Research Article
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Year 2020, Volume: 23 Issue: 2, 107 - 126, 28.05.2020
https://doi.org/10.5541/ijot.616899

Abstract

References

  • [1] I. C. Karagiannis and P. G. Soldatos, "Water desalination cost literature: review and assessment," Desalination, vol. 223, no. 1-3, pp. 448-456, 2008.[2] J. E. Miller, "Review of water resources and desalination technologies," Sandia national labs unlimited release report SAND-2003-0800, 2003.[3] E. Mathioulakis, V. Belessiotis, and E. Delyannis, "Desalination by using alternative energy: Review and state-of-the-art," desalination, vol. 203, no. 1-3, pp. 346-365, 2007.[4] C. Charcosset, "A review of membrane processes and renewable energies for desalination," Desalination, vol. 245, no. 1-3, pp. 214-231, 2009.[5] M. A. Eltawil, Z. Zhengming, and L. Yuan, "A review of renewable energy technologies integrated with desalination systems," Renewable and Sustainable Energy Reviews, vol. 13, no. 9, pp. 2245-2262, 2009.[6] K. P. Lee, T. C. Arnot, and D. Mattia, "A review of reverse osmosis membrane materials for desalination—development to date and future potential," Journal of Membrane Science, vol. 370, no. 1-2, pp. 1-22, 2011.[7] S. Porada, R. Zhao, A. Van Der Wal, V. Presser, and P. Biesheuvel, "Review on the science and technology of water desalination by capacitive deionization," Progress in materials science, vol. 58, no. 8, pp. 1388-1442, 2013.[8] L. F. Greenlee, D. F. Lawler, B. D. Freeman, B. Marrot, and P. Moulin, "Reverse osmosis desalination: water sources, technology, and today's challenges," Water research, vol. 43, no. 9, pp. 2317-2348, 2009.[9] F. Banat, "Economic and technical assessment of desalination technologies," in IWA Conference-New Technologies for Water and Wastewater Treatment in the 21st Century, Geneva, Switzerland, June, 2007, pp. 6-8.[10] D. Conti, "Thermodynamic and Economic Evaluation of Co-Production Plants for Electricity and Potable Water," Project paper, Polytechnic of Milan, 2003.[11] L. Garcia-Rodriguez, "Seawater desalination driven by renewable energies: a review," Desalination, vol. 143, no. 2, pp. 103-113, 2002.[12] A. Subramani and J. G. Jacangelo, "Emerging desalination technologies for water treatment: a critical review," Water research, vol. 75, pp. 164-187, 2015.[13] T. Matsuura, "Progress in membrane science and technology for seawater desalination—a review," Desalination, vol. 134, no. 1-3, pp. 47-54, 2001.[14] D. M. Warsinger, J. Swaminathan, E. Guillen-Burrieza, and H. A. Arafat, "Scaling and fouling in membrane distillation for desalination applications: a review," Desalination, vol. 356, pp. 294-313, 2015.[15] H. Sharon and K. Reddy, "A review of solar energy driven desalination technologies," Renewable and Sustainable Energy Reviews, vol. 41, pp. 1080-1118, 2015.[16] S. Tadros, "A new look at dual purpose, water and power, plants-economy and design features," Desalination, vol. 30, no. 1, p. 613, 1979.[17] M. Darwish, F. A. Yousef, and N. Al-Najem, "Energy consumption and costs with a multi-stage flashing (MSF) desalting system," Desalination, vol. 109, no. 3, pp. 285-302, 1997.[18] N. M. Wade, "Energy and cost allocation in dual-purpose power and desalination plants," Desalination, vol. 123, no. 2-3, pp. 115-125, 1999.[19] M. Darwish, "Co-generation power desalting plants: new outlook with gas turbines," Desalination, vol. 161, no. 1, pp. 1-12, 2004.[20] E. Cardona and A. Piacentino, "Optimal design of cogeneration plants for seawater desalination," Desalination, vol. 166, pp. 411-426, 2004.[21] Y. Wang and N. Lior, "Performance analysis of combined humidified gas turbine power generation and multi-effect thermal vapor compression desalination systems—Part 1: The desalination unit and its combination with a steam-injected gas turbine power system," Desalination, vol. 196, no. 1-3, pp. 84-104, 2006.[22] Y. Wang and N. Lior, "Performance analysis of combined humidified gas turbine power generation and multi-effect thermal vapor compression desalination systems: part 2: the evaporative gas turbine based system and some discussions," Desalination, vol. 207, no. 1-3, pp. 243-256, 2007.[23] M. Khoshgoftar Manesh, M. Amidpour, and M. Hamedi, "Optimization of the coupling of pressurized water nuclear reactors and multistage flash desalination plant by evolutionary algorithms and thermoeconomic method," International Journal of Energy Research, vol. 33, no. 1, pp. 77-99, 2009.