Condenser Excel Carh

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    totalcondenser at ethanoldistillation column

    tube side shell side

    TB1 212 F TA1 77 F

    TB2 158 F TA2 120 F

    TBave 185 F TAave 98.5 FTwall 141.75 F

    Z 0.7962962963

    X 0.4

    Y 0.948 from Foust,Figure15.14a

    delta T1 92

    delta T2 81

    delta Tcorr 81.8913719363

    one shell pass, two tube passes

    properties

    density 53.434 lbft3 density 62.012375 lbft3

    specific heat,Cp 0.7268 !tulb F specific heat,Cp 1.0014 !tulb Fk 0.238 !tuft h F k 0.36155 !tuft h F

    viscosity 2.75"#04 lbft s viscosity 4.65"#04 lbft s

    deltav 471.92076 !tulb deltav #988.615 !tulb

    !ass flowrate 25044.92263 lbh !ass flowrate 297308.466 lbh

    " 12802162 !tuh

    assu!e no of tubes 360 tubes

    tube s$ecifications from Foust

    do 1 indi 0.87 in

    t 0.065 in

    %o 0.261 ft2ft

    %i 0.2278 ft2ft

    $itchdiameter 1.25 #i 0.00412826 ft2

    $itch 1.25 in n#i 0.74308658 ft2

    clearance 0.25 in

    $ 400099.364 lbft2 h

    &c 22 tubes %re 17346.7312

    'smin 27.75 %pr 4.63156155

    (herefore use from )err* &'!a( 0.013 from Foust

    'nominal 30 in

    'o 30 in hi 521.46275 !tuft2 h F

    'i 29 in )i 0.00841827 h ftF!tu

    +chedule 40

    #shell 0.3125 ft2

    $*+%C-./0T%-"+

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    $!a( 80143.752416 lbh ft2

    %re 6.74"/03

    %pr 3.0274212706

    &'!a( 0.013 from Foust, Figure15.16

    ho 361.8367758892 !tuh ft2 F

    )o 0.010588801 h ft F!tu

    Al! 0.2440237046

    ksteel 26 !tuh ft F

    )wall 0.0008537422

    Tl 158 F

    k 0.2384 !tuhftF

    density 53.454 lbft3

    viscosity 2.78"#04 lbft sTv 212 F

    density 0.09235 lbft3

    hfil! 774.8245015305

    )fil! 0.0049448844 h ft F !tu

    total 0.0248057004 h ft F!tu

    #ince the area of the phase with the 'reatest resistance is the shell side,consider Ao

    154.457143634 !tu h ft2 F

    % 1012.1320390108 ft2

    - 12.3437119067 ft

    3s 45167782947:

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    ,Figure15.16

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    Te!perature, ; #pecific heat, Cp, Btu3lb < ensity, lb3ft= Tr

    ethanol =465=722 65714=119>77 84597>4797>29 65>917>8699

    water =465=722 156684262661 >156=169>788= 65481828742

    TBA =465=722 659=81846688 885:462>9>2:2 65>:2187:2=

    TB =465=722 65881=996>49 8>5=922:1117: 65>>:48=>>4

    isobutene =465=722 65>=8::4=2:8 =15:96:61>:== 659=9811492

    0.7260720935 53.4538327536

    (em$erature, =465=722

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    latent heat, Btu3lb

    =>252=>>=6719:

    16615628874=8>4

    2=151178:>:92>

    1=>56:866=>8:2

    1285976867:687