Self-powered wastewater system recovers water and fertilizer using internal bioelectricity

By Newark Burstable Team
A new self-powered platform combining electrically assisted forward osmosis with a microbial desalination cell uses internally generated bioelectricity to recover water and struvite fertilizer from livestock wastewater, reducing reliance on external power.
Self-powered wastewater system recovers water and fertilizer using internal bioelectricity

A study published in Environmental Science and Ecotechnology reports a self-powered platform that integrates electrically assisted forward osmosis (eFO) with a microbial desalination cell (MDC) to recover water and nutrients from synthetic livestock wastewater. The system uses bioelectricity generated by wastewater-fed microbes to drive ion migration, promote struvite formation, increase water transport, and improve desalination, offering a path toward compact wastewater refineries that recover resources while reducing reliance on external electricity.

Conventional wastewater treatment has largely focused on pollutant removal, but growing water scarcity, energy constraints, and fertilizer demand are pushing the field toward resource recovery. Forward osmosis can draw water across a membrane with low hydraulic pressure, while bioelectrochemical systems such as MDCs can convert organic matter into electricity and help move salts. However, these tools are often run separately: FO systems face concentration polarization and reverse salt flux, and electrically assisted FO usually needs continuous external power. Based on these challenges, researchers from Temple University and New Jersey Institute of Technology developed an integrated eFO–MDC system that uses bioelectricity generated during organic matter oxidation to drive ion migration, recover struvite fertilizer, improve water flux, and enhance desalination.

In the eFO module, an osmotic gradient pulls water from the wastewater side toward a magnesium sulfate draw solution. When a mild electric field is applied, magnesium ions migrate back toward the wastewater side, where they react with ammonium and phosphate to precipitate as struvite, a slow-release fertilizer. In the MDC, electroactive microorganisms oxidize organic matter, generate electrons, and support desalination. The researchers harvested this microbial electricity, stored it in a 400-farad supercapacitor, regulated the voltage, and fed it back to the eFO unit. At bench scale, the MDC generated more than 7.0 milliwatts, while the eFO module consumed less than 1.0 milliwatt. Compared with the control, water flux rose by 57%, struvite recovery increased from 0.25 to 0.71 grams at 1.8 volts, and total desalination efficiency improved by 45%. At higher voltage, struvite recovery reached 1.03 grams at 3.8 volts. To guide operation, the team also developed a hybrid model combining mechanistic transport equations with a support vector machine (SVM), enabling prediction of struvite recovery, chemical oxygen demand (COD), conductivity, and power output across different operating conditions.

The authors said the study shows how wastewater treatment can be redesigned as a connected resource-recovery loop rather than a set of separate unit operations. The important step lay not only in coupling a membrane process with a bioelectrochemical process, but also in allowing the electricity generated by microorganisms to directly control ion movement and fertilizer formation. In their view, this internal feedback makes the approach more practical for nutrient-rich streams such as livestock wastewater, where water recovery, salinity control, and phosphorus recovery can all create value.

The results point to applications in decentralized wastewater treatment, agricultural waste management, and future resource-recovery facilities. The paper also makes clear that scale-up will require engineering work: the MDC produced enough power for the eFO module, but hydraulic retention times, module sizing, struvite harvesting, membrane scaling, and electrode durability still need optimization. A techno-economic assessment estimated a bench-scale net treatment cost of 10.2 United States dollars per cubic meter, falling to 3.3 United States dollars per cubic meter in an engineering scale-up scenario. The study was partially supported by the U.S. Bureau of Reclamation (Award#: 13761566 and R22AC00433) and the NSF/BSF project (Award#: 2215387). Publication of this article was funded in part by the Temple University Libraries Open Access Publishing Fund.

Newark Burstable Team

Newark Burstable Team

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