[24] S. Soufari, M. Zamen, and M. Amidpour, "Performance optimization of the humidification–dehumidification desalination process using mathematical programming," Desalination, vol. 237, no. 1-3, pp. 305-317, 2009.[25] M. Zamen, M. Amidpour, and S. M. Soufari, "Cost optimization of a solar humidification–dehumidification desalination unit using mathematical programming," Desalination, vol. 239, no. 1-3, pp. 92-99, 2009.[26] S. E. Shakib, M. Amidpour, and C. Aghanajafi, "Simulation and optimization of multi effect desalination coupled to a gas turbine plant with HRSG consideration," Desalination, vol. 285, pp. 366-376, 2012.[27] A. Alzahrani, J. Orfi, and Z. Alsuhaibani, "Performance analysis of a gas turbine unit combined with MED-TVC and RO desalination systems," Desalination and Water Treatment, vol. 55, no. 12, pp. 3350-3357, 2015.[28] N. M. Eshoul, B. Agnew, and R. Z. Mathkor, "Thermodynamic analysis of combined cycle power plant standalone and coupled with multi effect desalination with thermal vapor compression," in IREC2015 The Sixth International Renewable Energy Congress, 2015: IEEE, pp. 1-6.[29] N. Eshoul, A. Almutairi, R. Lamidi, H. Alhajeri, and A. Alenezi, "Energetic, Exergetic, and Economic Analysis of MED-TVC Water Desalination Plant with and without Preheating," Water, vol. 10, no. 3, p. 305, 2018.[30] J. Kucera, Desalination: water from water. John Wiley & Sons, 2019.[31] M. Ohkawara, G. Nemoto, Y. Kansha, A. Tsutsumi, M. Ishizuka, and H. Mizuno, "Seawater desalination device and seawater desalination method," ed: Google Patents, 2019.[32] H. Wang, "Low-energy desalination," Nature nanotechnology, vol. 13, no. 4, p. 273, 2018.[33] A. Bejan, G. Tsatsaronis, M. Moran, and M. J. Moran, Thermal Design and Optimization. Wiley, 1996.[34] I. Dincer, M. A. Rosen, and P. Ahmadi, Optimization of Energy Systems. Wiley, 2017.[35] I. Dincer and M. A. Rosen, "Chapter 3 - Chemical Exergy," in Exergy (Second Edition), I. Dincer and M. A. Rosen, Eds.: Elsevier, 2013, pp. 31-49.[36] M. H. Sharqawy, S. M. Zubair, and J. H. Lienhard, "Second law analysis of reverse osmosis desalination plants: An alternative design using pressure retarded osmosis," Energy, vol. 36, no. 11, pp. 6617-6626, 2011/11/01/ 2011.[37] E. J. C. Cavalcanti, "Exergoeconomic and exergoenvironmental analyses of an integrated solar combined cycle system," Renewable and Sustainable Energy Reviews, vol. 67, pp. 507-519, 2017.[38] M. Goedkoop, R. Spriensma, S. Effting, and M. Collignon, The Eco-indicator 99: A Damage Oriented Method for Life-cycle Impact Assessment : Manual for Designers. PRé, Product Ecology consultants, 2000.[39] G. Raluy, L. Serra, and J. Uche, "Life cycle assessment of MSF, MED and RO desalination technologies," Energy, vol. 31, no. 13, pp. 2361-2372, 2006/10/01/ 2006.[40] A. Valero et al., "CGAM problem: Definition and conventional solution," Energy, vol. 19, no. 3, pp. 279-286, 1994/03/01/ 1994.[41] K. H. Mistry, M. Antar, and J. H. Lienhard V, An improved model for multiple effect distillation. 2012, pp. 1-15.[42] A. S. Hassan and M. A. Darwish, "Performance of thermal vapor compression," Desalination, vol. 335, no. 1, pp. 41-46, 2014/02/17/ 2014.[43] A. Al-Zahrani, J. Orfi, Z. Al-Suhaibani, B. Salim, and H. Al-Ansary, "Thermodynamic Analysis of a Reverse Osmosis Desalination Unit with Energy Recovery System," Procedia Engineering, vol. 33, pp. 404-414, 2012/01/01/ 2012.[44] H. Ghaebi, M. H. Saidi, and P. Ahmadi, "Exergoeconomic optimization of a trigeneration system for heating, cooling and power production purpose based on TRR method and using evolutionary algorithm," Applied Thermal Engineering, vol. 36, pp. 113-125, 2012/04/01/ 2012.[45] F. A. Boyaghchi and P. Heidarnejad, "Thermoeconomic assessment and multi objective optimization of a solar micro CCHP based on Organic Rankine Cycle for domestic application," Energy Conversion and Management, vol. 97, pp. 224-234, 2015/06/01/ 2015.[46] Y. M. El-Sayed, The Thermoeconomics of Energy Conversions. Elsevier Science, 2013.[47] C. Park et al., "Stochastic cost estimation approach for full-scale reverse osmosis desalination plants," Journal of Membrane Science, vol. 364, no. 1, pp. 52-64, 2010/11/15/ 2010.[48] W. Zhou, L. Song, and T. K. Guan, "A numerical study on concentration polarization and system performance of spiral wound RO membrane modules," Journal of Membrane Science, vol. 271, no. 1, pp. 38-46, 2006/03/01/ 2006.

