Page 200 - Analysis, Synthesis and Design of Chemical Processes, Third Edition
P. 200
From Figure 7.4, (2001) = ($ 250)(100) = $25,000 (the evaluation path is shown on Figure 7.4).
The bare module cost for shell-and-tube heat exchangers is given by Equation A.4.
(A.4)
The values of B and B for floating-head heat exchangers from Table A.4 are 1.63 and 1.66, respectively.
2
1
The pressure factor is obtained from Equation A.3.
(A.3)
From Table A.2, for pressures <5 barg, C = C = C = 0, and from Equation A.3, F = 1. Using data in
2
3
p
1
Table A.3 for shell-and-tube heat exchangers with both shell and tubes made of carbon steel
(Identification Number = 1) and Figure A.8, F = 1. Substituting this data into Equation A.4 gives
M
