Table 1.
MFC | COD removal efficiencya (%) | Total concentration of organic acidsb (mM) | J csc (mA m−2) | P dmax (mW m−2) | C.E. e (%) |
---|---|---|---|---|---|
pH 7.0 | 57.8 ± 8.82 | 0.47 | 410 ± 176 | 381 ± 155 | 34.0 ± 9.18 |
pH 5.5 | 57.1 ± 12.8 | 1.19 | 253 ± 52.1 | 147 ± 18.3 | 12.1 ± 3.11 |
pH 4.0 | 56.9 ± 3.61 | 1.80 | 40.7 ± 14.6 | 5.14 ± 1.64 | 1.06 ± 1.43 |
aChemical oxygen demand (COD) removal efficiency (%) was calculated as follows: 100 × [COD concentration in synthetic wastewater (mg-COD L−1)–COD concentration in broth (mg-COD L−1)]/COD concentration in synthetic wastewater (mg-COD L−1)
bSum of the organic acid concentrations in the suspended fractions of samples collected after 30 days’ operation at pH 7.0, pH 5.5, or pH 4.0
cShort-circuit current density [J sc (mA m−2)] was determined from the power density curves
dMaximum power density [P max (mW m−2)] was obtained from the peak in the power density curves
eCoulombic efficiency (C.E.) was calculated based on the COD removal (CODin–CODout) and the measured current, using 1 g of COD = 0.125 mol of electrons, and 1 A = 5.39 × 1023 electrons per day