4E Analysis of Power and Water Cogeneration Plant based on Integrated MED-TVC and RO Desalination Units

Year 2020, Volume: 23 Issue: 2, 107 - 126, 28.05.2020
https://doi.org/10.5541/ijot.616899

Abstract

In this study, integration of RO desalination unit with power and water cogeneration plant located in Qeshm Island in Iran has been investigated. The desalination unit exists in this plant is MED-TVC type. In this regard, energy, exergy, exergoeconomic, and exergoenvironmental (4E) analyses have been performed by developing a computer code using Matlab. Validation of thermodynamic data has been performed through comparing the results of modeling by Matlab with the simulation done in Thermoflex software and the real data gathered from the Qeshm cogeneration plant. The results show the acceptable accuracy of thermodynamic modeling. The exergoenvironmental analysis has been conducted based on Life Cycle Assessment (LCA). In this regard, the weight function of TVC is proposed in this paper based on technical data in different nominal sizes in order to estimate the environmental impacts of this component. The cogeneration plant produces 25.7 MW power, consuming 6 kg/s steam can lead to production of 51.7 kg/s desalinated water. The gained output ratio (GOR) is about 8.7 for the MEDTVC unit. The performance ratio (PR) of RO desalination unit which is added to the downstream of MED-TVC has been calculated about 0.5. Integrating RO desalination unit with MED-TVC enhances the production of fresh water by 255.132 ton per hour.
Exergetic efficiency, total cost rate of the system and total environmental impact rate of the system has been calculated 46.86 %, 64.01 $/min and 29.49 pts/min, respectively. Since the largest share of exergy destruction rate of the system belongs to the gas cycle and also Qeshm Island has a warm and muggy climate, adding a chiller type air cooling system to inlet of air compressor can decrease the power demand of air compressor and fuel consumption of combustion chamber which makes the system more efficient and reduce the cost and environmental impact rate of the system.




