168791182 coil design xlsx
TRANSCRIPT
-
8/16/2019 168791182 Coil Design Xlsx
1/11
-
8/16/2019 168791182 Coil Design Xlsx
2/11
+h 80
>
-
8/16/2019 168791182 Coil Design Xlsx
3/11
PROPERTIES OF HOT & COLD FLUID
Steam [Use TABLE 6-16
3.71 HEnthalpy/ Latent heat of evaporation (E) 877.5 !"#/l$
i*+o+ity (,) 0.01- +
Se!"#$e Fl%# '(ate!)
pe+i2+ Heat of e**el +ontent ( p) 1 inal "empe+i2+ ravity of Li%&i' ( g) 0. 8 "ime to
L*+ mean Tem, D# e!en$e '.T)"D -5.00 nte
L"D 133.-0 nt 9" 1 .07 E:tHeat Lo** thro&gh ve**el (if ve**el not in*&late' el*e ?0) 78000.00
%ant#t0 * L#2%# t* 3e 4eate 5
%ant#t0 * L#2%# t* 3e 4eate 5 ' *! 3at$4 P!* %$t#*n) -5.-- ft3/hr
@a** loA BateC @ 4015.3- l$/hr - .4 g
Heat Be%&ire'C 84 30.80 !"#/Hr
Heat "ran*fer oeF+ientC # 11.75
;rea of oil Be%&ire' (;r)? / ( #9" ) 0.88 of ipe 1.55 in Dv/30
learan+e from ve**el Aall ( ) 10 in
-.4- in
Length of ipe re%&ire' (Lr)?;r/ -0.- 38374 ftoil ra'i&* (D+) - in (Dc > 20di)it+h (p) .5 in ( Pmax=5*NPS & Pmin=2*NPS; r
8. 178 -18 4-.3 8747ele+te' n&m$er of t&rn* (Lselect< li !id le"el)
;+t&al Length of +oilC La -1. - 4-.3 8747Bate of loAC G? /E -7.7- l$/hr
3 8810.1055
3.33ft/*e+ 1.015-7 m/*e+
4.418045081 p*ig
f? 0.0 5 for Be?3 8810
pe+i2+ ol&me ( *) ft 3 /l$
!"#/l$/o
ft 3 /hr( " /")
?@ 9" L!"#/hr=ft =o
ft
enterline 'iameter of oil (D +)
ele+te' n&m$er of t&rn*C *ele+t
Beynol'* n&m$erC Be ? (-.31 G)/ ('i ,)
elo+ity of team in GaterC ? 0.00085G */ 'ire**&re 'ropC 9 ? fL a / 3gD i g i* a++ '&e to gravity?4.17I10
-
8/16/2019 168791182 Coil Design Xlsx
4/11
3.87 ft
3.44 ft.7 ft
3 .83134 .00
77.00
08.400.5 Hr
in0.07 75 ft
0.344 ft /ft
-
8/16/2019 168791182 Coil Design Xlsx
5/11
-
8/16/2019 168791182 Coil Design Xlsx
6/11
1 2 5 10 20 50 100
0.667 0.524 0.388 0.313 0.255 0.197 0.164
0.01 0.01 0.011 0.012 0.012 0.013 0.0141500 0.041 0.041 0.041 0.041 0.041 0.041 0.0411450 0.04 0.04 0.04 0.04 0.04 0.04 0.041400 0.039 0.039 0.039 0.039 0.039 0.039 0.0391350 0.038 0.038 0.038 0.038 0.038 0.038 0.0381300 0.037 0.037 0.037 0.037 0.037 0.037 0.0371250 0.035 0.035 0.035 0.035 0.035 0.035 0.0351200 0.034 0.034 0.034 0.034 0.034 0.034 0.0341150 0.034 0.034 0.034 0.034 0.034 0.034 0.0341100 0.032 0.032 0.032 0.032 0.032 0.032 0.0321050 0.031 0.031 0.031 0.031 0.031 0.031 0.0311000 0.03 0.03 0.03 0.03 0.03 0.03 0.03950 0.029 0.029 0.029 0.029 0.029 0.029 0.029900 0.028 0.028 0.028 0.028 0.028 0.028 0.028850 0.026 0.026 0.026 0.026 0.26 0.026 0.027800 0.025 0.025 0.025 0.025 0.025 0.025 0.025750 0.024 0.024 0.024 0.024 0.024 0.024 0.024700 0.023 0.023 0.023 0.023 0.023 0.023 0.023
650 0.022 0.022 0.022 0.022 0.022 0.022 0.022600 0.021 0.021 0.021 0.021 0.021 0.021 0.021550 0.02 0.02 0.02 0.02 0.02 0.02 0.02500 0.019 0.019 0.019 0.019 0.019 0.019 0.019450 0.018 0.018 0.018 0.018 0.017 0.017 0.017400 0.016 0.016 0.016 0.016 0.016 0.016 0.016350 0.015 0.015 0.015 0.015 0.015 0.015 0.015300 0.014 0.014 0.014 0.014 0.014 0.014 0.182250 0.013 0.013 0.013 0.013 0.013 0.228 0.228200 0.012 0.012 0.012 0.012 0.3 0.3 0.3
