Author/Authors :
Abedi, Mohammad Reza Energy Systems Engineering Group - Faculty of Marine Science - Islamic Azad University North Tehran Branch, Tehran, Iran , Salehi, Gholamreza Mechanical Engineering Group - Faculty of Engineering - Islamic Azad University Central Tehran Branch, Tehran, Iran , Torabi Azad, Masoud Energy Systems Engineering Group - Faculty of Marine Science - Islamic Azad University North Tehran Branch, Tehran, Iran , Khosgoftar Manesh, Mohammad Hasan Environmental and Biological Systems Research Lab (EEBRlab) - Division of Thermal Sciences and Energy Systems - Department of Mechanical Engineering - Faculty of Technology & Engineering - University of Qom, Qom, Iran , Fallahsohi, Hossein Energy Systems Engineering Group - Faculty of Marine Science - Islamic Azad University North Tehran Branch, Tehran, Iran
Abstract :
Hybrid power and desalinated water generation systems with two Multi-Effect
Distillation (MED) technologies and Reverse Osmosis (RO) are investigated for a combined-
cycle power plant in this study. The generated steam enters MED from the low-pressure
section of the Heat Recovery Steam Generator (HRSG) in the hybrid system. Seawater is
divided into two sections after entering the MED condenser – one part is fed into MED and its
process. The other is rejected after cooling in the condenser and turns back to the sea. A
reverse osmotic desalination system is implemented in this study. In the present combined
cycles, steam generated in the Low Pressure (LP) section enters the steam turbine. To reduce
the generated power and increase desalinated water in MED and RO, exergy analysis and
cycle optimization are required. The system is simulated and verified based on the available
data on the model power plant. The results showed that by selecting 43 optimization
parameters and applying constraints like acidification temperature, the integrated cycle's
exergy efficiency could be raised by 50%. Under this condition, the water price is calculated to
be 1.16 $/m3. Under hybrid conditions of the design power and freshwater cogeneration
system, the present design's efficiency without optimization and its final cost is 48.8% and
approximately 1.2 $/m3.
Keywords :
Hybrid desalination system , MED , RO , combined cycle , economic analysis , exergy