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Controlling Ethanol Use in Chain Elongation by CO2 Loading Rate.
Roghair, Mark; Hoogstad, Tim; Strik, David P B T B; Plugge, Caroline M; Timmers, Peer H A; Weusthuis, Ruud A; Bruins, Marieke E; Buisman, Cees J N.
Afiliação
  • Roghair M; Sub-department of Environmental Technology, Wageningen University & Research , Bornse Weilanden 9, 6708 WG, Wageningen, The Netherlands.
  • Hoogstad T; Sub-department of Environmental Technology, Wageningen University & Research , Bornse Weilanden 9, 6708 WG, Wageningen, The Netherlands.
  • Strik DPBTB; Sub-department of Environmental Technology, Wageningen University & Research , Bornse Weilanden 9, 6708 WG, Wageningen, The Netherlands.
  • Plugge CM; Laboratory of Microbiology, Wageningen University & Research , Stippeneng 4, 6708 WE, Wageningen, The Netherlands.
  • Timmers PHA; Wetsus, European Centre of Excellence for Sustainable Water Technology , Oostergoweg 9, 8911 MA Leeuwarden, The Netherlands.
  • Weusthuis RA; Laboratory of Microbiology, Wageningen University & Research , Stippeneng 4, 6708 WE, Wageningen, The Netherlands.
  • Bruins ME; Wetsus, European Centre of Excellence for Sustainable Water Technology , Oostergoweg 9, 8911 MA Leeuwarden, The Netherlands.
  • Buisman CJN; Bioprocess Engineering, Wageningen University & Research , Droevendaalsesteeg 1, 6708 PB, Wageningen, The Netherlands.
Environ Sci Technol ; 52(3): 1496-1505, 2018 02 06.
Article em En | MEDLINE | ID: mdl-29304274
ABSTRACT
Chain elongation is an open-culture biotechnological process which converts volatile fatty acids (VFAs) into medium chain fatty acids (MCFAs) using ethanol and other reduced substrates. The objective of this study was to investigate the quantitative effect of CO2 loading rate on ethanol usages in a chain elongation process. We supplied different rates of CO2 to a continuously stirred anaerobic reactor, fed with ethanol and propionate. Ethanol was used to upgrade ethanol itself into caproate and to upgrade the supplied VFA (propionate) into heptanoate. A high CO2 loading rate (2.5 LCO2·L-1·d-1) stimulated excessive ethanol oxidation (EEO; up to 29%) which resulted in a high caproate production (10.8 g·L-1·d-1). A low CO2 loading rate (0.5 LCO2·L-1·d-1) reduced EEO (16%) and caproate production (2.9 g·L-1·d-1). Heptanoate production by VFA upgrading remained constant (∼1.8 g·L-1·d-1) at CO2 loading rates higher than or equal to 1 LCO2·L-1·d-1. CO2 was likely essential for growth of chain elongating microorganisms while it also stimulated syntrophic ethanol oxidation. A high CO2 loading rate must be selected to upgrade ethanol (e.g., from lignocellulosic bioethanol) into MCFAs whereas lower CO2 loading rates must be selected to upgrade VFAs (e.g., from acidified organic residues) into MCFAs while minimizing use of costly ethanol.
Assuntos

Texto completo: 1 Base de dados: MEDLINE Assunto principal: Dióxido de Carbono / Reatores Biológicos Idioma: En Ano de publicação: 2018 Tipo de documento: Article

Texto completo: 1 Base de dados: MEDLINE Assunto principal: Dióxido de Carbono / Reatores Biológicos Idioma: En Ano de publicação: 2018 Tipo de documento: Article