150 0.011 0.011 0.427 0.427 0.427 0.427 0.427100 0.68 0.68 0.68 0.68 0.68 0.68 0.6850 1.299 1.299 1.299 1.299 1.299 1.299 1.29932 1.753 1.753 1.753 1.753 1.753 1.753 1.753
Dynami+ i*+o*ity = J =
"emperat& ;$*ol&te pre**
( oF)
SaturatedWater
SaturatedSteam
The critical point for water i 705.40 oF and 32Blue ! &i co it$ of water
http://www.engineeringtoolbox.com/dynamic-absolute-kinematic-viscosity-d_412.htmlhttp://www.engineeringtoolbox.com/temperature-d_291.htmlhttp://www.engineeringtoolbox.com/pressure-d_587.htmlhttp://www.engineeringtoolbox.com/pressure-d_587.htmlhttp://www.engineeringtoolbox.com/temperature-d_291.htmlhttp://www.engineeringtoolbox.com/dynamic-absolute-kinematic-viscosity-d_412.html
-
8/16/2019 168791182 Coil Design Xlsx
7/11
1% Supercritical fluid are pha e of u# tance at hi'h pre ure a#o&e their critical temperature . Supercritic
-
8/16/2019 168791182 Coil Design Xlsx
8/11
200 500 1000 2000 5000 7500 10000
0.138 0.111 0.094 0.078 ! ! !
0.015 0.017 0.019 0.023 ! ! !0.041 0.042 0.042 0.042 0.044 0.046 0.0480.04 0.04 0.041 0.041 0.043 0.045 0.047
0.039 0.039 0.04 0.04 0.042 0.044 0.0470.038 0.038 0.038 0.039 0.041 0.044 0.0470.037 0.037 0.037 0.038 0.04 0.043 0.0460.036 0.036 0.036 0.037 0.039 0.042 0.0450.034 0.035 0.035 0.036 0.038 0.041 0.0450.034 0.034 0.034 0.034 0.037 0.041 0.0450.032 0.033 0.033 0.034 0.037 0.04 0.0450.031 0.032 0.032 0.033 0.036 0.04 0.0470.03 0.03 0.031 0.032 0.035 0.041 0.049
0.029 0.029 0.03 0.031 0.035 0.042 0.0520.028 0.028 0.028 0.029 0.035 0.045 0.0570.027 0.027 0.027 0.028 0.035 0.052 0.0640.025 0.026 0.026 0.027 0.04 0.062 0.0710.024 0.025 0.025 0.026 0.057 0.071 0.0780.023 0.023 0.024 0.026 0.071 0.079 0.085
0.022 0.023 0.023 0.023 0.082 0.088 0.0920.021 0.021 0.021 0.087 0.091 0.096 0.1010.02 0.02 0.019 0.095 0.101 0.105 0.109
0.018 0.018 0.103 0.105 0.111 0.114 0.1190.017 0.115 0.116 0.118 0.123 0.127 0.1310.016 0.131 0.132 0.134 0.138 0.143 0.1470.152 0.153 0.154 0.155 0.16 0.164 0.1680.183 0.183 0.184 0.185 0.19 0.194 0.1980.228 0.228 0.229 0.231 0.235 0.238 0.242
0.3 0.301 0.301 0.303 0.306 0.31 0.313
0.427 0.427 0.428 0.429 0.431 0.434 0.4370.68 0.68 0.68 0.68 0.681 0.682 0.683
1.299 1.299 1.299 1.296 1.289 1.284 1.2791.752 1.751 1.753 1.745 1.733 1.723 1.713
(+enti oi*e)
&re = p = (p*ia)
6.2 psia (374 oC - 218 atm) ! "or pre ure #e$ond thi point the fluid i upercritical 1%.
http://www.engineeringtoolbox.com/dynamic-absolute-kinematic-viscosity-d_412.htmlhttp://www.engineeringtoolbox.com/pressure-d_587.htmlhttp://www.engineeringtoolbox.com/pressure-d_587.htmlhttp://www.engineeringtoolbox.com/dynamic-absolute-kinematic-viscosity-d_412.html
-
8/16/2019 168791182 Coil Design Xlsx
9/11
al water i uperheated team under hi'h pre ure of more than 3206.2 psia (200 atm) . (nder the e conditio
-
8/16/2019 168791182 Coil Design Xlsx
10/11
-
8/16/2019 168791182 Coil Design Xlsx
11/11
n upercritical water decompo e to man$ u# tance