TY - JOUR
T1 - Multi-objective optimization design of condenser in an organic Rankine cycle for low grade waste heat recovery using evolutionary algorithm
AU - Wang, Jiangfeng
AU - Wang, Man
AU - Li, Maoqing
AU - Xia, Jiaxi
AU - Dai, Yiping
PY - 2013/7
Y1 - 2013/7
N2 - The optimum design of a condenser is significant in an organic Rankine cycle to achieve higher waste heat utilization efficiency. Based on the mathematical model of a condenser using plate heat exchanger (PHE), some key geometric parameters on the total heat transfer surface area and pressure drop of the condenser are examined. In order to obtain geometric parameters of a plate heat exchanger, a multi-objective optimization of the condenser in organic Rankine cycle is conducted to achieve the optimal geometry design. The total heat transfer surface area and pressure drop are selected as two objective functions to minimize both total heat transfer surface area and pressure drop under the constant heat transfer rate and LMTD conditions. The plate width, plate length and plant distance are selected as the decision variables. Non-dominated sorting generic algorithm-II (NSGA-II) which is an effective multi-objective optimization method is employed to solve this multi-objective optimization design of PHE. The results show that an increase in channel distance or plate width increases the total heat transfer surface area and decreases pressure drop in the condenser. It is noted that the plate length of PHE has a positive effect on the optimization design of PHE. By multi-objective optimization design of the PHE, a Pareto optimal point curve is obtained, which shows that a decrease in total heat transfer surface area of a condenser can increase the pressure drop through the condenser. •Effects of key geometric parameters on the performance of condenser are examined.•Multi-objective optimization is conducted to obtain optimum geometric parameters.•NSGA-II is employed to achieve the multi-objective optimization problem.
AB - The optimum design of a condenser is significant in an organic Rankine cycle to achieve higher waste heat utilization efficiency. Based on the mathematical model of a condenser using plate heat exchanger (PHE), some key geometric parameters on the total heat transfer surface area and pressure drop of the condenser are examined. In order to obtain geometric parameters of a plate heat exchanger, a multi-objective optimization of the condenser in organic Rankine cycle is conducted to achieve the optimal geometry design. The total heat transfer surface area and pressure drop are selected as two objective functions to minimize both total heat transfer surface area and pressure drop under the constant heat transfer rate and LMTD conditions. The plate width, plate length and plant distance are selected as the decision variables. Non-dominated sorting generic algorithm-II (NSGA-II) which is an effective multi-objective optimization method is employed to solve this multi-objective optimization design of PHE. The results show that an increase in channel distance or plate width increases the total heat transfer surface area and decreases pressure drop in the condenser. It is noted that the plate length of PHE has a positive effect on the optimization design of PHE. By multi-objective optimization design of the PHE, a Pareto optimal point curve is obtained, which shows that a decrease in total heat transfer surface area of a condenser can increase the pressure drop through the condenser. •Effects of key geometric parameters on the performance of condenser are examined.•Multi-objective optimization is conducted to obtain optimum geometric parameters.•NSGA-II is employed to achieve the multi-objective optimization problem.
KW - Condenser
KW - Genetic algorithm
KW - Low grade waste heat
KW - Multi-objective optimization
KW - Organic Rankine cycle
KW - Plate heat exchanger
UR - https://www.scopus.com/pages/publications/84878830673
U2 - 10.1016/j.icheatmasstransfer.2013.04.014
DO - 10.1016/j.icheatmasstransfer.2013.04.014
M3 - 文章
AN - SCOPUS:84878830673
SN - 0735-1933
VL - 45
SP - 47
EP - 54
JO - International Communications in Heat and Mass Transfer
JF - International Communications in Heat and Mass Transfer
ER -