Utilization of municipal wastewater for cooling in thermoelectric power plants
•A model is developed to predict the water quality in the recirculating cooling loop.•NH3 and CO2 evaporation in the cooling tower can significantly impact cooling loop pH.•The effects of the CO2 and NH3 mass transfer coefficients on loop pH are quantified.•Salt formation significantly impacts the l...
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Veröffentlicht in: | Fuel (Guildford) 2013-09, Vol.111 (C), p.103-113 |
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Format: | Artikel |
Sprache: | eng |
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Zusammenfassung: | •A model is developed to predict the water quality in the recirculating cooling loop.•NH3 and CO2 evaporation in the cooling tower can significantly impact cooling loop pH.•The effects of the CO2 and NH3 mass transfer coefficients on loop pH are quantified.•Salt formation significantly impacts the loop pH for nitrified municipal wastewater.•The rates of evaporation of volatiles are proportional to the flow rate of the blowdown.
A process simulation model has been developed using Aspen Plus® with the OLI (OLI System, Inc.) water chemistry model to predict water quality in the recirculating cooling loop utilizing secondary- and tertiary-treated municipal wastewater as the source of makeup water. Simulation results were compared with pilot-scale experimental data on makeup water alkalinity, loop pH, and ammonia evaporation. The effects of various parameters including makeup water quality, salt formation, NH3 and CO2 evaporation mass transfer coefficients, heat load, and operating temperatures were investigated. The results indicate that, although the simulation model can capture the general trends in the loop pH, experimental data on the rates of salt precipitation in the system are needed for more accurate prediction of the loop pH. It was also found that stripping of ammonia and carbon dioxide in the cooling tower can influence the cooling loop pH significantly. The effects of the NH3 mass transfer coefficient on cooling loop pH appear to be more significant at lower values (e.g., kNH3 |
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ISSN: | 0016-2361 1873-7153 |
DOI: | 10.1016/j.fuel.2013.03.062 |