The work proposes an insight into an innovative combination of thermal seawater desalination technologies (forward osmosis and membrane distillation) fed by sensible waste heat recovered from the cooler of a supercritical CO2 cycle of a concentrating solar plant. The sensible heat at low temperature, from 50 to 75 °C, is exploited in the forward osmosis plant adopting a thermo-responsive draw agent, where 60% of available freshwater is separated from the seawater with a thermal consumption of 89 kWhth/m3. At temperatures up to 90 – 100 °C, the rejected heat is used in the vacuum membrane distillation plant with an innovative layout, bringing the brine close to crystallization and entailing a thermal consumption of 187 kWhth/m3. Finally, a crystallizer operated with the sensible low temperature heat from the cycle precipitates the salts, recovering part of them. The work presents a novel integration in series of various thermal desalination technologies to approach zero liquid discharge and includes the system hybridization with a next generation renewable concentrating solar plant, demonstrating the technological attractiveness in both technologies. With simulations of annual performances of the solar-power section, assuming a 100 MWel CSP plant in Sevilla, the annual freshwater production is evaluated at 3.39 Mm3/year, with 32 kton/year of salts separated and 4040 equivalent operating hours. The proposed configuration leads to overall specific thermal consumption of 156 kWhth/m3, a level lower than conventional desalination solutions at constant output products, with water recovery ratio of 95%, thus reducing the issues related to brine management of commercial plants.

Hybridization of Innovative Seawater Thermal Desalination Technologies up to ZLD with sCO2 Concentrated Solar Power Plants

Morosini, Ettore;Carraretto, Igor Matteo;Manzolini, Giampaolo
2026-01-01

Abstract

The work proposes an insight into an innovative combination of thermal seawater desalination technologies (forward osmosis and membrane distillation) fed by sensible waste heat recovered from the cooler of a supercritical CO2 cycle of a concentrating solar plant. The sensible heat at low temperature, from 50 to 75 °C, is exploited in the forward osmosis plant adopting a thermo-responsive draw agent, where 60% of available freshwater is separated from the seawater with a thermal consumption of 89 kWhth/m3. At temperatures up to 90 – 100 °C, the rejected heat is used in the vacuum membrane distillation plant with an innovative layout, bringing the brine close to crystallization and entailing a thermal consumption of 187 kWhth/m3. Finally, a crystallizer operated with the sensible low temperature heat from the cycle precipitates the salts, recovering part of them. The work presents a novel integration in series of various thermal desalination technologies to approach zero liquid discharge and includes the system hybridization with a next generation renewable concentrating solar plant, demonstrating the technological attractiveness in both technologies. With simulations of annual performances of the solar-power section, assuming a 100 MWel CSP plant in Sevilla, the annual freshwater production is evaluated at 3.39 Mm3/year, with 32 kton/year of salts separated and 4040 equivalent operating hours. The proposed configuration leads to overall specific thermal consumption of 156 kWhth/m3, a level lower than conventional desalination solutions at constant output products, with water recovery ratio of 95%, thus reducing the issues related to brine management of commercial plants.
2026
Annual Analysis
CSP+D
Electricity and Freshwater
Forward Osmosis
Membrane Distillation
Solar Desalination
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Utilizza questo identificativo per citare o creare un link a questo documento: https://hdl.handle.net/11311/1317945
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