Shell and Tube Heat Exchanger Cost Estimation

Shell And Tube Tube Heat H eat Exchanger Exchanger Cost Estimation 21 June 2012 Posted by ankur2061  in Technical

As promised in my earlier blog entry "Cost Estimation Of i!ed oof #Cone$ Carbon %teel %torage Tan&s"' today(s blog entry relates to cost estimation of %)T heat e!changers* The e+uations are empirical and the reference is the same i*e*, "Estimate Costs of -eat E!changers E!chan gers and %torage Tan&s .ia Correlations" by Armando /* Corripio' atherine %* Chrien' and arence /* E.ans' Chemical Engineering maga3ine January 24' 1562* There is a bunch of e+uations and it too& some time to program it in e!cel but ultimately it as done* et us get don to the e+uations, Base Cost for CS loating!Head" #00 k$ag %100 &sig' exchanger S( )nits

C/ 7 E8P#6*202 9 0*0140:;lnA 0*014 0:;lnA 9 0*0:611;#lnA$ 0*0:611;#lnA$2$ here, C/ 7 /ase Cost of the -E' m2? > 9 0*060;lnA$ here, = 7 E!changer@type cost factor   Design-pressure cost factor, F  P 

700-2100 kPag , P 7 0*6544 9 0*0>561;lnA 2100-4200 kPag , P 7 1*2002 9 0*0B1>0;lnA 4200-6200 kPag , P 7 1*>2B2 9 0*12066;lnA here, P 7 =esign@pressure cost factor   Material-of-Construction Cost Factor, F  M 

SS316 ,  71*>1>> 9 0*225:;lnA SS304,  71*1551 9 0*1456>;lnA SS347 ,  71*166 9 0*2216:;lnA  Nikel 200,

 72*544 9 0*:0645;lnA  !o"el 400,  72*25: 9 0*>BB;lnA  #"o"el 600,  72*>10 9 0*40B:>;lnA  #"olo$ %2&,  72*::4 9 0*>5B0:;lnA Tita"iu',  72*4:1B 9 0*>251;lnA  Ha(tello$,  7*B:1> 9 1*41BB>;lnA here,  7 aterial@of@construction cost factor  Heat!Exchanger Cost " C E

CE 7 C/;/;=; here, CE 7 -eat E!changer Cost' 20 9 0*>251;lnA  Ha(tello$,  70*14>5 9 1*41BB>;lnA here,  7 aterial@of@construction cost factor  Heat!Exchanger Cost " C E

CE 7 C/;/;=; here, CE 7 -eat E!changer Cost'