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Supercritical water gasification of timothy grass as an energy crop in the presence of alkali carbonate and hydroxide catalysts
Affiliation:1. Department of Energy Engineering, Science and Research Branch, Islamic Azad University, Tehran, Iran;2. School of Chemistry, College of science, University of Tehran, Tehran, Iran
Abstract:
This study is focused on identifying the candidature of timothy grass as an energy crop for hydrogen-rich syngas production through supercritical water gasification. Timothy grass was gasified in supercritical water to investigate the impacts of temperature (450–650 °C), biomass-to-water ratio (1:4 and 1:8) and reaction time (15–45 min) in the pressure range of 23–25 MPa. The impacts of carbonate catalysts (e.g., Na2CO3 and K2CO3) and hydroxide catalysts (e.g., NaOH and KOH) at variable mass fractions (1–3%) were examined to maximize hydrogen yields. In the non-catalytic gasification of timothy grass, highest hydrogen (5.15 mol kg−1) and total gas yields (17.2 mol kg−1) with greater carbon gasification efficiency (33%) and lower heating value (2.21 MJ m−3) of the gas products were obtained at 650 °C with 1:8 biomass-to-water ratio for 45 min. However, KOH at 3% mass fraction maximized hydrogen and total gas yields up to 8.91 and 30.6 mol kg−1, respectively. Nevertheless, NaOH demonstrated highest carbon gasification efficiency (61.3%) and enhanced lower heating value of the gas products (4.68 MJ m−3). Timothy grass biochars were characterized through Fourier transform infrared spectroscopy, Raman spectroscopy and scanning electron microscopy to understand the behavior of the feedstock to rising temperature and reaction time. The overall findings suggest that timothy grass is a promising feedstock for hydrogen production via supercritical water gasification.
Keywords:Hydrogen  Supercritical water gasification  Temperature  Feed concentration  Reaction time  BTW"  },{"  #name"  :"  keyword"  ,"  $"  :{"  id"  :"  kwrd0045"  },"  $$"  :[{"  #name"  :"  text"  ,"  _"  :"  Biomass-to-water  CGE"  },{"  #name"  :"  keyword"  ,"  $"  :{"  id"  :"  kwrd0055"  },"  $$"  :[{"  #name"  :"  text"  ,"  _"  :"  Carbon gasification efficiency  FTIR"  },{"  #name"  :"  keyword"  ,"  $"  :{"  id"  :"  kwrd0065"  },"  $$"  :[{"  #name"  :"  text"  ,"  _"  :"  Fourier transform infrared  GC"  },{"  #name"  :"  keyword"  ,"  $"  :{"  id"  :"  kwrd0075"  },"  $$"  :[{"  #name"  :"  text"  ,"  _"  :"  Gas chromatography  HHV"  },{"  #name"  :"  keyword"  ,"  $"  :{"  id"  :"  kwrd0085"  },"  $$"  :[{"  #name"  :"  text"  ,"  _"  :"  Higher heating value  LHV"  },{"  #name"  :"  keyword"  ,"  $"  :{"  id"  :"  kwrd0095"  },"  $$"  :[{"  #name"  :"  text"  ,"  _"  :"  Lower heating value  SEM"  },{"  #name"  :"  keyword"  ,"  $"  :{"  id"  :"  kwrd0105"  },"  $$"  :[{"  #name"  :"  text"  ,"  _"  :"  Scanning electron microscopy  SCW"  },{"  #name"  :"  keyword"  ,"  $"  :{"  id"  :"  kwrd0115"  },"  $$"  :[{"  #name"  :"  text"  ,"  _"  :"  Supercritical water  SCWG"  },{"  #name"  :"  keyword"  ,"  $"  :{"  id"  :"  kwrd0125"  },"  $$"  :[{"  #name"  :"  text"  ,"  _"  :"  Supercritical water gasification  WGS"  },{"  #name"  :"  keyword"  ,"  $"  :{"  id"  :"  kwrd0135"  },"  $$"  :[{"  #name"  :"  text"  ,"  _"  :"  Water-gas shift
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