Abstract
In this work, a multi-effect distillation with thermal vapor compression desalination unit is proposed to satisfy the freshwater demand of São Mateus, Espírito Santo, Brazil. The desalination unit is driven by saturated vapor produced by boiler or heat recovery steam generator. The goal and main contribution of this work are, respectively, to compare and evaluate the most feasible configuration among a steam power cycle, gas turbine and combined cycle power plant. To accomplish this objective, the first and second laws of thermodynamics are used, and economic analyses are carried out for each option. In consequence, an optimization using a genetic algorithm shows the optimal results. The usage of an exergy-based approach for cost allocation assists in the best judgment. For instance, the combined cycle power plant driving a desalination unit presents the highest net power generation of 51.7 MW and a total cost rate of 24,811 US$ h−1, which means a Leveled Cost of Energy of around 0.132 US$ kWh−1. In addition, it has the lowest exergetic and monetary costs of net power (2.316 kJ kJ−1 and 0.132 US$ kWh−1) and freshwater (17.9 kJ kJ−1 and 2.684 US$ kWh−1). However, it also has the highest environmental cost for net power (22.451 kgCO2 kWh−1) and the second highest one for freshwater (196.120 × 10−3 kgCO2 m−3).
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Abbreviations
- c:
-
Monetary unit cost [US$ kWh−1]
- CRF:
-
Annual capital recovery factor
- DTML:
-
Logarithmic mean temperature difference [°C]
- E:
-
Exergy [kW]
- h:
-
Specific enthalpy [kJ kg−1]
- k:
-
Exergetic unit cost [kW kW−1]
- \({\dot{m}}\) :
-
Mass flow rate [kg s−1]
- N:
-
Hour of plant operation per year [h]
- OF:
-
Objective function
- P:
-
Pressure [kPa]
- \({\dot{Q}}\) :
-
Heat transfer rate [kW]
- RP:
-
Pressure relation
- T:
-
Temperature [°C]
- TCI:
-
Total cost of investment
- \({\dot{W}}\) :
-
Power [kW]
- x:
-
Mass fraction
- Ż:
-
Cost rate [$ s−1]
- AC:
-
Air compressor
- APP:
-
Economizer approach
- BO:
-
Boiler
- br:
-
Brine
- CC:
-
Combustion chamber
- ec:
-
Economizer
- ev:
-
Evaporator
- F:
-
Fuel
- fw:
-
Freshwater
- GT:
-
Gas turbine
- in:
-
Inlet
- NET:
-
Net output
- out:
-
Outlet
- PM:
-
Pump and motor
- PP:
-
Pinch point
- rw:
-
Return water
- SA:
-
Superheating
- sh:
-
Superheater
- ST:
-
Steam turbine
- sw:
-
Sea water
- TOT:
-
Total
- α:
-
External fuel unit cost
- η:
-
Isentropic efficiency
- λ:
-
Specific CO2 emission [kgCO2 kWh−1]
- φ:
-
Maintenance factor [–]
- ΔT:
-
Temperature difference [°C]
- AC:
-
Air compressor
- BO:
-
Boiler
- CC:
-
Combustion chamber
- CCI:
-
Construction cost index
- CCPP:
-
Combined cycle power plant
- CEPCI:
-
Chemical engineering plant cost index
- ENR:
-
Engineering News-Record
- FI:
-
Installation factor
- GOR:
-
Gain output ration
- GT:
-
Gas turbine
- HRS:
-
Heat recovery steam generator
- MED:
-
Multi-effect distillation
- MSF:
-
Multi stage flash
- OF:
-
Objective function
- PEC:
-
Purchase equipment cost
- PM:
-
Pump and motor
- RO:
-
Reverse osmosis
- ST:
-
Steam turbine
- TVC:
-
Thermal vapor compression
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Acknowledgements
The authors would like to thank Professor Márcio Coelho de Mattos, Head of DEM/Ufes, for his support.
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This research did not receive any specific grant from funding agencies in the public, commercial, or not-for-profit sectors.
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Chun, A., Barone, M.A. & Lourenço, A.B. Optimization of three power and desalination plants and exergy-based economic and CO2 emission cost allocation and comparison. Int J Energ Water Res 4, 13–25 (2020). https://doi.org/10.1007/s42108-019-00047-3
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DOI: https://doi.org/10.1007/s42108-019-00047-3