Abstract

To efficiently utilize low-concentrate digestate nutrients, further treatment is needed to decrease their volume, recover process water, and increase nutrient concentrations. Membrane distillation (MD) is a thermally driven process that is advantageous due to its ability to harness low-grade waste heat to treat highly complex wastewater streams. This study assessed the techno-economic performance of integrating MD for two-fold concentrations of nutrients and the recovery of process water from digestate at a thermophilic biogas plant. Thermal assessment showed that the recovered waste heat from flue gas and digestate fully met the thermal energy demand of MD and saved 20% of boiler energy by heating incoming slurry. The permeate flux from MD was 3.5 L/(m(2)h) and 3.1 L/(m(2)h) at 66 degrees C and 61 degrees C digestate inlet temperatures during winter and summer, respectively. With internal heat recovery, the specific heat demand for MD was 80 kWh/m(3) and 100 kWh/m(3) in winter and summer, respectively. The unit cost of MD permeate was estimated to be 3.6 euro/m(3) and 4.1 euro/m(3) at a digestate feed temperature of 66 degrees C and 61 degrees C (with heat recovery), and 7.6 euro/m(3) and 9.1 euro/m(3) (without heat recovery) in winter and summer, respectively. However, cost sensitivity analyses showed that waste heat recovery and thermal energy cost variations had a significant impact on the MD permeate production cost. Nevertheless, the economic assessment indicated that the thermal integration of a biogas plant with industrial-scale MD digestate treatment capacity could be economically feasible, with winter being more economically favorable due to higher waste heat recovery.

Keywords

thermophilic biogas plant; membrane distillation; digestate effluent treatment; concentrated nutrients and water recovery; techno-economic analysis

Published in

Sustainability
2022, volume: 14, number: 20, article number: 13535
Publisher: MDPI

Authors' information