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A new side-looking at the dark fermentation of sugarcane vinasse: Improving the carboxylates production in mesophilic EGSB by selection of the hydraulic retention time and substrate concentration
Authors:Andressa Picionieri Bernal  Camila Aparecida de Menezes  Edson Luiz Silva
Affiliation:1. Department of Hydraulics and Sanitation, University of São Paulo, Av. Trabalhador Sãocarlense, 400, Centro, CEP 13566-590, São Carlos, SP, Brazil;2. Department of Chemical Engineering, Federal University of São Carlos, Rod. Washington Luis, Km 235, CEP 13565-905, São Carlos, SP, Brazil
Abstract:In recent years, a lot of scientific effort has been put into reusing the energy potential of sugarcane vinasse by dark fermentation. However, the findings so far indicate that new pathways need to be followed. In this context, this study assessed the effect of hydraulic retention time (HRT, from 24 to 1 h) on vinasse fermentation (10, 20, and 30 g COD L?1) in three mesophilic expanded granular sludge bed reactors (EGSB). The carbohydrate conversion remained above 60% at all organic loading rates applied. The maximum hydrogen production rate (8.77 L day?1 L?1) was obtained for 720 kg COD m?3 day?1 and associated to the lactate-acetate pathway. The highest productivities of propionic, acetic, and butyric acids were 3.11, 1.68, and 2.45 g L?1 h?1, respectively, at a HRT of 1 h. At this HRT, the degrees of acidification remained between 54% and 76% in all EGSB reactors. This research provides insights for carboxylate production from sugarcane vinasse and suggests applying the EGSB setup in the acidogenic stage of two-stage processes.
Keywords:Expanded granular sludge bed reactor  Sugarcane stillage  Volatile fatty acids  Acidogenic reactor  Degree of acidification  AFBR"  },{"  #name"  :"  keyword"  ,"  $"  :{"  id"  :"  kwrd0040"  },"  $$"  :[{"  #name"  :"  text"  ,"  _"  :"  anaerobic fluidized bed reactor  APBR"  },{"  #name"  :"  keyword"  ,"  $"  :{"  id"  :"  kwrd0050"  },"  $$"  :[{"  #name"  :"  text"  ,"  _"  :"  anaerobic packed bed reactor  AnSTBR"  },{"  #name"  :"  keyword"  ,"  $"  :{"  id"  :"  kwrd0060"  },"  $$"  :[{"  #name"  :"  text"  ,"  _"  :"  anaerobic structured bed reactors  COD"  },{"  #name"  :"  keyword"  ,"  $"  :{"  id"  :"  kwrd0070"  },"  $$"  :[{"  #name"  :"  text"  ,"  _"  :"  chemical oxygen demand  DOA"  },{"  #name"  :"  keyword"  ,"  $"  :{"  id"  :"  kwrd0080"  },"  $$"  :[{"  #name"  :"  text"  ,"  _"  :"  degree of acidification  EGSB"  },{"  #name"  :"  keyword"  ,"  $"  :{"  id"  :"  kwrd0090"  },"  $$"  :[{"  #name"  :"  text"  ,"  _"  :"  expanded granular sludge bed  hydrogen  HAc"  },{"  #name"  :"  keyword"  ,"  $"  :{"  id"  :"  kwrd0110"  },"  $$"  :[{"  #name"  :"  text"  ,"  _"  :"  acetic acid  HBu"  },{"  #name"  :"  keyword"  ,"  $"  :{"  id"  :"  kwrd0120"  },"  $$"  :[{"  #name"  :"  text"  ,"  _"  :"  butyric acid  HLa"  },{"  #name"  :"  keyword"  ,"  $"  :{"  id"  :"  kwrd0130"  },"  $$"  :[{"  #name"  :"  text"  ,"  _"  :"  lactic acid  HPR"  },{"  #name"  :"  keyword"  ,"  $"  :{"  id"  :"  kwrd0140"  },"  $$"  :[{"  #name"  :"  text"  ,"  _"  :"  hydrogen production rate  HPr"  },{"  #name"  :"  keyword"  ,"  $"  :{"  id"  :"  kwrd0150"  },"  $$"  :[{"  #name"  :"  text"  ,"  _"  :"  propionic acid  HRT"  },{"  #name"  :"  keyword"  ,"  $"  :{"  id"  :"  kwrd0160"  },"  $$"  :[{"  #name"  :"  text"  ,"  _"  :"  hydraulic retention time  HY"  },{"  #name"  :"  keyword"  ,"  $"  :{"  id"  :"  kwrd0170"  },"  $$"  :[{"  #name"  :"  text"  ,"  _"  :"  hydrogen yield  NaOH"  },{"  #name"  :"  keyword"  ,"  $"  :{"  id"  :"  kwrd0180"  },"  $$"  :[{"  #name"  :"  text"  ,"  _"  :"  sodium hydroxide  OLR"  },{"  #name"  :"  keyword"  ,"  $"  :{"  id"  :"  kwrd0190"  },"  $$"  :[{"  #name"  :"  text"  ,"  _"  :"  organic loading rate
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