References

  • [1] I. C. Karagiannis and P. G. Soldatos, "Water desalination cost literature: review and assessment," Desalination, vol. 223, no. 1-3, pp. 448-456, 2008.[2] J. E. Miller, "Review of water resources and desalination technologies," Sandia national labs unlimited release report SAND-2003-0800, 2003.[3] E. Mathioulakis, V. Belessiotis, and E. Delyannis, "Desalination by using alternative energy: Review and state-of-the-art," desalination, vol. 203, no. 1-3, pp. 346-365, 2007.[4] C. Charcosset, "A review of membrane processes and renewable energies for desalination," Desalination, vol. 245, no. 1-3, pp. 214-231, 2009.[5] M. A. Eltawil, Z. Zhengming, and L. Yuan, "A review of renewable energy technologies integrated with desalination systems," Renewable and Sustainable Energy Reviews, vol. 13, no. 9, pp. 2245-2262, 2009.[6] K. P. Lee, T. C. Arnot, and D. Mattia, "A review of reverse osmosis membrane materials for desalination—development to date and future potential," Journal of Membrane Science, vol. 370, no. 1-2, pp. 1-22, 2011.[7] S. Porada, R. Zhao, A. Van Der Wal, V. Presser, and P. Biesheuvel, "Review on the science and technology of water desalination by capacitive deionization," Progress in materials science, vol. 58, no. 8, pp. 1388-1442, 2013.[8] L. F. Greenlee, D. F. Lawler, B. D. Freeman, B. Marrot, and P. Moulin, "Reverse osmosis desalination: water sources, technology, and today's challenges," Water research, vol. 43, no. 9, pp. 2317-2348, 2009.[9] F. Banat, "Economic and technical assessment of desalination technologies," in IWA Conference-New Technologies for Water and Wastewater Treatment in the 21st Century, Geneva, Switzerland, June, 2007, pp. 6-8.[10] D. Conti, "Thermodynamic and Economic Evaluation of Co-Production Plants for Electricity and Potable Water," Project paper, Polytechnic of Milan, 2003.[11] L. Garcia-Rodriguez, "Seawater desalination driven by renewable energies: a review," Desalination, vol. 143, no. 2, pp. 103-113, 2002.[12] A. Subramani and J. G. Jacangelo, "Emerging desalination technologies for water treatment: a critical review," Water research, vol. 75, pp. 164-187, 2015.[13] T. Matsuura, "Progress in membrane science and technology for seawater desalination—a review," Desalination, vol. 134, no. 1-3, pp. 47-54, 2001.[14] D. M. Warsinger, J. Swaminathan, E. Guillen-Burrieza, and H. A. Arafat, "Scaling and fouling in membrane distillation for desalination applications: a review," Desalination, vol. 356, pp. 294-313, 2015.[15] H. Sharon and K. Reddy, "A review of solar energy driven desalination technologies," Renewable and Sustainable Energy Reviews, vol. 41, pp. 1080-1118, 2015.[16] S. Tadros, "A new look at dual purpose, water and power, plants-economy and design features," Desalination, vol. 30, no. 1, p. 613, 1979.[17] M. Darwish, F. A. Yousef, and N. Al-Najem, "Energy consumption and costs with a multi-stage flashing (MSF) desalting system," Desalination, vol. 109, no. 3, pp. 285-302, 1997.[18] N. M. Wade, "Energy and cost allocation in dual-purpose power and desalination plants," Desalination, vol. 123, no. 2-3, pp. 115-125, 1999.[19] M. Darwish, "Co-generation power desalting plants: new outlook with gas turbines," Desalination, vol. 161, no. 1, pp. 1-12, 2004.[20] E. Cardona and A. Piacentino, "Optimal design of cogeneration plants for seawater desalination," Desalination, vol. 166, pp. 411-426, 2004.[21] Y. Wang and N. Lior, "Performance analysis of combined humidified gas turbine power generation and multi-effect thermal vapor compression desalination systems—Part 1: The desalination unit and its combination with a steam-injected gas turbine power system," Desalination, vol. 196, no. 1-3, pp. 84-104, 2006.[22] Y. Wang and N. Lior, "Performance analysis of combined humidified gas turbine power generation and multi-effect thermal vapor compression desalination systems: part 2: the evaporative gas turbine based system and some discussions," Desalination, vol. 207, no. 1-3, pp. 243-256, 2007.[23] M. Khoshgoftar Manesh, M. Amidpour, and M. Hamedi, "Optimization of the coupling of pressurized water nuclear reactors and multistage flash desalination plant by evolutionary algorithms and thermoeconomic method," International Journal of Energy Research, vol. 33, no. 1, pp. 77-99, 2009.