A pilot scale reactor for bio-hydrogen production

  • Aron Scaletta, BioEnergy Lab, ENVIRONMENT PARK S.p.A., Italy
  • Dott Barbara La Licata, BioEnergy Lab, ENVIRONMENT PARK S.p.A., Italy
  • Ing Fabio Sagnelli, BioEnergy Lab, ENVIRONMENT PARK S.p.A., Italy
  • Ing Alexia Boulanger, BioEnergy Lab, ENVIRONMENT PARK S.p.A., France
  • Ing PhD Paola Zitella, BioEnergy Lab, ENVIRONMENT PARK S.p.A., Italy
  • Prof Bernardo Ruggeri, BioEnergy Lab, ENVIRONMENT PARK S.p.A., Italy
  • The objective of this study is to investigate dark anaerobic fermentation as a suitable technology for producing hydrogen. Tests were run at two different initial sucrose concentrations (50 and 100g/l) in a pilot scale reactor under batch conditions. The digester consists of a vessel connected to a gas collection system and equipped with a stirrer (max. speed 30rpm) and a pH and temperature control system. Gas produced could be monitored thanks to a gas counter, while the composition could be analyzed through a gas-cromatograph. Temperature, pH and ORP could also be registered via PLC. Anaerobic digested sludge, pre-treated for 24h at pH=3 to inhibit methanogenic bacteria, was used as inoculum, and then fed with a medium containing the sucrose solution, salts and micronutrients. Chemical and biological analysis were performed at different times on samples for the determination of sucrose and biomass concentration, ATP and VFAs. No pH and temperature regulation occurred during fermentation, so pH decreased constantly, while temperature remained at 20°C. In terms of gas produced, the best results were observed at 100g/l of sucrose with 23l of hydrogen produced against 4l at 50g/l. In fact sucrose was mainly consumed at 100g/l with a conversion of 44%, instead of 25%. However for both experiments yield remained at 0.20÷0.32 mol H2/mol sucrose, because of low temperatures and development of a mixed culture. A kinetic approach was proposed for future experiments under continuous conditions, suggesting that inlet sucrose concentration should vary in a range of 60÷70g/l for maximizing hydrogen production.

    Sucrose at 50 g/l Sucrose at 100g/l
    Total gas (l) % % H2 % CO2 Sucrose (g/l) Total gas (l) % H2 % CO2 Sucrose (g/l)
    t = 0h - - - 45 - - - 90
    t = 24h - - - 42 - - - 74
    t = 42h 4.8 9 91 36 3.6 15 85 53
    t = 47h 7.5 13 87 34 4.8 17 83 51
    t = 64h 16.1 23 77 34 18.4 28 72 51
    t =72h 19.3 30 70 34 36.3 40 60 51
    t = 100h 20.4 40 60 34 66.9 46 54 51