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Economic and Technical Analysis of a Hybrid Dry Cooling Cycle to Replace Conventional Wet Cooling Towers for High Process Cooling Loads

Author

Listed:
  • Aqeel Ahmad Taimoor

    (Department of Chemical and Materials Engineering, King Abdulaziz University, P.O. Box, 80204, Jeddah 21589, Saudi Arabia)

  • Usman Saeed

    (Department of Chemical and Materials Engineering, King Abdulaziz University, P.O. Box, 80204, Jeddah 21589, Saudi Arabia)

  • Sami-ullah Rather

    (Department of Chemical and Materials Engineering, King Abdulaziz University, P.O. Box, 80204, Jeddah 21589, Saudi Arabia)

  • Saad Al-Shahrani

    (Department of Chemical and Materials Engineering, King Abdulaziz University, P.O. Box, 80204, Jeddah 21589, Saudi Arabia)

  • Hisham S. Bamufleh

    (Department of Chemical and Materials Engineering, King Abdulaziz University, P.O. Box, 80204, Jeddah 21589, Saudi Arabia)

  • Hesham Alhumade

    (Department of Chemical and Materials Engineering, King Abdulaziz University, P.O. Box, 80204, Jeddah 21589, Saudi Arabia)

  • Aliyu Adebayo Sulaimon

    (Department of Petroleum Engineering, Universiti Teknologi PETRONAS, Bandar Seri Iskandar 32610, Perak, Malaysia)

  • Walid M. Alalayah

    (Department of Chemical and Materials Engineering, King Abdulaziz University, P.O. Box, 80204, Jeddah 21589, Saudi Arabia)

  • Azmi Mohd Shariff

    (Department of Chemical Engineering, Universiti Teknologi PETRONAS, Bandar Seri Iskandar 32610, Perak, Malaysia)

Abstract

Scarcity has made fresh water too economically and socially too valuable to be used by the processing industry without restriction. Wet evaporative cooling cycles offer competitive advantages in terms of CoP compared to other cooling cycles with relatively low cost but requiring extensive quantities of water. Dry cooling, on the other hand, requires large heat-transfer areas, in addition to high power requirements. In this study, a hybrid cycle is proposed for high-end cooling loads of 215 MW. The proposed cycle combines the benefits of phase change to make dry cycles competitive. Furthermore, the proposed cycle also diminishes the extensive use of various chemicals used in wet cooling cycles. The applicable dry bulb temperature range is 25–50 °C. Variations in cooling fluid cold temperature due to ambient conditions are curtailed to a maximum of 2 °C by the proposed cycle. A technoeconomic comparison of the proposed solution to wet evaporative cooling is presented, and the effects are summarized without providing extensive design calculations. ASPEN modules are used design and simulation.

Suggested Citation

  • Aqeel Ahmad Taimoor & Usman Saeed & Sami-ullah Rather & Saad Al-Shahrani & Hisham S. Bamufleh & Hesham Alhumade & Aliyu Adebayo Sulaimon & Walid M. Alalayah & Azmi Mohd Shariff, 2022. "Economic and Technical Analysis of a Hybrid Dry Cooling Cycle to Replace Conventional Wet Cooling Towers for High Process Cooling Loads," Energies, MDPI, vol. 15(21), pages 1-17, October.
    • Handle: RePEc:gam:jeners:v:15:y:2022:i:21:p:7986-:d:955158
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    References listed on IDEAS

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    1. Li, Xiaoxiao & Duniam, Sam & Gurgenci, Hal & Guan, Zhiqiang & Veeraragavan, Anand, 2017. "Full scale experimental study of a small natural draft dry cooling tower for concentrating solar thermal power plant," Applied Energy, Elsevier, vol. 193(C), pages 15-27.
    2. Ehsan, M. Monjurul & Guan, Zhiqiang & Gurgenci, Hal & Klimenko, Alexander, 2020. "Feasibility of dry cooling in supercritical CO2 power cycle in concentrated solar power application: Review and a case study," Renewable and Sustainable Energy Reviews, Elsevier, vol. 132(C).
    3. Sun, Yubiao & Duniam, Sam & Guan, Zhiqiang & Gurgenci, Hal & Dong, Peixin & Wang, Jianyong & Hooman, Kamel, 2019. "Coupling supercritical carbon dioxide Brayton cycle with spray-assisted dry cooling technology for concentrated solar power," Applied Energy, Elsevier, vol. 251(C), pages 1-1.
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