TY - GEN
T1 - MINLP optimization algorithm for the synthesis of heat and work exchange networks
AU - Onishi, Viviani C.
AU - Ravagnani, Mauro A. S. S.
AU - Caballero, José A.
PY - 2014
Y1 - 2014
N2 - This paper introduces a new optimization model for the simultaneous synthesis of heat and work exchange networks. The work integration is performed in the work exchange network (WEN), while the heat integration is carried out in the heat exchanger network (HEN). In the WEN synthesis, streams at high-pressure (HP) and low-pressure (LP) are subjected to pressure manipulation stages, via turbines and compressors running on common shafts and stand-alone equipment. The model allows the use of several units of single-shaft-turbine-compressor (SSTC), as well as helper motors and generators to respond to any shortage and/or excess of energy, respectively, in the SSTC axes. The heat integration of the streams occurs in the HEN between each WEN stage. Thus, as the inlet and outlet streams temperatures in the HEN are dependent of the WEN design, they must be considered as optimization variables. The proposed multi-stage superstructure is formulated in mixed-integer nonlinear programming (MINLP), in order to minimize the total annualized cost composed by capital and operational expenses. A case study is conducted to verify the accuracy of the proposed approach. The results indicate that the heat integration between the WEN stages is essential to enhance the work integration, and to reduce the total cost of process due the need of a smaller amount of hot and cold utilities.
AB - This paper introduces a new optimization model for the simultaneous synthesis of heat and work exchange networks. The work integration is performed in the work exchange network (WEN), while the heat integration is carried out in the heat exchanger network (HEN). In the WEN synthesis, streams at high-pressure (HP) and low-pressure (LP) are subjected to pressure manipulation stages, via turbines and compressors running on common shafts and stand-alone equipment. The model allows the use of several units of single-shaft-turbine-compressor (SSTC), as well as helper motors and generators to respond to any shortage and/or excess of energy, respectively, in the SSTC axes. The heat integration of the streams occurs in the HEN between each WEN stage. Thus, as the inlet and outlet streams temperatures in the HEN are dependent of the WEN design, they must be considered as optimization variables. The proposed multi-stage superstructure is formulated in mixed-integer nonlinear programming (MINLP), in order to minimize the total annualized cost composed by capital and operational expenses. A case study is conducted to verify the accuracy of the proposed approach. The results indicate that the heat integration between the WEN stages is essential to enhance the work integration, and to reduce the total cost of process due the need of a smaller amount of hot and cold utilities.
KW - Heat exchanger network (HEN)
KW - Heat integration
KW - Mixed-integer nonlinear programming (MINLP)
KW - Optimization
KW - Work exchange network (WEN)
UR - https://www.scopus.com/pages/publications/84902972571
U2 - 10.1016/B978-0-444-63456-6.50020-X
DO - 10.1016/B978-0-444-63456-6.50020-X
M3 - Conference contribution
AN - SCOPUS:84902972571
SN - 9780444634566
T3 - Computer Aided Chemical Engineering
SP - 115
EP - 120
BT - 24th European Symposium on Computer Aided Process Engineering
PB - Elsevier B.V.
T2 - 24th European Symposium on Computer Aided Process Engineering 2014
Y2 - 16 June 2014 through 18 June 2014
ER -