Targeting and Design of Work and Heat Exchange Networks

Work and heat are the two major forms of energy consumption in the process industry. They are respectively consumed in the work exchange and heat exchange networks. Due to the tight interactions be...

[1]  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 .

[2]  Chao Fu,et al.  Work Exchange Networks (WENs) and Work and Heat Exchange Networks (WHENs) - A Review of the Current State-of-the-Art , 2020 .

[3]  Zuwei Liao,et al.  Modelling and simulation of two-bed PSA process for separating H2 from methane steam reforming , 2019, Chinese Journal of Chemical Engineering.

[4]  Yongrong Yang,et al.  Transshipment type heat exchanger network model for intra- and inter-plant heat integration using process streams , 2019, Energy.

[5]  Truls Gundersen,et al.  Model reformulations for Work and Heat Exchange Network (WHEN) synthesis problems , 2019, Comput. Chem. Eng..

[6]  Paul I. Barton,et al.  Nonsmooth Formulation for Handling Unclassified Process Streams in the Optimization of Work and Heat Exchange Networks , 2019, Industrial & Engineering Chemistry Research.

[7]  Yongrong Yang,et al.  A novel two-step method to design inter-plant hydrogen network , 2019, International Journal of Hydrogen Energy.

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

[9]  Yongrong Yang,et al.  Molecular reconstruction: Recent progress toward composition modeling of petroleum fractions , 2019, Chemical Engineering Journal.

[10]  Chao Fu,et al.  Identifying optimal thermodynamic paths in work and heat exchange network synthesis , 2018, AIChE Journal.

[11]  Viviani C. Onishi,et al.  Optimal synthesis of work and heat exchangers networks considering unclassified process streams at sub and above-ambient conditions , 2018, Applied Energy.

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

[13]  Zuwei Liao,et al.  Optimal design of hybrid cryogenic flash and membrane system , 2018 .

[14]  Yongrong Yang,et al.  New transshipment type MINLP model for heat exchanger network synthesis , 2017 .

[15]  Christos T. Maravelias,et al.  Simultaneous Utility and Heat Exchanger Area Targeting for Integrated Process Synthesis and Heat Integration , 2017 .

[16]  Linlin Liu,et al.  Step-wise synthesis of work exchange networks involving heat integration based on the transshipment model☆ , 2017 .

[17]  Zuwei Liao,et al.  Optimal process design for recovering effluent gas at subambient temperature , 2017 .

[18]  Ignacio E. Grossmann,et al.  A novel disjunctive model for the simultaneous optimization and heat integration , 2017, Comput. Chem. Eng..

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

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

[21]  Zuwei Liao,et al.  Strategy of effluent recovery technology selection in polyolefin plants , 2016 .

[22]  Chao Fu,et al.  Sub-ambient heat exchanger network design including expanders , 2015 .

[23]  Chao Fu,et al.  Integrating compressors into heat exchanger networks above ambient temperature , 2015 .

[24]  Chao Fu,et al.  Integrating expanders into heat exchanger networks above ambient temperature , 2015 .

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

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

[27]  Ignacio E. Grossmann,et al.  An alternative disjunctive optimization model for heat integration with variable temperatures , 2013, Comput. Chem. Eng..

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

[29]  Paul Serban Agachi,et al.  Review: Important contributions in development and improvement of the heat integration techniques , 2010, Comput. Chem. Eng..

[30]  Truls Gundersen,et al.  A liquefied energy chain for transport and utilization of natural gas for power production with CO2 capture and storage – Part 1 , 2009 .

[31]  Truls Gundersen,et al.  A liquefied energy chain for transport and utilization of natural gas for power production with CO2 capture and storage - Part 2: The offshore and the onshore processes , 2009 .

[32]  Truls Gundersen,et al.  A liquefied energy chain for transport and utilization of natural gas for power production with CO2 capture and storage – Part 3: The combined carrier and onshore storage , 2009 .

[33]  T. Gundersen,et al.  A liquefied energy chain for transport and utilization of natural gas for power production with CO2 capture and storage - Part 4: Sensitivity analysis of transport pressures and benchmarking with conventional technology for gas transport , 2009 .

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

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

[36]  Laurence A. Wolsey,et al.  Integer and Combinatorial Optimization , 1988, Wiley interscience series in discrete mathematics and optimization.

[37]  Ignacio E. Grossmann,et al.  Simultaneous optimization and heat integration of chemical processes , 1986 .

[38]  William R. Paterson,et al.  A replacement for the logarithmic mean , 1984 .

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

[40]  Dale F. Rudd,et al.  The synthesis of system designs. II. Heuristic structuring , 1969 .