Simultaneous synthesis of utility system and heat exchanger network incorporating steam condensate and boiler feedwater

A heat exchanger network (HEN) is an important part in processing plants used to recover heat from process streams. A utility system supplies heating and cooling utilities and introduces additional hot and cold streams for the processes. The HEN and utility system (e.g., Rankine cycle-based cogeneration system) are closely interconnected primarily through steam, steam condensate leaving the turbines, and process surplus heat. The recovery of the sensible heat from the steam condensate and process surplus heat through an integration technique may contribute significantly to the reduction of the heating and cooling utility consumption in the heat exchanger network as well as in the primary energy consumption in the utility system. In this paper, a systematic methodology for the simultaneous synthesis and design of a utility system and HEN is proposed. The heat recovery from the steam condensate and boiler feedwater preheating are integrated into the HEN synthesis together with the design optimization of a Rankine cycle-based utility system. In addition to the simultaneous design of the utility and heat-recovery systems, the optimization variables include the steam condensate target temperature, the steam level for process heating, the energy demand for the utility system, the returning temperature of the steam condensate, and the final temperature of the boiler feed water. The total site HEN is composed of several interlinked sub-HENs. A model for the new hot utility-process cold stream HEN is formulated together with the hot -cold process streams of the HEN. The linking constraints between sub-HENs and the utility system are formulated. Several case studies are elaborated to demonstrate the effectiveness and applicability of the proposed methodology. Compared with the former design methods without integrating steam condensate sensible heat and boiler feedwater preheating, meaningful economic benefits can be achieved by applying the proposed framework.

[1]  Ying Chen,et al.  Operational planning optimization of multiple interconnected steam power plants considering environmental costs , 2012 .

[2]  Cheng-Liang Chen,et al.  Heat-Exchanger Network Synthesis Involving Organic Rankine Cycle for Waste Heat Recovery , 2014 .

[3]  Christodoulos A. Floudas,et al.  Automatic synthesis of optimum heat exchanger network configurations , 1986 .

[4]  Arthur W. Westerberg,et al.  Minimum utility usage in heat exchanger network synthesis : a transportation problem , 1983 .

[5]  John R. Flower,et al.  Synthesis of heat exchanger networks: I. Systematic generation of energy optimal networks , 1978 .

[6]  T. Majozi,et al.  Steam System Network Synthesis Using Process Integration , 2008 .

[7]  Chonghun Han,et al.  Simultaneous synthesis of a heat exchanger network with multiple utilities using utility substages , 2015, Comput. Chem. Eng..

[8]  C. Chou,et al.  A thermodynamic approach to the design and synthesis of plant utility systems , 1987 .

[9]  John R. Flower,et al.  Synthesis of heat exchanger networks: II. Evolutionary generation of networks with various criteria of optimality , 1978 .

[10]  Martín Picón-Núñez,et al.  Modelling the power production of single and multiple extraction steam turbines , 2010 .

[11]  Arturo Jiménez-Gutiérrez,et al.  Synthesis of Heat Exchanger Networks with Optimal Placement of Multiple Utilities , 2010 .

[12]  Cheng-Liang Chen,et al.  Design of Entire Energy System for Chemical Plants , 2012 .

[13]  Juan M. Zamora,et al.  A global MINLP optimization algorithm for the synthesis of heat exchanger networks with no stream splits , 1998 .

[14]  Mahmoud M. El-Halwagi,et al.  Multiobjective design of interplant trigeneration systems , 2014 .

[15]  Mahmoud M. El-Halwagi,et al.  Optimal design of thermal membrane distillation systems with heat integration with process plants , 2015 .

[16]  Iftekhar A. Karimi,et al.  Synthesis of heat exchanger networks with nonisothermal phase changes , 2009 .

[17]  Jiří Jaromír Klemeš,et al.  Centralised utility system planning for a Total Site Heat Integration network , 2013, Comput. Chem. Eng..

[18]  Luis Puigjaner,et al.  Targeting and design methodology for reduction of fuel, power and CO2 on total sites , 1997 .

