Bio-hydrogen production from waste fermentation: Mixing and static conditions

X Gómez, MJ Cuetos, JI Prieto, A Morán - Renewable Energy, 2009 - Elsevier
Renewable Energy, 2009Elsevier
One of the main disadvantages of the dark fermentation process is the cost associated with
the stages needed for obtaining H2 producing microorganisms. Using anaerobic microflora
in fermentation systems directly is an alternative which is gaining special interest when
considering the implementation of large-scale plants and the use of wastes as substrate
material. The performance of two H2 producing microflora obtained from different anaerobic
cultures was studied in this paper. Inoculum obtained from a waste sludge digester and from …
One of the main disadvantages of the dark fermentation process is the cost associated with the stages needed for obtaining H2 producing microorganisms. Using anaerobic microflora in fermentation systems directly is an alternative which is gaining special interest when considering the implementation of large-scale plants and the use of wastes as substrate material. The performance of two H2 producing microflora obtained from different anaerobic cultures was studied in this paper. Inoculum obtained from a waste sludge digester and from a laboratory digester treating slaughterhouse wastes were used to start up H2 fermentation systems. Inoculum acclimatized to slaughterhouse wastes gave better performance in terms of stability. However, due to the limited availability of this seed material, further work was performed to study the behaviour of the inoculum obtained from the municipal wastewater treatment plant. The process was evaluated under static and mixing conditions. It was found that application of a low organic loading rate favoured the performance of the fermentation systems, and that agitation of the reacting mass could alleviate unsteady performance. Specific H2 production obtained was in the range of 19–26L/kg SVfed with maximum peak production of 38–67L/kg SVfed. Although the performance of the systems was unsteady, recovery could be achieved by suspending the feeding process and controlling the pH in the range of 5.0–5.5. Testing the recovery capacity of the systems under temperature shocks resulted in total stoppage of H2 production.
Elsevier
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