The suitability of fermenter liquor from MSW as an electron donor for hypersaline sulfate reduction
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Updated: Jan 8, 2026

Development of Sulfidogenic Sludge from Marine Sediments and Trichloroethylene Reduction in an Upflow Anaerobic Sludge Blanket Reactor
Published on: October 15, 2015
M Patel1, M Peces2, D Villa-Gomez1
1School of Civil Engineering, The University of Queensland, St Lucia 4072, Australia.
Abstract:
Liquor from the fermentation of the organic fraction of municipal solid waste (OFMSW) was tested as a carbon source for sulfate reducing organisms under saline to hypersaline conditions for treating acid mine drainage in arid climates. Two 1.4 L reactors were operated continuously, one as a control maintained at a salinity of 20 g NaCl/L, the other (the test reactor) operated at salinities up to 50 g NaCl/L. Both reactors were first fed a synthetic mix of VFAs (acetate, propionate, butyrate, and valerate) at a COD ratio of 2:1:3:0.5 and at an organic loading rate of 1.56 gCOD/L/d with sulfate supplied in excess as Na2SO4. The sulfate reduction rate (SRR) was unaffected by the salinity up to 35 g NaCl/L, but was adversely affected in hypersaline (>35 g NaCl/L) conditions. The stabilized SRR at 50 g NaCl/L was 0.43 ± 0.01 g SO4-S/L/d compared to 0.66 ± 0.01 g SO4-S/L/d in the control reactor. Upon replacing the VFA mixture in both reactors with fermenter liquor (a mixture of alcohols, VFAs, lactate and succinate and 29 ± 4 % of unidentified COD), at the same COD loading rate, the SRR recovered in the test reactor (50 g NaCl/L) to 0.56 ± 0.01 g SO4-S/L/d with full utilisation of acetate by completely oxidizing sulfate reducers, no methane production and over 65 % utilisation of the un-identified COD fraction.