[19]  Christodoulos A. Floudas,et al.  ANTIGONE: Algorithms for coNTinuous / Integer Global Optimization of Nonlinear Equations , 2014, Journal of Global Optimization.

[20]  Denny K. S. Ng,et al.  Automated targeting model for synthesis of heat exchanger network with utility systems , 2016 .

[21]  X. Zhu,et al.  Automated design method for heat exchanger network using block decomposition and heuristic rules , 1997 .

[22]  Ignacio E. Grossmann,et al.  Simultaneous optimization models for heat integration—II. Heat exchanger network synthesis , 1990 .

[23]  Ignacio E. Grossmann,et al.  Optimal synthesis of heat exchanger networks involving isothermal process streams , 2008, Comput. Chem. Eng..

[24]  W. Verheyen,et al.  Design of flexible heat exchanger network for multi-period operation , 2006 .

[25]  Xianglong Luo,et al.  Modeling and optimization of a utility system containing multiple extractions steam turbines , 2011 .

[26]  Mahmoud M. El-Halwagi,et al.  Optimal integration of organic Rankine cycles with industrial processes , 2013 .

[27]  Ying Chen,et al.  Multi-objective optimization for the design and synthesis of utility systems with emission abatement technology concerns , 2014 .

[28]  Kevin C. Furman,et al.  A Critical Review and Annotated Bibliography for Heat Exchanger Network Synthesis in the 20th Century , 2002 .

[29]  E. Hohmann Optimum networks for heat exchange , 1999 .

[30]  Ying Chen,et al.  Heat integration of regenerative Rankine cycle and process surplus heat through graphical targeting and mathematical modeling technique , 2012 .

[31]  Robin Smith,et al.  Heat recovery and power targeting in utility systems , 2015 .

[32]  Ignacio E. Grossmann,et al.  Simultaneous optimization models for heat integration—I. Area and energy targeting and modeling of multi-stream exchangers , 1990 .

[33]  Iftekhar A. Karimi,et al.  Heat exchanger network synthesis using a stagewise superstructure with non-isothermal mixing , 2012 .

[34]  Ying Chen,et al.  Mathematical modeling, validation, and operation optimization of an industrial complex steam turbine network-methodology and application , 2016 .

[35]  Xianglong Luo,et al.  A multi-period mathematical model for simultaneous optimization of materials and energy on the refining site scale , 2015 .

[36]  Zhigang Shang,et al.  A transhipment model for the optimisation of steam levels of total site utility system for multiperiod operation , 2004, Comput. Chem. Eng..

[37]  Ignacio E. Grossmann,et al.  A structural optimization approach in process synthesis. II: Heat recovery networks , 1983 .

[38]  Jiří Jaromír Klemeš,et al.  Recent developments in Process Integration , 2013 .

[39]  Mahmoud M. El-Halwagi,et al.  Optimum heat storage design for solar‐driven absorption refrigerators integrated with heat exchanger networks , 2014 .

[40]  Zdravko Kravanja,et al.  Simultaneous synthesis of process water and heat exchanger networks , 2013 .

[41]  Christodoulos A. Floudas,et al.  Heat exchanger network synthesis without decomposition , 1991 .

[42]  Mahmoud M. El-Halwagi,et al.  Multi-objective optimization of process cogeneration systems with economic, environmental, and social tradeoffs , 2012, Clean Technologies and Environmental Policy.

[43]  Xianglong Luo,et al.  Coupling Process Plants and Utility Systems for Site Scale Steam Integration , 2013 .

[44]  Antonis C. Kokossis,et al.  Conceptual optimisation of utility networks for operational variations—I. targets and level optimisation , 1998 .

[45]  Ying Chen,et al.  Operational planning optimization of steam power plants considering equipment failure in petrochemical complex , 2013 .

[46]  Jiří Jaromír Klemeš,et al.  Total Site Heat Integration incorporating the water sensible heat , 2014 .

[47]  M. El‐Halwagi,et al.  Optimization across the Water–Energy Nexus for Integrating Heat, Power, and Water for Industrial Processes, Coupled with Hybrid Thermal-Membrane Desalination , 2016 .