Find the bare module cost of a floating-head shell-and-tube heat exchanger with a heat transfer area of 100m2 at the end of 2006(Cl=500). The operating pressure of the equipment is 1.0 bar, with both shell-and-tube sides constructed of carbon steel. The cost curve for this heat exchanger is given The bare module cost of the HE is given as CBM=Cp0[B1+B2FpFM1] The values of B1 and B2 for floating-head heat exchangers from Table A.4 are 1.63 and 1.66. respectively. The pressure tactor is obtained from log10FP=C1+C2log10P+C3(log10P)2 Value of the 3 constants is zero. - Repeat Example 7.10 considering the following: - Operating pressure 12 bar. - Floating head, shell \& tube constructed using stainless steel (SS)