Date of Award

10-28-2024

Publication Type

Thesis

Degree Name

M.A.Sc.

Department

Civil and Environmental Engineering

Keywords

Co-digestion;Methane Yield;Organic Waste;Raw Sludge;Reactors;Wet Cake

Supervisor

Rajesh Seth

Supervisor

Niharendu Biswas

Creative Commons License

Creative Commons Attribution 4.0 International License
This work is licensed under a Creative Commons Attribution 4.0 International License.

Abstract

Many waste types from various industries require proper treatment send disposal especially if they are organic and generated daily. Anaerobic digestion can degrade this waste to form biogas, a main component of natural gas. Waste-to-energy would also enable practical and sustainable uses of these materials to help reduce the energy crisis and emissions that increase global warming. Using industrial waste such as wet distillers’ grains (wet cake) is a great method for improving the results of the digestion of raw sludge. Co-digestion is also conducted to try and boost biogas production, particularly the methane yield and to mix wastes that may have been deemed unfeasible by themselves. This was observed from the biomethane potential (BMP) test conducted, which utilised different mix ratios for co-digesting wet cake and raw sludge. The test was conducted under mesophilic conditions at a food-to-micro-organism ratio of 0.5. Results showed that mono-digestion of wet cake had the highest bio-methane potential at 256 ± 2.1 NmL CH4/gCODadded (382 ± 3.2 NmL CH4/gVSadded), while raw sludge had the lowest at 94 ± 2.3 NmL CH4/gCODadded (154 ± 3.7 NmL CH4/gVSadded). The co-digested mixes fell within the range of results for wet cake and raw sludge. Statistically, the mix ratios were not significantly different from the expected experimental yield based on the sum of the individual wastes to conclude there was no synergistic or antagonistic effect. Two (2) Reactors (R1: wet cake + raw sludge and R2 wet cake only) were also operated semi-continuously for a hydraulic retention time of 20 days. Reactor 1 demonstrated stable operations at an organic loading rate of 3.82 g VS/L.day with approximate VS and TCOD removals of 59% and 54%, respectively, for 40 days, after which instability occurred shown by high VFA concentrations. Reactor 2 sustained stable operations at a loading of 2.81 g VS/L.day for 24 days with VS and TCOD removal of 73% and 61%, respectively, but showed instability immediately after an increase in loading to 3.97 g VS/L.day with high VFA concentrations. Further assessment of the effects of co-digestion is required to determine optimal conditions

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