For each of the duplicate tests, a subsample of bioreactor biomass (250 mL) was transferred anaerobically to a 330 mL glass vessel. The biomass was flushed with a mixed gas (90% CH4, 5% CO2, and 5% N2) for 10 min. Approiximately 10 mL 13C-labelled methane (Sigma-Aldrich, 99 atom % 13C, USA) and ~0.03 g 57Fe-labelled ferrihydrite were added to each vessel on Day 34. Each vessel was pressurised to 1.2 atm through injecting helium. Each test lasted for ~110 days.
During the tests, Fe(III) and Fe(II) in liquid and solid phases were sampled every 3–7 days and measured for their 57Fe(III)/56Fe(III), 54Fe(III)/56Fe(III), 57Fe(II)/56Fe(II) and 54Fe(II)/56Fe(II) ratios. After the 57Fe(III)/56Fe(III) ratio reached a steady state (Supplementary Figure 2), methane in gas phase, CO2 in gas, liquid and solid phases, Fe(III)/Fe(II) in liquid and solid phases were sampled every week and measured for their concentrations and the respective isotopic fractions.
Total methane, Fe(III) and Fe(II) and their consumption/production rates were calculated as described in section “mass- and electron balance tests”. Total CO2 was quantified by considering the amounts in gas, liquid and solid phases, and the profile of CO2 was used to determine its production rate (rCO2) via linear regression. The amounts of methane, CO2, Fe(III) and Fe(II) and their respective isotopic fractions were used to calculate the amounts of 13CH4, 13CO2, 57Fe(III), and 57Fe(II). The profiles of 13CH4, 13CO2, 57Fe(III) and 57Fe(II) were used to determine the consumption rates of 13CH4 (r13CH4) and 57Fe(III) (r57Fe(III)), and the production rates of 13CO2 (r13CO2) and 57Fe(II) (r57Fe(II)) via linear regression.
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