Anaerobic co-digestion of glycerol waste and distillery wastewater for bio-hythane production: Performance and ADM-1 based kinetics

• Anaerobic co-digestion of glycerol and distilled wastewater contributes synergisms. • Rather high BHP (147 mL/g-VS) and BMP (650 mL/g-VS) were achieved • Valuable bio-hythane could be feasibly recovered from CSTR-UASB reactor in series. • High energy of 106 kWh/m 3 -substrate is obtained from this continuous two-stage process. • Kinetic model developed can describe this two-stage co-digestion process. Glycerol waste (GW), with its high carbon content, was co-digested with nitrogen-rich distillery wastewater (DW) in this experiment to evaluate hydrogen and methane production in a two-stage anaerobic digestion (AD) system. Bio-hydrogen potential (BHP) and methane potential (BMP) were conducted under thermophilic conditions (55°C) for the co-digestion of GW and acetone-butanol-ethanol distillery wastewater (ABE-DW) at various mixing ratios of 0:100, 20:80, 40:60, 50:50, 60:40, 80:20, and 100:0 (%VS) to determine the optimal mixing ratio. The highest BHP of 147 mL-H 2 /g-VS and BMP of 650 mL-CH 4 /g-VS were achieved at a GW to ABE-DW mixing ratio 50:50. Then. the process proceded with the continuous two-stage anaerobic process which was later implemented with the continuously stirred tank reactor (CSTR) for hydrogen production and the up-flow anaerobic sludge blanket (UASB) reactor for methane production in order to assess system performance. A mixture of GW and DW from commercial ethanol production (ethanol-DW) at a 50:50 mixing ratio was fed into the CSTR at a 4-day HRT, and the CSTR effluent was subsequently fed into the UASB at 21-day and 18-day HRTs. The CSTR achieved a hydrogen yield of 83.6 mL-H 2 /g-VS, while methane yields in the UASB were 367 mL-CH 4 /g-VS at a 21-day HRT and 440 mL-CH 4 /g-VS at an 18-day HRT. Additionally, the original ADM-1 was modified to describe the two-stage anaerobic co-digestion of GW and DW. This enhanced model effectively predicts the performance of the two-stage anaerobic process for co-digesting GW and DW.

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Publication Details

Journal
Carbon Resources Conversion
Published
2025-03-07
DOI
https://doi.org/10.1016/j.crcon.2025.100311
Citations
5
Primary Topic
Anaerobic Digestion and Biogas Production
Type
article
Field-Weighted Citation Impact
5.03

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article

Anaerobic co-digestion of glycerol waste and distillery wastewater for bio-hythane production: Performance and ADM-1 based kinetics

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5 citations
Carbon Resources Conversion
Anaerobic Digestion and Biogas Production
5.03
article

Anaerobic co-digestion of glycerol waste and distillery wastewater for bio-hythane production: Performance and ADM-1 based kinetics

Rattana Jariyaboon, Prawit Kongjan, Khaliyah Sani, Hidenari Yasui, Sompong O‐Thong, Alissara Reungsang
article en
5 citations

Abstract

• Anaerobic co-digestion of glycerol and distilled wastewater contributes synergisms. • Rather high BHP (147 mL/g-VS) and BMP (650 mL/g-VS) were achieved • Valuable bio-hythane could be feasibly recovered from CSTR-UASB reactor in series. • High energy of 106 kWh/m 3 -substrate is obtained from this continuous two-stage process. • Kinetic model developed can describe this two-stage co-digestion process. Glycerol waste (GW), with its high carbon content, was co-digested with nitrogen-rich distillery wastewater (DW) in this experiment to evaluate hydrogen and methane production in a two-stage anaerobic digestion (AD) system. Bio-hydrogen potential (BHP) and methane potential (BMP) were conducted under thermophilic conditions (55°C) for the co-digestion of GW and acetone-butanol-ethanol distillery wastewater (ABE-DW) at various mixing ratios of 0:100, 20:80, 40:60, 50:50, 60:40, 80:20, and 100:0 (%VS) to determine the optimal mixing ratio. The highest BHP of 147 mL-H 2 /g-VS and BMP of 650 mL-CH 4 /g-VS were achieved at a GW to ABE-DW mixing ratio 50:50. Then. the process proceded with the continuous two-stage anaerobic process which was later implemented with the continuously stirred tank reactor (CSTR) for hydrogen production and the up-flow anaerobic sludge blanket (UASB) reactor for methane production in order to assess system performance. A mixture of GW and DW from commercial ethanol production (ethanol-DW) at a 50:50 mixing ratio was fed into the CSTR at a 4-day HRT, and the CSTR effluent was subsequently fed into the UASB at 21-day and 18-day HRTs. The CSTR achieved a hydrogen yield of 83.6 mL-H 2 /g-VS, while methane yields in the UASB were 367 mL-CH 4 /g-VS at a 21-day HRT and 440 mL-CH 4 /g-VS at an 18-day HRT. Additionally, the original ADM-1 was modified to describe the two-stage anaerobic co-digestion of GW and DW. This enhanced model effectively predicts the performance of the two-stage anaerobic process for co-digesting GW and DW.

Carbon Resources ConversionVol. 8(3)
Prince of Songkla University (TH), The University of Kitakyushu (JP), Khon Kaen University (TH), Mahidol University (TH)
Prince of Songkla University, National Research Council of Thailand, Thailand Science Research and Innovation
Clean water and sanitation
Openalex Percentile: Top 6%
Anaerobic Digestion and Biogas Production
5.03
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