A pinch-based method for defining pressure manipulation routes in work and heat exchange networks

Abstract Aiming for more energetically efficient and sustainable solutions, academic attention to work and heat integration (WHI) has grown in the last decade. Simultaneous models for work and heat exchanger network (WHEN) synthesis often derive from heat integration (HI) frameworks. However, it can be noted that simultaneous optimization models for WHI are considerably more complex to solve than in the HI case. The design of efficient pressure manipulation routes (i.e., allocation and sizing of compression and expansion machinery) in process streams prior to heat exchange match allocation can make the optimization procedure more efficient. This work proposes a systematic procedure based on a model that employs Pinch Analysis concepts for defining these routes based on capital and operating cost targets. The solution approach is a hybrid meta-heuristic method based on Simulated Annealing (SA) and Particle Swarm Optimization (PSO). The obtained routes are then converted into a HI problem by fixing pressure manipulation unit sizes. The detailed HI solution is finally transferred into a WHI optimization model as initial design. In the two tackled examples, the total annual costs (TAC) predicted by the Pinch-based model differed by 0.5% and 1.2% from the final optimized WHEN obtained in the detailed WHI framework.

[1]  Linlin Liu,et al.  Upgraded Graphical Method for the Synthesis of Direct Work Exchanger Networks , 2017 .

[2]  Chao Fu,et al.  Work and heat integration: An emerging research area , 2018, Energy.

[3]  Iftekhar A. Karimi,et al.  Work-heat exchanger network synthesis (WHENS) , 2016 .

[4]  Viviani C. Onishi,et al.  Simultaneous synthesis of work exchange networks with heat integration , 2014 .

[5]  Li Zhao,et al.  Multi-stage gas separation membrane processes used in post-combustion capture: Energetic and economic analyses , 2010 .

[6]  T. Gundersen,et al.  Heat and work integration: Fundamental insights and applications to carbon dioxide capture processes , 2016 .

[7]  Paul I. Barton,et al.  Synthesis of heat exchanger networks at subambient conditions with compression and expansion of process streams , 2011 .

[8]  Carlos A. Infante Ferreira,et al.  Pinch Analysis and Process Integration , 2016 .

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

[10]  R. N. Blurton,et al.  CONSERVATION OF ENERGY ON A 40,000 BPSD FLUID CATALYTIC CRACKING UNIT UTILISING A FLUE GAS EXPANSION TURBINE , 1982 .

[11]  Jiří Jaromír Klemeš,et al.  New directions in the implementation of Pinch Methodology (PM) , 2018, Renewable and Sustainable Energy Reviews.

[12]  Truls Gundersen,et al.  An Extended Pinch Analysis and Design procedure utilizing pressure based exergy for subambient cooling , 2007 .

[13]  Bodo Linnhoff,et al.  Cost optimum heat exchanger networks—1. Minimum energy and capital using simple models for capital cost , 1990 .

[14]  M. Rosen Environmental sustainability tools in the biofuel industry , 2018 .

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

[16]  Warren D. Seider,et al.  Product and Process Design Principles: Synthesis, Analysis, and Evaluation , 1998 .

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

[18]  Manfred Morari,et al.  Area and capital cost targets for heat exchanger network synthesis with constrained matches and unequal heat transfer coefficients , 1990 .

[19]  Chao Fu,et al.  Correct integration of compressors and expanders in above ambient heat exchanger networks , 2016 .

[20]  Jiří Jaromír Klemeš,et al.  Forty years of Heat Integration: Pinch Analysis (PA) and Mathematical Programming (MP) , 2013 .

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

[22]  Iftekhar A. Karimi,et al.  Unified Heat Exchanger Network Synthesis via a Stageless Superstructure , 2019, Industrial & Engineering Chemistry Research.

[23]  Mauro A.S.S. Ravagnani,et al.  Heat Exchanger Network Synthesis without stream splits using parallelized and simplified simulated Annealing and Particle Swarm Optimization , 2017 .

[24]  James Kennedy,et al.  Particle swarm optimization , 2002, Proceedings of ICNN'95 - International Conference on Neural Networks.

[25]  Iftekhar A. Karimi,et al.  Framework for work‐heat exchange network synthesis (WHENS) , 2018 .

[26]  C. D. Gelatt,et al.  Optimization by Simulated Annealing , 1983, Science.

[27]  Mauro A.S.S. Ravagnani,et al.  A new framework for work and heat exchange network synthesis and optimization , 2019, Energy Conversion and Management.

[28]  Mauro A.S.S. Ravagnani,et al.  Large-Scale Heat Exchanger Networks Synthesis using Simulated Annealing and the novel Rocket Fireworks Optimization , 2017 .

[29]  L. T. Fan,et al.  Analysis of a Work Exchanger Network , 1996 .

[30]  Mauro A.S.S. Ravagnani,et al.  Synthesis and optimization of work and heat exchange networks using an MINLP model with a reduced number of decision variables , 2020 .

[31]  Mauro A.S.S. Ravagnani,et al.  An Enhanced Stage-wise Superstructure for Heat Exchanger Networks Synthesis with New Options for Heaters and Coolers Placement , 2018 .

[32]  Christodoulos A. Floudas,et al.  Strategies for overcoming uncertainties in heat exchanger network synthesis , 1989 .

[33]  Mauro A.S.S. Ravagnani,et al.  Work and heat exchange network synthesis considering multiple electricity-related scenarios , 2019, Energy.

[34]  Kevin C. Furman,et al.  Computational complexity of heat exchanger network synthesis , 2001 .

[35]  Viviani C. Onishi,et al.  Simultaneous synthesis of heat exchanger networks with pressure recovery: optimal integration between heat and work , 2014 .

[36]  B. Linnhoff,et al.  The pinch design method for heat exchanger networks , 1983 .

[37]  Iftekhar A. Karimi,et al.  Preliminary synthesis of work exchange networks , 2012, Comput. Chem. Eng..

[38]  William T. Andrews,et al.  A twelve-year history of large scale application of work-exchanger energy recovery technology☆ , 2001 .

[39]  Mauro A.S.S. Ravagnani,et al.  A new stage-wise superstructure for heat exchanger network synthesis considering substages, sub-splits and cross flows , 2018, Applied Thermal Engineering.

[40]  Viviani C. Onishi,et al.  Retrofit of heat exchanger networks with pressure recovery of process streams at sub-ambient conditions , 2015 .

[41]  Chao Fu,et al.  Work and heat integration—A new field in process synthesis and process systems engineering , 2018, AIChE Journal.

[42]  Richard Turton,et al.  Analysis, Synthesis and Design of Chemical Processes , 2002 .

[43]  Chao Fu,et al.  Towards the use of mathematical optimization for work and heat exchange networks , 2017 .

[44]  G. Manfrida,et al.  Exergoeconomic and exergoenvironmental analysis of an integrated solar gas turbine/combined cycle power plant , 2018, Energy.

[45]  Yuan Xiao,et al.  Non-structural model of heat exchanger network: Modeling and optimization , 2019 .

[46]  L. T. Fan,et al.  Flow work exchanger , 1967 .