Page 312 - Design and Operation of Heat Exchangers and their Networks

298 Design and operation of heat exchangers and their networks

Example H6C4—cont’d

Table 6.29 Problem data for H6C4 (Khorasany and Fesanghary, 2009).
2
_
Stream T in (°C) T out (°C) C (kW/K) α (kW/m K) Cost ($/kWyr)
H1 85 45 156.3 0.05
H2 120 40 50 0.05
H3 125 35 23.9 0.05
H4 56 46 1250 0.05
H5 90 86 1500 0.05
H6 225 75 50 0.05
C1 40 55 466.7 0.05
C2 55 65 600 0.05
C3 65 165 180 0.05
C4 10 170 81.3 0.05
HU 200 198 0.05 100
CU 15 20 0.05 15
2
Heat exchanger cost¼60A$/yr (A in m )
Total annual cost ($/yr)

Solutions in the literature Reported Revised
Own work – 5,585,391
Xiao and Cui (2017) 5,589,493 a 5,585,784
Peng and Cui (2015) 5,596,079 5,592,285
Chen and Cui (2016) 5,593,970 b 5,593,028
Zhang et al. (2017) 5,607,761 5,607,754
He and Cui (2013) 5,609,271 5,609,270
Ravagnani et al. (2005) 5,672,821
Myankooh and Shafiei (2016) 5,640,721 5,640,719
Myankooh and Shafiei (2015) 5,640,724
Huang et al. (2012) c 5,738,268 5,642,268
Huo et al. (2013) 5,645,688 5,642,387
Khorasany and Fesanghary (2009) 5,662,366 5,642,958
Gorji-Bandpy et al. (2011) 5,139,495 5,643,660
Huo et al. (2012) 5,657,000 5,646,818
Yerramsetty and Murty (2008) 5,666,756 5,666,750

Total annual cost ($/yr)
Solutions in the literature
2
Heat exchanger cost58000+60A$/yr (A in m ) Reported Revised
Pava ˜o et al. (2017a) 5,713,267 5,713,267
Pava ˜o et al. (2017b) 5,715,026 5,714,929
Huang and Karimi (2014) 5,733,679 5,734,428
a
After revision, H1C2 is deleted.
b
After revision, 5units are deleted.
c
With stream split.