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Exploring N-best solution space for heat integrated hydrogen regeneration network using sequential graph-theoretic approach
Affiliation:1. Research Centre for Sustainable Technologies, Faculty of Engineering, Computing and Science, Swinburne University of Technology, Jalan Simpang Tiga, 93350 Kuching, Sarawak, Malaysia;2. Department of Chemical and Biological Engineering, Monash University, Melbourne, VIC 3800, Australia;3. Integrated Engineering, Department of Environmental Science and Engineering, College of Engineering, Kyung Hee University, 1732 Deogyeong-daero, Giheung-gu, Yongin-Si, Gyeonggi-do 17104, Republic of Korea;4. Department of Computer Science and Systems Technology, University of Pannonia, 8200, Veszprém, Egyetem u. 10, Hungary;5. Széchenyi István University, 9026 Gy?r, Egyetem tér 1, Hungary
Abstract:To achieve the ever-stringent sustainable goals, this paper aims to synthesize a heat integrated hydrogen regeneration network (HIHRN) using a graph-theoretic-based sequential method. Firstly, the optimal and near-optimal structures for a hydrogen regeneration networks (HRN) are determined using P-graph model with consideration of both impurity and pressure constraints. These networks are then used as inputs in P-HENS software to generate a list of optimal and near-optimal heat exchanger network (HEN) structures. An eight source and sink problem is used to demonstrate the effectiveness of the proposed method. There are 199,677 feasible HIHRN structures identified, while the 6 near-optimal solutions which are within 0.05% tolerance of the optimal network cost (i.e., less than 33.04 M$/y) are presented together with the top four HEN designs that can offer comparable costs (~115,500 $/y). In addition, the impacts of pressure swing adsorber (PSA) pressure drop consideration and minimum temperature difference on the optimal design are also presented.
Keywords:Oil refinery  Hydrogen network  Heat integration  Process optimization  P-graph  P-HENS  ABB"  },{"  #name"  :"  keyword"  ,"  $"  :{"  id"  :"  pc_u2OPuz4P5Y"  },"  $$"  :[{"  #name"  :"  text"  ,"  _"  :"  Accelerated branch and bound  CCR"  },{"  #name"  :"  keyword"  ,"  $"  :{"  id"  :"  pc_DuxVZS9elE"  },"  $$"  :[{"  #name"  :"  text"  ,"  _"  :"  Continuous catalytic reformer  CHNT"  },{"  #name"  :"  keyword"  ,"  $"  :{"  id"  :"  pc_P7qRCP1eqp"  },"  $$"  :[{"  #name"  :"  text"  ,"  _"  :"  Cracked naptha hydrotreater  DHT"  },{"  #name"  :"  keyword"  ,"  $"  :{"  id"  :"  pc_NsTfDbo5o0"  },"  $$"  :[{"  #name"  :"  text"  ,"  _"  :"  Diesel hydrotreater  HC"  },{"  #name"  :"  keyword"  ,"  $"  :{"  id"  :"  pc_ydrHtGbw9b"  },"  $$"  :[{"  #name"  :"  text"  ,"  _"  :"  Hydrocracker  HEN"  },{"  #name"  :"  keyword"  ,"  $"  :{"  id"  :"  pc_onu1o46Fsg"  },"  $$"  :[{"  #name"  :"  text"  ,"  _"  :"  Heat exchanger network  HIHRN"  },{"  #name"  :"  keyword"  ,"  $"  :{"  id"  :"  pc_x4X6eCvAQl"  },"  $$"  :[{"  #name"  :"  text"  ,"  _"  :"  Heat integrated hydrogen regeneration network  HIWN"  },{"  #name"  :"  keyword"  ,"  $"  :{"  id"  :"  pc_7q49M3U3Yj"  },"  $$"  :[{"  #name"  :"  text"  ,"  _"  :"  Heat integrated water network  HIWRN"  },{"  #name"  :"  keyword"  ,"  $"  :{"  id"  :"  pc_PdTsFI4KB5"  },"  $$"  :[{"  #name"  :"  text"  ,"  _"  :"  Heat integrated water regeneration network  HN"  },{"  #name"  :"  keyword"  ,"  $"  :{"  id"  :"  pc_l9b2V6zVaS"  },"  $$"  :[{"  #name"  :"  text"  ,"  _"  :"  Hydrogen network  HNDAO"  },{"  #name"  :"  keyword"  ,"  $"  :{"  id"  :"  pc_dGXo4CRYC0"  },"  $$"  :[{"  #name"  :"  text"  ,"  _"  :"  Hydrogen network design and optimization  HNR"  },{"  #name"  :"  keyword"  ,"  $"  :{"  id"  :"  pc_vEIYUHdUob"  },"  $$"  :[{"  #name"  :"  text"  ,"  _"  :"  Hydrogen network retrofit  HRN"  },{"  #name"  :"  keyword"  ,"  $"  :{"  id"  :"  pc_HiaFOfXlI2"  },"  $$"  :[{"  #name"  :"  text"  ,"  _"  :"  Hydrogen regeneration network  IS4"  },{"  #name"  :"  keyword"  ,"  $"  :{"  id"  :"  pc_0NGDNYckua"  },"  $$"  :[{"  #name"  :"  text"  ,"  _"  :"  C4 Isomerization  JHT"  },{"  #name"  :"  keyword"  ,"  $"  :{"  id"  :"  pc_VBoZIEwCYl"  },"  $$"  :[{"  #name"  :"  text"  ,"  _"  :"  Jet fuel hydrotreater  LP"  },{"  #name"  :"  keyword"  ,"  $"  :{"  id"  :"  pc_xTl27LQ2Tx"  },"  $$"  :[{"  #name"  :"  text"  ,"  _"  :"  Linear programming  MP"  },{"  #name"  :"  keyword"  ,"  $"  :{"  id"  :"  pc_J5VnYSroMP"  },"  $$"  :[{"  #name"  :"  text"  ,"  _"  :"  Mathematical programming  MILP"  },{"  #name"  :"  keyword"  ,"  $"  :{"  id"  :"  pc_OKDLqIbRJq"  },"  $$"  :[{"  #name"  :"  text"  ,"  _"  :"  Multiple integer nonlinear programming  PI"  },{"  #name"  :"  keyword"  ,"  $"  :{"  id"  :"  pc_cXGLUCgSyL"  },"  $$"  :[{"  #name"  :"  text"  ,"  _"  :"  Process integration  PNS"  },{"  #name"  :"  keyword"  ,"  $"  :{"  id"  :"  pc_bzRLY1Jouc"  },"  $$"  :[{"  #name"  :"  text"  ,"  _"  :"  Process network synthesis  PSA"  },{"  #name"  :"  keyword"  ,"  $"  :{"  id"  :"  pc_xwGuma3Q2z"  },"  $$"  :[{"  #name"  :"  text"  ,"  _"  :"  Pressure swing adsorber  RCN"  },{"  #name"  :"  keyword"  ,"  $"  :{"  id"  :"  pc_Rx1swFEsgC"  },"  $$"  :[{"  #name"  :"  text"  ,"  _"  :"  Resource conservation network  TAC"  },{"  #name"  :"  keyword"  ,"  $"  :{"  id"  :"  pc_GAik8l1Yfa"  },"  $$"  :[{"  #name"  :"  text"  ,"  _"  :"  Total annual cost  WRN"  },{"  #name"  :"  keyword"  ,"  $"  :{"  id"  :"  pc_EyO3KQt53s"  },"  $$"  :[{"  #name"  :"  text"  ,"  _"  :"  Water regeneration network
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