[24] S. Soufari, M. Zamen, and M. Amidpour, "Performance optimization of the humidification–dehumidification desalination process using mathematical programming," Desalination, vol. 237, no. 1-3, pp. 305-317, 2009.[25] M. Zamen, M. Amidpour, and S. M. Soufari, "Cost optimization of a solar humidification–dehumidification desalination unit using mathematical programming," Desalination, vol. 239, no. 1-3, pp. 92-99, 2009.[26] S. E. Shakib, M. Amidpour, and C. Aghanajafi, "Simulation and optimization of multi effect desalination coupled to a gas turbine plant with HRSG consideration," Desalination, vol. 285, pp. 366-376, 2012.[27] A. Alzahrani, J. Orfi, and Z. Alsuhaibani, "Performance analysis of a gas turbine unit combined with MED-TVC and RO desalination systems," Desalination and Water Treatment, vol. 55, no. 12, pp. 3350-3357, 2015.[28] N. M. Eshoul, B. Agnew, and R. Z. Mathkor, "Thermodynamic analysis of combined cycle power plant standalone and coupled with multi effect desalination with thermal vapor compression," in IREC2015 The Sixth International Renewable Energy Congress, 2015: IEEE, pp. 1-6.[29] N. Eshoul, A. Almutairi, R. Lamidi, H. Alhajeri, and A. Alenezi, "Energetic, Exergetic, and Economic Analysis of MED-TVC Water Desalination Plant with and without Preheating," Water, vol. 10, no. 3, p. 305, 2018.[30] J. Kucera, Desalination: water from water. John Wiley & Sons, 2019.[31] M. Ohkawara, G. Nemoto, Y. Kansha, A. Tsutsumi, M. Ishizuka, and H. Mizuno, "Seawater desalination device and seawater desalination method," ed: Google Patents, 2019.[32] H. Wang, "Low-energy desalination," Nature nanotechnology, vol. 13, no. 4, p. 273, 2018.[33] A. Bejan, G. Tsatsaronis, M. Moran, and M. J. Moran, Thermal Design and Optimization. Wiley, 1996.[34] I. Dincer, M. A. Rosen, and P. Ahmadi, Optimization of Energy Systems. Wiley, 2017.[35] I. Dincer and M. A. Rosen, "Chapter 3 - Chemical Exergy," in Exergy (Second Edition), I. Dincer and M. A. Rosen, Eds.: Elsevier, 2013, pp. 31-49.[36] M. H. Sharqawy, S. M. Zubair, and J. H. Lienhard, "Second law analysis of reverse osmosis desalination plants: An alternative design using pressure retarded osmosis," Energy, vol. 36, no. 11, pp. 6617-6626, 2011/11/01/ 2011.[37] E. J. C. Cavalcanti, "Exergoeconomic and exergoenvironmental analyses of an integrated solar combined cycle system," Renewable and Sustainable Energy Reviews, vol. 67, pp. 507-519, 2017.[38] M. Goedkoop, R. Spriensma, S. Effting, and M. Collignon, The Eco-indicator 99: A Damage Oriented Method for Life-cycle Impact Assessment : Manual for Designers. PRé, Product Ecology consultants, 2000.[39] G. Raluy, L. Serra, and J. Uche, "Life cycle assessment of MSF, MED and RO desalination technologies," Energy, vol. 31, no. 13, pp. 2361-2372, 2006/10/01/ 2006.[40] A. Valero et al., "CGAM problem: Definition and conventional solution," Energy, vol. 19, no. 3, pp. 279-286, 1994/03/01/ 1994.[41] K. H. Mistry, M. Antar, and J. H. Lienhard V, An improved model for multiple effect distillation. 2012, pp. 1-15.[42] A. S. Hassan and M. A. Darwish, "Performance of thermal vapor compression," Desalination, vol. 335, no. 1, pp. 41-46, 2014/02/17/ 2014.[43] A. Al-Zahrani, J. Orfi, Z. Al-Suhaibani, B. Salim, and H. Al-Ansary, "Thermodynamic Analysis of a Reverse Osmosis Desalination Unit with Energy Recovery System," Procedia Engineering, vol. 33, pp. 404-414, 2012/01/01/ 2012.[44] H. Ghaebi, M. H. Saidi, and P. Ahmadi, "Exergoeconomic optimization of a trigeneration system for heating, cooling and power production purpose based on TRR method and using evolutionary algorithm," Applied Thermal Engineering, vol. 36, pp. 113-125, 2012/04/01/ 2012.[45] F. A. Boyaghchi and P. Heidarnejad, "Thermoeconomic assessment and multi objective optimization of a solar micro CCHP based on Organic Rankine Cycle for domestic application," Energy Conversion and Management, vol. 97, pp. 224-234, 2015/06/01/ 2015.[46] Y. M. El-Sayed, The Thermoeconomics of Energy Conversions. Elsevier Science, 2013.[47] C. Park et al., "Stochastic cost estimation approach for full-scale reverse osmosis desalination plants," Journal of Membrane Science, vol. 364, no. 1, pp. 52-64, 2010/11/15/ 2010.[48] W. Zhou, L. Song, and T. K. Guan, "A numerical study on concentration polarization and system performance of spiral wound RO membrane modules," Journal of Membrane Science, vol. 271, no. 1, pp. 38-46, 2006/03/01/ 2006.
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Details

