168791182 coil design xlsx

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    +h 80

    >

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    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

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    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

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    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

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    1% Supercritical fluid are pha e of u# tance at hi'h pre ure a#o&e their critical temperature . Supercritic

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    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

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    al water i uperheated team under hi'h pre ure of more than 3206.2 psia (200 atm) . (nder the e conditio

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    n upercritical water decompo e to man$ u# tance