TY - JOUR
T1 - Hythane production from brewery wastewater-generated biogas using a membrane electrochemical cell
AU - Rao, Yue
AU - He, Zhen
N1 - Publisher Copyright:
© 2025 Water Environment Federation.
PY - 2025/5
Y1 - 2025/5
N2 - Converting organic wastes into hythane, a blend of hydrogen (5% to 25%) and methane (75% to 95%), will not only reduce waste discharge but also maximize energy recovery. Herein, a membrane electrochemical cell was investigated to produce hythane from biogas generated in anaerobic digestion of brewery wastewater (BW). The key parameters including current densities, electrolyte concentrations, and biogas flow rates were examined in batch tests. Under an optimal condition (210 mA, 100 mM electrolyte, 1 mL min−1 of biogas flow), the system achieved the production of hythane containing 70.6% ± 1.1% CH4, 27.3% ± 0.5% H2, and 2.1% ± 1.6% CO2 (corresponding to 91.1% ± 6.4% CO2 removal). Meanwhile, the H2S concentration was decreased from 513 to 2 ppm, 99.9% ± 0.2% removal. Energy efficiency of this system was estimated 61.8% ± 10.7%, and energy output increased by 54.4% ± 10.6% with biogas upgrading to hythane. These results encourage further exploration of electrochemical approach for simultaneous biogas upgrading and hythane production. Practitioner Points: An innovative approach is demonstrated for efficient simultaneous biogas upgrading and electrochemical hythane production. Hythane composition is affected by the applied current and biogas flow rate. Biogas from brewery wastewater is converted into hythane with composition of 70.6% ± 1.1% CH4, 27.3% ± 0.5% H2, and 2.1% ± 1.6% of CO2. Electrochemical treatment achieves significant removal of H2S from the produced hythane.
AB - Converting organic wastes into hythane, a blend of hydrogen (5% to 25%) and methane (75% to 95%), will not only reduce waste discharge but also maximize energy recovery. Herein, a membrane electrochemical cell was investigated to produce hythane from biogas generated in anaerobic digestion of brewery wastewater (BW). The key parameters including current densities, electrolyte concentrations, and biogas flow rates were examined in batch tests. Under an optimal condition (210 mA, 100 mM electrolyte, 1 mL min−1 of biogas flow), the system achieved the production of hythane containing 70.6% ± 1.1% CH4, 27.3% ± 0.5% H2, and 2.1% ± 1.6% CO2 (corresponding to 91.1% ± 6.4% CO2 removal). Meanwhile, the H2S concentration was decreased from 513 to 2 ppm, 99.9% ± 0.2% removal. Energy efficiency of this system was estimated 61.8% ± 10.7%, and energy output increased by 54.4% ± 10.6% with biogas upgrading to hythane. These results encourage further exploration of electrochemical approach for simultaneous biogas upgrading and hythane production. Practitioner Points: An innovative approach is demonstrated for efficient simultaneous biogas upgrading and electrochemical hythane production. Hythane composition is affected by the applied current and biogas flow rate. Biogas from brewery wastewater is converted into hythane with composition of 70.6% ± 1.1% CH4, 27.3% ± 0.5% H2, and 2.1% ± 1.6% of CO2. Electrochemical treatment achieves significant removal of H2S from the produced hythane.
KW - anaerobic digestion
KW - biogas
KW - brewery wastewater
KW - electrochemical system
KW - hydrogen
UR - https://www.scopus.com/pages/publications/105006775393
U2 - 10.1002/wer.70098
DO - 10.1002/wer.70098
M3 - Article
C2 - 40420366
AN - SCOPUS:105006775393
SN - 1061-4303
VL - 97
JO - Water Environment Research
JF - Water Environment Research
IS - 5
M1 - e70098
ER -