Production of biohydrogen from waste wheat in continuously operated UPBR: The effect of influent substrate concentration


Gorgec F. K., KARAPINAR İ.

INTERNATIONAL JOURNAL OF HYDROGEN ENERGY, cilt.44, sa.32, ss.17323-17333, 2019 (SCI-Expanded) identifier identifier

  • Yayın Türü: Makale / Tam Makale
  • Cilt numarası: 44 Sayı: 32
  • Basım Tarihi: 2019
  • Doi Numarası: 10.1016/j.ijhydene.2018.12.213
  • Dergi Adı: INTERNATIONAL JOURNAL OF HYDROGEN ENERGY
  • Derginin Tarandığı İndeksler: Science Citation Index Expanded (SCI-EXPANDED), Scopus
  • Sayfa Sayıları: ss.17323-17333
  • Anahtar Kelimeler: Biohydrogen, Hydrolyzed wheat, Dark fermentation, Continuous, Influent substrate concentration, Packed bed, BIO-HYDROGEN PRODUCTION, PACKED-BED REACTOR, PRODUCTION PERFORMANCE, IMMOBILIZED CELLS, SLUDGE SYSTEMS, FLUIDIZED-BED, GROUND WHEAT, DARK, FERMENTATION, STARCH
  • Dokuz Eylül Üniversitesi Adresli: Evet

Özet

Utilization of waste materials is one of the most economical approaches to biohydrogen production. Continuous generation of biohydrogen in a bioreactor makes the process more economical with respect to the conventional physical and chemical method. The two main parameters that affect the biohydrogen production in a continuously operated bioreactor are hydraulic retention time (HRT) and influent substrate concentrations. The effect of influent substrate concentration on biohydrogen generation in an up-flow packed bed reactor (UPBR) at HRT = 3 h was investigated in this study. The substrate was waste wheat which was acid hydrolyzed in H2SO4 by adjusting the pH value to pH = 2, under high temperature as T = 90 degrees C in an autoclave to obtain fermentable sugar solution. A natural and porous support particle namely, aquarium biological sponge (ABS) was the microbial immobilization surface in the reactor. Total and hydrogen gas volumes, hydrogen percentage, influent and effluent substrate concentrations, VFA concentrations were monitored. The influent substrate concentration (TSO) was varied between TSO = 10 g/L and TSO = 35 g/L. The process performance was evaluated as biohydrogen volume, percentages, rate and yield under varying operating conditions. The production volume (4275 ml/day) and the rate (3.05 L H-2/L day) were maximum at influent sugar concentration of TSO = 25 g/L, but the yield reached to its maximum value as Y = 1.22 mol H-2/mol glucose at TSO = 19 g/L. Substrate limitation and inhibitions were observed at influent concentrations of TSO = 10 g/L and TSO = 35 g/L, respectively. The results indicated that ABS could be suggested as a microbial support particle for hydrogen generation in immobilized systems. (C) 2019 Hydrogen Energy Publications LLC. Published by Elsevier Ltd. All rights reserved.