Primary Language English
Subjects Mechanical Engineering
Journal Section Regular Original Research Article
Authors

Hossein Vazini Modabber

Mohammad Hasan Khoshgoftar Manesh

Publication Date May 28, 2020
Published in Issue Year 2020 Volume: 23 Issue: 2

Cite

APA Vazini Modabber, H., & Khoshgoftar Manesh, M. H. (2020). 4E Analysis of Power and Water Cogeneration Plant based on Integrated MED-TVC and RO Desalination Units. International Journal of Thermodynamics, 23(2), 107-126. https://doi.org/10.5541/ijot.616899
AMA Vazini Modabber H, Khoshgoftar Manesh MH. 4E Analysis of Power and Water Cogeneration Plant based on Integrated MED-TVC and RO Desalination Units. International Journal of Thermodynamics. May 2020;23(2):107-126. doi:10.5541/ijot.616899
Chicago Vazini Modabber, Hossein, and Mohammad Hasan Khoshgoftar Manesh. “4E Analysis of Power and Water Cogeneration Plant Based on Integrated MED-TVC and RO Desalination Units”. International Journal of Thermodynamics 23, no. 2 (May 2020): 107-26. https://doi.org/10.5541/ijot.616899.
EndNote Vazini Modabber H, Khoshgoftar Manesh MH (May 1, 2020) 4E Analysis of Power and Water Cogeneration Plant based on Integrated MED-TVC and RO Desalination Units. International Journal of Thermodynamics 23 2 107–126.
IEEE H. Vazini Modabber and M. H. Khoshgoftar Manesh, “4E Analysis of Power and Water Cogeneration Plant based on Integrated MED-TVC and RO Desalination Units”, International Journal of Thermodynamics, vol. 23, no. 2, pp. 107–126, 2020, doi: 10.5541/ijot.616899.
ISNAD Vazini Modabber, Hossein - Khoshgoftar Manesh, Mohammad Hasan. “4E Analysis of Power and Water Cogeneration Plant Based on Integrated MED-TVC and RO Desalination Units”. International Journal of Thermodynamics 23/2 (May 2020), 107-126. https://doi.org/10.5541/ijot.616899.
JAMA Vazini Modabber H, Khoshgoftar Manesh MH. 4E Analysis of Power and Water Cogeneration Plant based on Integrated MED-TVC and RO Desalination Units. International Journal of Thermodynamics. 2020;23:107–126.
MLA Vazini Modabber, Hossein and Mohammad Hasan Khoshgoftar Manesh. “4E Analysis of Power and Water Cogeneration Plant Based on Integrated MED-TVC and RO Desalination Units”. International Journal of Thermodynamics, vol. 23, no. 2, 2020, pp. 107-26, doi:10.5541/ijot.616899.
Vancouver Vazini Modabber H, Khoshgoftar Manesh MH. 4E Analysis of Power and Water Cogeneration Plant based on Integrated MED-TVC and RO Desalination Units. International Journal of Thermodynamics. 2020;23(2):107-26.

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