4.7 Article

Membrane distillation for separation and recovery of valuable compounds from anaerobic digestates

Journal

SEPARATION AND PURIFICATION TECHNOLOGY
Volume 315, Issue -, Pages -

Publisher

ELSEVIER
DOI: 10.1016/j.seppur.2023.123687

Keywords

Digestate treatment; Nutrients separation; Membrane distillation; Water recovery

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This study assesses the potential of Direct Contact Membrane Distillation (DCMD) for separating nutrients and recovering water from the liquid phase of digestate. The results show that DCMD can effectively separate water vapor and address the issues of high salinity and soluble ammoniacal nitrogen in digestate, making it possible for digestate to be reused.
Digestate - the wet by-product of the anaerobic digestion (AD) of organic waste - is composed of a mixture of residual organic matter, microbial biomass and inorganic compounds. Although digestate is rich in nutrients, the occurrence of high levels of salinity and soluble ammoniacal nitrogen (N-NH4+) limits its direct exploitation as organic fertilizer and imposes a complex disposal. This study assesses at laboratory-scale the potential of Direct Contact Membrane Distillation (DCMD) for the separation of nutrients and the recovery of water from the liquid phase of the digestate produced by a digester that treats cattle manure and agricultural residues. Experimental tests, carried out at different feed temperature (50-70 degrees C) and initial pH (6-8.2) of the liquid digestate, aimed at investigating the effect of the operating conditions on the transmembrane flux of water vapor, the concentration of N-NH4+, P-PO3-, and Chemical Oxygen Demand (COD) in both permeate (also referred to as distillate) and retentate streams. For raw digestate, the initial transmembrane flux enhanced from 1.83 L center dot m(-2)center dot h(-1) to 5.55 L center dot m(-2)center dot h(-1), in response to increasing temperature gradient. Overall, the highest achieved water recovery factor was 40% at a feed temperature of 70 degrees C. The pH had a limited impact on the transmembrane flux, whereas notably affected the DCMD performance in terms of separation efficiency. In particular, a pH reduction from 8.2 (raw digestate) to 6 was able to completely avoid the transfer of N-NH4+ into the distillate. Compared to the concentration in the raw digestate, the reduction of COD and P-PO3- in the distillate was 99.0% and 99.9%, respectively. Regardless feed temperature, the performance of the process was subjected to a significant decline of evaporation rate due to occurrence of membrane fouling; however, cycles of cleaning with citric acid allowed to partially regenerate the membrane by removing the reversible cake of foulants accumulated on the surface. The results demonstrate an adequate performance of MD process for recovering water and nutrients, leading to a dehydrated fraction of the digestate phase that can be easily stored and used in agronomic practices.

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