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  • 7/25/2019 Hysys data summary

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    Problem 1

    Problem 2 PART AD501

    Temp of Steam(4.4 atm)(Celsius) 147

    Temp of IncomingStream

    (Celsius) 121.3Temp of Outgiong

    Stream(Celsius) 121.5

    og mean Temperature

    !i"ernce 25.59986979

    # $ %eat transfercoe&cient ('m2*s) 2000

    + , #*A*-T + $ nerg/ put into

    reboiler (0#r) 1.15E+08+ $ nerg/ put into

    reboiler (0s) 3.20E+04+ $ nerg/ put into

    reboiler (s) 3.20E+07A , +(#*-T)

    Area of Reboiler (m2) 624.4606415

    %eat of apori3ation(00g steam) 2121

    o Pressure SteamRe5uire6 (0g) 5.43E+04

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    R,2 R,7 R,8515 EtOH 0.9985 0.9986 0.9986510 EtOH 0.1941 0.1948 0.1962510 H2O 0.8053 0.8047 0.8035510 CO2 0.0006 0.0005 0.0003

    QH512

    1.11E+0

    8

    1.11E+0

    8

    1.11E+0

    8

    QRB5021.05E+0

    71.03E+0

    79.87E+0

    6

    QH5037.05E+0

    67.05E+0

    66.98E+0

    6

    QCD5011.92E+0

    62.82E+0

    64.64E+0

    6

    QH5068.13E+0

    58.13E+0

    58.13E+0

    5

    QH5091.54E+0

    71.54E+0

    71.55E+0

    7

    QRB501

    1.14E+0

    8

    1.15E+0

    8

    1.17E+0

    8

    QT507-8

    -1.50E+0

    4

    -1.47E+0

    4

    -1.40E+0

    4

    QCD5027.17E+0

    77.14E+0

    77.11E+0

    7

    QH5076.27E+0

    56.29E+0

    56.32E+0

    5

    TotalEnerg

    2.96E+07

    2.94E+07

    2.94E+07

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    3/7

    !e not"#e$ t%at an "n#rea&e "n t%e re'() rat"o o* t%e &&te "n#rea&e$ t%e,(r"t o* t%e nal ,ro$(#t (t al&o "n#rea&e$ t%e energ ne#e&&ar to#o,lete t%e ,ro#e&&. T%e ao(nt o* $"&t"llate &ent a#/ t%ro(g% t%e

    #ol(n "& "n#rea&e$ "t% an "n#rea&"ng re'() rat"o %"#% "& %at allo& *or

    Problem 2 PART 9!8:2

    R,7 R,7.; R,8515

    EtOH 0.9974 0.9985 0.9985511

    EtOH 0.689 0.7989 0.8002511H2O 0.3092 0.1992 0.1979511CO2 0.0018 0.0019 0.0019

    QRB5011.15E+

    081.15E+

    081.15E+0

    8

    QCD501

    2.82E+

    06

    2.82E+

    06

    2.82E+0

    6

    QRB5022.53E+

    061.04E+

    073.29E+0

    7

    QCD5026.24E+

    077.16E+

    079.41E+0

    7

    QH5067.88E+

    058.13E+

    058.13E+0

    5

    QT507-8

    -2.78E+

    04

    -1.49E+

    04

    -1.48E+0

    4

    QH5031.01E+

    077.11E+

    067.07E+0

    6

    QH5075.87E+

    056.28E+

    056.29E+0

    5

    QH5091.44E+

    071.54E+

    071.54E+0

    7

    QH5121.11E+

    081.11E+

    081.11E+0

    8

    Totalnerg/

    2.87E+07

    2.94E+07

    2.94E+07

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    t%e "n#rea&e "n ,(r"t ot% "n t%e oer%ea$ ,ro$(#t &trea a& ell a& t%enal et%anol ,ro$(#t.

    Problem 7 $

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    to o##(r re&(lt"ng "n a $e#rea&e "n ,(r"t. T%ere a& no ,ro,ort"onal"t to t%e"n#rea&e &"n#e e ere not a$;(&t"ng t%e n(er o* tra& to #o,en&ate *or

    t%e "n#rea&e "n 'o rate&.

    Problem 4

    C%ang"ng t%e Oer%ea$ 'o rate *ro t%e &e#on$ #ol(n &%oe$ a$e#rea&e "n t%e et%anol #on#entrat"on "n t%e &trea &"n#e t%e $"l(te$&trea #onta"ne$ ,ro,ort"onall ore ater. T%"& "n#rea&e $"$ not %ae a$e&"rale e

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    6/7

    Problem 8

    & t%e #on$en&at"on ,re&&(re "n#rea&e$ t%e reo"ler ,re&&(re a& "n#rea&e$

    to a"nta"n t%e ,re&&(re $ro,. T%"& re&(lte$ "n a tra te,erat(re "n#rea&e&"n#e t%e #ol(n ,re&&(re "& #%ange$ an$ a $"re#t re&(lt "n t%e olat"l"t"e& o*t%e ar"o(& #o,onent&. Re'()"ng t%e #o,onent& e#oe& "n#rea&"ngl$"=#(lt a& t%e ,re&&(re "& "n#rea&e$. T%"& $"=#(lt "n re'() re&(lt& "n oreenerg re>("re$ to #o,lete t%e &e,arat"on.

  • 7/25/2019 Hysys data summary

    7/7

    Problem =

    !e not"#e$ a &(&tant"al $"