorption temperatures of 80 °C. The KOH6-PR/ethanol and the WPT-AC/ethanol pairs also give good performances comparable to that of the Maxsorb-III/methanol pair. However, the SAC-2/R32 pair possesses a higher concentration difference than the Maxsorb-III/methanol, KOH6-PR/ethanol and WPT-AC/ethanol pairs but shows a lower performance. This is due to the lower isosteric heat of adsorption of SAC-2/R32 compared to these pairs. It is found that Maxsorb-III/methanol, KOH6-PR/ethanol and WPT-AC/ethanol are the most promising pairs for application in designing adsorption cooling and refrigeration systems.

Suggested Citation

  • Faizan Shabir & Muhammad Sultan & Yasir Niaz & Muhammad Usman & Sobhy M. Ibrahim & Yongqiang Feng & Bukke Kiran Naik & Abdul Nasir & Imran Ali, 2020. "Steady-State Investigation of Carbon-Based Adsorbent–Adsorbate Pairs for Heat Transformation Application," Sustainability, MDPI, vol. 12(17), pages 1-15, August.
    • Handle: RePEc:gam:jsusta:v:12:y:2020:i:17:p:7040-:d:405750
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    References listed on IDEAS

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    2. Asfahan, Hafiz M. & Sultan, Muhammad & Miyazaki, Takahiko & Saha, Bidyut B. & Askalany, Ahmed A. & Shahzad, Muhammad W. & Worek, William, 2022. "Recent development in adsorption desalination: A state of the art review," Applied Energy, Elsevier, vol. 328(C).

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