Geothermal energy for wastewater and sludge treatment: An exergoeconomic analysis. (15th November 2020)

• Record Type: Journal Article
• Authors: Di Fraia, Simona; Macaluso, Adriano; Massarotti, Nicola; Vanoli, Laura
• Is Part Of: Energy conversion and management. Volume 224(2020)
• Publication Date: 2020-11-15
• Subjects: Renewable energy -- Polygeneration -- Organic Rankine Cycle -- Geothermal energy -- Thermal drying -- Exergoeconomics; Direct energy conversion -- Periodicals; Energy storage -- Periodicals; Energy transfer -- Periodicals; Énergie -- Conversion directe -- Périodiques; Direct energy conversion; Periodicals; 621.3105
• DOI: 10.1016/j.enconman.2020.113180
• Languages: English
• ISSNs: 0196-8904

Abstract

Graphical abstract: Highlights: Thermal drying is the system component with the lowest exergy efficiency. Increasing the heating system temperature performance of the system increases. When the geo-fluid increase by 50 °C, drying and electricity costs vary by 19% and 28% respectively. Minimum hourly exergoeconomic cost is got when geo-fluid is 110 °C and recycled fraction is 59%. Cost of sludge drying with geothermal energy is similar to that with solar energy. Abstract: The highest economic and environmental costs of wastewater treatment plants are related to waste disposal, which is mainly sludge disposal, and energy supply. Such challenges are even more critical in islands, where there are many environmental, landscape, and geographical constraints that make the use of conventional technologies difficult. For this reason, a geothermal energy system for wastewater and sludge treatment, and power production is proposed. Such a system is assessed through an exergoeconomic analysis, performed in Engineering Equation Solver environment, that allows determining the exergoeconomic costs of geo-fluid, electricity production, and sludge drying. The sensitivity analyses, carried out to assess the effect of several design parameters, have highlighted that the geothermal source temperature significantly affects the system operation and consequently the exergoeconomic costs, which range 77–95 c€/kWhex for sludge treatment and between 4.8 and 6.6c€/kWhex for electricity production. Finally, multivariate optimization has been carried out to find the conditions that minimize the exergoeconomic costs of the system. The total hourly exergoeconomic cost of the system products, namely sludge and electricity, is minimized when the geothermal source temperature is equal to 110 °C and the 58.91% of the desiccant flow is recycled. Overall, this study outlines that an exergy-based economic analysis is fundamental to assess the economic viability of innovative integrated solutions based on renewables.