Then, the MXC was operated in continuous mode. Acetate medium or domestic wastewater (filtered and raw) was fed find more to the MXC at a flow rate of 37.5 mL/h using a cartridge-type peristaltic pump (Master Flex® L/S digital drive, Model 7523-80, Cole-Parmer,

Canada) to maintain hydraulic residence time (HRT) of 8 h in the anode chamber. MXC performance and effluent quality were evaluated with different feed conditions at a fixed HRT of 8 h. First, buffer concentration effect was assessed with acetate medium (2.7 ± 0.2 mM, 175 ± 10 mg COD/L) amended with 50 mM or 5 mM bicarbonate buffer (Run 1 and 2). Then, wastewater biodegradability against acetate medium was investigated at Run 3. To avoid particulate (i.e., SS) effects on current generation and exclusively assess the biodegradability of the wastewater against acetate, the wastewater was filtered and fed to the MXC. Particulates were separated from the wastewater in two filtration steps using glass fiber filters (Fisherbrand glass Dabrafenib research buy fiber filter, 1.6 μm, G6, Cat. No. 09-804-55 A) and glass microfiber filters (Whatmann microfiber filter, 1.2 μm, GF/C, Cat. No. 1822-070). The average soluble COD (SCOD) for the domestic wastewater was close to the COD concentration of the acetate medium. Table 1 summarizes the

characteristics of the domestic wastewater. At Run 4, buffer effect on current density was re-assessed in the MXC fed with the filtered wastewater having

50 mM bicarbonate buffer. At Run 5, the MXC was operated with the acetate medium having 5 mM bicarbonate buffer to recover current density. After that, SS collected from the wastewater were added to the acetate medium at Run 6. To collect SS, the domestic wastewater was centrifuged at 5000 rpm for 15 min with a centrifuge (Beckman TJ-6 Tabletop Centrifuge, Beckman Coulter Inc. CA, USA). The SS was added to the acetate medium (L) having 230 ± 28 mg SS/L, which is close to SS concentration in the wastewater (see Table 1). At Run 7, the domestic Neratinib chemical structure wastewater was directly used as substrate for the MXC. A feed tank was continuously mixed with a magnetic stirrer (Model VS-C4, VWR International Inc., Canada) at 200 rpm to avoid sedimentation of SS for Run 6 and 7. Data was collected after current density reached at steady state in each condition. Table 2 summarizes different feed conditions. For estimation of pseudo, apparent Ks (mg COD/L) for the MXC, acetate concentration in the medium was varied from 1 to 425 mg COD/L. The response of current density at different SCOD concentrations was recorded. Then, the best-fit apparent Ks value was estimated with Eq. (1) and the relative least squares method [17] using MS 2007 excel solver. The best-fit Ks value was used to simulate current density in response to acetate concentration using Eq. (1), which can validate the apparent Ks for current density in the MXC.