Abstract

The production of hydrogen from food wastes was studied in a two‐stage (dark fermentation‐digestion) process under mesophilic conditions. The effect of a recycling stream, from the methanogenic phase to the fermentation phase, over H2 production and alkali consumption was evaluated in a semicontinuous fermentation process. The cases of no‐recycling, direct recycling, and membrane permeate recycling of methanogenic supernatant (using an ultrafiltration and nanofiltration membrane) were evaluated.Adding a recycling stream from a methanogenic reactor to the hydrogen‐producing reactor significantly reduced the need of external alkali addition for pH control, up to 52%. The performance of the hydrogen‐producing reactors receiving the recycling stream was similar in all cases tested, with values of specific hydrogen production of about 30 mL g−1 VSadded. This value was also similar to that one obtained from the no‐recycling configuration. The use of a membrane pretreatment stage proved to be not necessary. Operating conditions established in the fermentation stage were enough to avoid any detrimental effect associated to methanogenic microflora predominance. © 2014 American Institute of Chemical Engineers Environ Prog, 34: 227–233, 2015

Full Text
Paper version not known

Talk to us

Join us for a 30 min session where you can share your feedback and ask us any queries you have

Schedule a call

Disclaimer: All third-party content on this website/platform is and will remain the property of their respective owners and is provided on "as is" basis without any warranties, express or implied. Use of third-party content does not indicate any affiliation, sponsorship with or endorsement by them. Any references to third-party content is to identify the corresponding services and shall be considered fair use under The CopyrightLaw.