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Biomass gasification coupled with producer gas cleaning,bottling and HTS catalyst treatment for H2-rich gas production
Affiliation:1. Tokyo University of Agriculture and Technology, Naka-cho 2-24-16, Koganei-shi, Tokyo, Japan;2. School of Engineering, The University of Tokyo, Hongo, Tokyo, 113-8656, Japan;3. Institute of Industrial Science, The University of Tokyo, 4-6-1, Komaba, Meguro-ku, Tokyo, 153-8505, Japan;1. School of Environmental and Safety Engineering, North University of China, People''s Republic of China;2. School of Chemical Engineering and Technology, North University of China, Taiyuan 030051, People''s Republic of China;1. School of Chemistry and Chemical Engineering, South China University of Technology; Guangdong Key Lab for Fuel Cell Technology, Guangzhou 510641, China;2. School of Materials Science and Engineering, Georgia Institute of Technology, 771 Ferst Drive, Atlanta, GA 30332-0245, United States;1. State Key Laboratory of Petroleum Resources and Prospecting, China University of Petroleum at Beijing, Changping, 100249, China;2. The University of Texas at Austin, Austin, TX, 78712, USA;1. Department of Chemical Engineering, Indian Institute of Technology Hyderabad, Kandi, Sangareddy, 502285, Telangana, India;2. Department of Chemistry, Indian Institute of Technology Hyderabad, Kandi, Sangareddy, 502285, Telangana, India
Abstract:The aim of the present study is to demonstrate the production of hydrogen-rich fuel gas from J. curcas residue cake. A comprehensive experimental study for the production of hydrogen rich fuel gas from J. curcas residue cake via downdraft gasification followed by high temperature water gas shift catalytic treatment has been carried out. The gasification experiments are performed at different equivalence ratios and performance of the process is reported in terms of producer gas composition & its calorific value, gas production rate and cold gas efficiency. The producer gas is cleaned of tar and particulate matters by passing it through venturi scrubber followed by sand bed filter. The clean producer gas is then compressed at 0.6 MPa and bottled into a gas cylinder. The bottled producer gas and a simulated mixture of producer gas are then subjected to high temperature shift (HTS) catalytic treatment for hydrogen enriched gas production. The effect of three different operating parameters GHSV, steam to CO ratio and reactor temperature on the product gas composition and CO conversion is reported. From the experimental study it is found that, the presence of oxygen in the bottled producer gas has affected the catalyst activity. Moreover, higher concentration of oxygen concentration in the bottled producer gas leads to the instantaneous deactivation of the HTS catalyst.
Keywords:Biomass gasification  Equivalence ratio  Hydrogen  High temperature shift catalyst  Gas hourly space velocity  ER"  },{"  #name"  :"  keyword"  ,"  $"  :{"  id"  :"  kwrd0040"  },"  $$"  :[{"  #name"  :"  text"  ,"  _"  :"  Equivalence ratio  GC"  },{"  #name"  :"  keyword"  ,"  $"  :{"  id"  :"  kwrd0050"  },"  $$"  :[{"  #name"  :"  text"  ,"  _"  :"  Gas chromatograph  TCD"  },{"  #name"  :"  keyword"  ,"  $"  :{"  id"  :"  kwrd0060"  },"  $$"  :[{"  #name"  :"  text"  ,"  _"  :"  Thermal conductivity detector  TGA"  },{"  #name"  :"  keyword"  ,"  $"  :{"  id"  :"  kwrd0070"  },"  $$"  :[{"  #name"  :"  text"  ,"  _"  :"  Thermo-gravimetric analyzer  DTA"  },{"  #name"  :"  keyword"  ,"  $"  :{"  id"  :"  kwrd0080"  },"  $$"  :[{"  #name"  :"  text"  ,"  _"  :"  Differential temperature analyzer  XRD"  },{"  #name"  :"  keyword"  ,"  $"  :{"  id"  :"  kwrd0090"  },"  $$"  :[{"  #name"  :"  text"  ,"  _"  :"  X-ray Diffraction  FE-SEM"  },{"  #name"  :"  keyword"  ,"  $"  :{"  id"  :"  kwrd0100"  },"  $$"  :[{"  #name"  :"  text"  ,"  _"  :"  Field emission scanning electron micrograph  A/F"  },{"  #name"  :"  keyword"  ,"  $"  :{"  id"  :"  kwrd0110"  },"  $$"  :[{"  #name"  :"  text"  ,"  _"  :"  Air to fuel ratio  HHV"  },{"  #name"  :"  keyword"  ,"  $"  :{"  id"  :"  kwrd0120"  },"  $$"  :[{"  #name"  :"  text"  ,"  _"  :"  Higher heating value  LHV"  },{"  #name"  :"  keyword"  ,"  $"  :{"  id"  :"  kwrd0130"  },"  $$"  :[{"  #name"  :"  text"  ,"  _"  :"  Lower heating value  CV"  },{"  #name"  :"  keyword"  ,"  $"  :{"  id"  :"  kwrd0140"  },"  $$"  :[{"  #name"  :"  text"  ,"  _"  :"  Calorific value  CGE"  },{"  #name"  :"  keyword"  ,"  $"  :{"  id"  :"  kwrd0150"  },"  $$"  :[{"  #name"  :"  text"  ,"  _"  :"  Cold gas efficiency  CCE"  },{"  #name"  :"  keyword"  ,"  $"  :{"  id"  :"  kwrd0160"  },"  $$"  :[{"  #name"  :"  text"  ,"  _"  :"  Carbon conversion efficiency  V/v"  },{"  #name"  :"  keyword"  ,"  $"  :{"  id"  :"  kwrd0170"  },"  $$"  :[{"  #name"  :"  text"  ,"  _"  :"  volume to volume ratio  WGS"  },{"  #name"  :"  keyword"  ,"  $"  :{"  id"  :"  kwrd0180"  },"  $$"  :[{"  #name"  :"  text"  ,"  _"  :"  Water gas shift  MFC"  },{"  #name"  :"  keyword"  ,"  $"  :{"  id"  :"  kwrd0190"  },"  $$"  :[{"  #name"  :"  text"  ,"  _"  :"  Mass flow controller  HPLC"  },{"  #name"  :"  keyword"  ,"  $"  :{"  id"  :"  kwrd0200"  },"  $$"  :[{"  #name"  :"  text"  ,"  _"  :"  High performance liquid chromatography  GLS"  },{"  #name"  :"  keyword"  ,"  $"  :{"  id"  :"  kwrd0210"  },"  $$"  :[{"  #name"  :"  text"  ,"  _"  :"  Gas liquid separator  HTS"  },{"  #name"  :"  keyword"  ,"  $"  :{"  id"  :"  kwrd0220"  },"  $$"  :[{"  #name"  :"  text"  ,"  _"  :"  High temperature shift  S/CO"  },{"  #name"  :"  keyword"  ,"  $"  :{"  id"  :"  kwrd0230"  },"  $$"  :[{"  #name"  :"  text"  ,"  _"  :"  Steam to CO ratio  GHSV"  },{"  #name"  :"  keyword"  ,"  $"  :{"  id"  :"  kwrd0240"  },"  $$"  :[{"  #name"  :"  text"  ,"  _"  :"  Gas hourly space velocity
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