Zeotropic mixture as a working fluid for cascade Rankine cycle-based reverse osmosis: Energy, exergy, and economic analysis

This study investigates the cascade Rankine cycle coupled with a reverse osmosis system for brackish groundwater treatment. The proposed system integrates a steam Rankine cycle (SRC) and an organic Rankine cycle (ORC) in a looped configuration, utilizing solar energy as a heat source. Each Rankine c...

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Main Authors: Milan Raninga, Anurag Mudgal, Vivek Patel, Jatin Patel
Format: Article
Language:English
Published: Elsevier 2024-11-01
Series:International Journal of Thermofluids
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Online Access:http://www.sciencedirect.com/science/article/pii/S2666202724003306
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author Milan Raninga
Anurag Mudgal
Vivek Patel
Jatin Patel
author_facet Milan Raninga
Anurag Mudgal
Vivek Patel
Jatin Patel
author_sort Milan Raninga
collection DOAJ
description This study investigates the cascade Rankine cycle coupled with a reverse osmosis system for brackish groundwater treatment. The proposed system integrates a steam Rankine cycle (SRC) and an organic Rankine cycle (ORC) in a looped configuration, utilizing solar energy as a heat source. Each Rankine cycle is coupled with reverse osmosis (RO) to produce approximately 1 m3/h of permeate from each RO system. The system is investigated with working fluid combinations from R1233zd(E), R1234ze(Z), and R1336mzz(Z). Through comprehensive energy, exergy, and economic analyses, the system's performance is evaluated with zeotropic mixtures compared to pure R1233zd(E). The results demonstrate reliable performance with zeotropic mixtures, particularly R1233zd(E)/R1234ze(Z) with a mass composition of 0.6/0.4, demonstrating the maximum ORC expander work output of 1.15 kW. Parametric analysis reveals remarkable performance under different ORC system parameters. Variations in SRC condensation pressure show a trade-off performance between SRC and ORC turbine work output. Exergy analysis reveals an increase in exergy destruction by evaporation-based ORC components and a reduction in exergy destruction by condensation-based components, emphasizing improved irreversibility during the condensation process. Economic analysis indicates a marginal impact on the overall system cost, with the treated water cost ranging from 0.891 to 0.919 $/m3.
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spelling doaj-art-e05629b09bda42a48cb9fccba8ffde6a2025-08-20T02:50:13ZengElsevierInternational Journal of Thermofluids2666-20272024-11-012410089010.1016/j.ijft.2024.100890Zeotropic mixture as a working fluid for cascade Rankine cycle-based reverse osmosis: Energy, exergy, and economic analysisMilan Raninga0Anurag Mudgal1Vivek Patel2Jatin Patel3Department of Mechanical Engineering, School of Technology, Pandit Deendayal Energy University, Gandhinagar, IndiaCorresponding author.; Department of Mechanical Engineering, School of Technology, Pandit Deendayal Energy University, Gandhinagar, IndiaDepartment of Mechanical Engineering, School of Technology, Pandit Deendayal Energy University, Gandhinagar, IndiaDepartment of Mechanical Engineering, School of Technology, Pandit Deendayal Energy University, Gandhinagar, IndiaThis study investigates the cascade Rankine cycle coupled with a reverse osmosis system for brackish groundwater treatment. The proposed system integrates a steam Rankine cycle (SRC) and an organic Rankine cycle (ORC) in a looped configuration, utilizing solar energy as a heat source. Each Rankine cycle is coupled with reverse osmosis (RO) to produce approximately 1 m3/h of permeate from each RO system. The system is investigated with working fluid combinations from R1233zd(E), R1234ze(Z), and R1336mzz(Z). Through comprehensive energy, exergy, and economic analyses, the system's performance is evaluated with zeotropic mixtures compared to pure R1233zd(E). The results demonstrate reliable performance with zeotropic mixtures, particularly R1233zd(E)/R1234ze(Z) with a mass composition of 0.6/0.4, demonstrating the maximum ORC expander work output of 1.15 kW. Parametric analysis reveals remarkable performance under different ORC system parameters. Variations in SRC condensation pressure show a trade-off performance between SRC and ORC turbine work output. Exergy analysis reveals an increase in exergy destruction by evaporation-based ORC components and a reduction in exergy destruction by condensation-based components, emphasizing improved irreversibility during the condensation process. Economic analysis indicates a marginal impact on the overall system cost, with the treated water cost ranging from 0.891 to 0.919 $/m3.http://www.sciencedirect.com/science/article/pii/S2666202724003306Zeotropic mixturesSteam rankine cycleOrganic rankine cycleReverse osmosis
spellingShingle Milan Raninga
Anurag Mudgal
Vivek Patel
Jatin Patel
Zeotropic mixture as a working fluid for cascade Rankine cycle-based reverse osmosis: Energy, exergy, and economic analysis
International Journal of Thermofluids
Zeotropic mixtures
Steam rankine cycle
Organic rankine cycle
Reverse osmosis
title Zeotropic mixture as a working fluid for cascade Rankine cycle-based reverse osmosis: Energy, exergy, and economic analysis
title_full Zeotropic mixture as a working fluid for cascade Rankine cycle-based reverse osmosis: Energy, exergy, and economic analysis
title_fullStr Zeotropic mixture as a working fluid for cascade Rankine cycle-based reverse osmosis: Energy, exergy, and economic analysis
title_full_unstemmed Zeotropic mixture as a working fluid for cascade Rankine cycle-based reverse osmosis: Energy, exergy, and economic analysis
title_short Zeotropic mixture as a working fluid for cascade Rankine cycle-based reverse osmosis: Energy, exergy, and economic analysis
title_sort zeotropic mixture as a working fluid for cascade rankine cycle based reverse osmosis energy exergy and economic analysis
topic Zeotropic mixtures
Steam rankine cycle
Organic rankine cycle
Reverse osmosis
url http://www.sciencedirect.com/science/article/pii/S2666202724003306
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AT anuragmudgal zeotropicmixtureasaworkingfluidforcascaderankinecyclebasedreverseosmosisenergyexergyandeconomicanalysis
AT vivekpatel zeotropicmixtureasaworkingfluidforcascaderankinecyclebasedreverseosmosisenergyexergyandeconomicanalysis
AT jatinpatel zeotropicmixtureasaworkingfluidforcascaderankinecyclebasedreverseosmosisenergyexergyandeconomicanalysis