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Raffinate column

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    Composition of feed, top and bottom and relative vol

    The key components selected are n-C4 and i-C5 as light and heavy key resp

    Components Xf Xd Xb K-Values

    i-C4 0.1895 0.4789 0 3.4805390744

    n-C4 0.03 0.505 0.00!4 .!591457

    i-C5 0.314 0.0159 0.508 1.430511515

    5N5 0.038 0 0.0394 0.757098147

    2,2 DMC4 0.0!3 0 0.103 0.!71397855

    2,3 DMC4 0.018 0 0.098 0.53159!478

    2MC5 0.0!5 0 0.1079 0.505371437

    3MC5 0.04 0 0.0!!1 0.457!30077

    5N 0.04! 0 0.0704 0.3!5!1!515

    N 0.039 0 0.0!44 0.93987917N! 0.005 0 0.004 0.153777559

    "-#al$e %&"' 1.430511515 i-C5

    (vg Temp T 153.15 ) !7.31 C

    Cal"ulation of minimum number of sta#es Nm:

    )rom )enske *+$ation

    ,m 10.33899

    ,m 11

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    Cal"ulation of minimum re$u% ratio:

    )rom Col$rn and nder/ood /e have an epression or minim$m re2$ rati

    &'i ( Xif)*&'i - +)

    0.3790004519

    0.590!71!939

    -0.785

    -val$e can e o$nd y -0.01703993!

    -0.03903315

    -0.00791!7101

    -0.0!47099

    eed is at oiling point so +1 -0.014715!95-0.011330508

    thereore at 1.7 -0.00795!!1

    -0.000439

    0

    0

    0

    m61 .38!5911998 0

    m 1.38!5911998 0

    0

    00

    um 0.0!085975

    -Value 1.4

    e2$ ratio is 1. times the minim$m re2$ ratio

    e2$ atio 1. m

    e2$ atio 1.!!39094397

    Cal"ulation of Number of t.eoreti"al plates:

    /e rst need to nd the ratios o %mm61' and %61'

    mm61 0.580993375

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    61 0.!4!118!3!

    )rom *rar-addo correlation Vis / Vis 0

    ,m, 0.3 30.51 170.

    ,m 11 !5.84 1!0.

    , 34.375 3!7.3 191.58

    40!.!9 31.!7

    ,$mer o theoretical plates 438.44 !.!7

    444.19 8.8!

    35 384.13 08.7

    37.11 07.55

    440.5 43.4

    !53.! 90.84

    :;Connell;s correlation. 58.41 71.58

    )or #iscosity /e have

    0.17448!!103

    .1341955!7

    a 0.37388550

    *o !0 ?

    /"tual Number of 1ras:

    35

    0.!

    (ct$al @lates

    ,th

    late "ien" "al"ulation &o):

    olar avg #iscosity 6a m,sm

    elative volatility 'a

    rom :;Connell;s graph or eAciency o the col$mn %*o'

    ,th

    *o

    ,th*

    o

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    , 58.333333333

    , 59

    7eed-point lo"ation:

    sing "rikride empirical e+$ation

    here B 140 lmolhr

    915.4 lmolhr

    log %,r,s' -0.085755998,r,s 0.8081577

    @lates in stripping section %Belo/ the eed'

    ,,r6,s

    ,r6,s 59

    ,s 3.40311537

    ,s 33

    @lates in rectiying section %(ove the eed'

    ,r ,-,s

    ,r !

    )eed-point 7

    Column Diameter Cal"ulation:

    )looding velocity can e estimated rom the correlation given y )air

    here is the 2ooding velocity ased on net area (n

    (t this stage /e need to nd the li+$id-vapor 2o/ actor )D#

    or top and otto

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    (ss$me tray spacing o 0.5 m

    8e"tifin# e"tion:

    )ollo/ing are the necessary physical properties or iameter calc$lation take

    10.9!

    54.5

    G 9.41! dynecm or 0.00941!

    D/ 45!70 kghr

    #/ 70180 kghr

    0.0949!01!

    rom graph

    0.07

    0.0!01

    ,o/ the 2ooding velocity

    0.4193030581 ms

    esign or 85? 2ooding at maim$m 2o/ rate

    aim$m allo/ale vapor velocity ased on the net col$mn cross sctional ar

    0.35!4075993 ms

    aim$m vol$metric 2o/ rate !403

    1.778!11

    ,et (rea re+$ired (n 5.0

    Take do/ncomer area as 1? o the total cross sectional area

    Hv "gm3

    HD "gm3

    )D#

    "1

    or val$es other than 0.0,m s$race tension a correction is applied or "1

    "1

    v = 0.85

    v

    m3hr

    m3s

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    Total col$mn cross sectional area (c 5.!7

    iameter o the col$mn I%%(t J4'K'

    ia .!8!90!7354 m or 8.8

    9.0

    trippin# e"tion:

    )ollo/ing are the necessary physical properties or iameter calc$lation take

    13.87

    5!0

    G 8.!1 dynecm or 0.008!1

    D/ 117!00 kghr

    #/ !78!0 kghr

    0.77399!1

    rom graph

    0.0!5

    0.05

    ,o/ the 2ooding velocity

    0.3417!1918 ms

    esign or 85? 2ooding at maim$m 2o/ rate

    aim$m allo/ale vapor velocity ased on the net col$mn cross sctional ar

    0.90497!303 ms

    aim$m vol$metric 2o/ rate 4891

    1.358!11

    ,et (rea re+$ired (n 4.7

    Hv "gm3

    HD "gm3

    )D#

    "1

    or val$es other than 0.0,m s$race tension a correction is applied or "1

    "1

    v

    = 0.85

    v

    m3hr

    m3s

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    Take do/ncomer area as 1? o the total cross sectional area

    Total col$mn cross sectional area (c 5.31

    iameter o the col$mn I%%(t J4'K'

    ia .!01187735 m or 8.5Both diameters diLer less than 0?M thereore /e /ill have same diameter t

    ThereoreM governing iameter 9

    late /reas:

    (c Total col$mn cross seectional area

    (c 5.91

    (d Cross sectional area o do/ncomer 1? o (c

    (d 0.7093039

    (n ,et area availale (c-(d %or single pass'

    (n 5.0

    (a (ctive or $ling area (c-(d

    (a 4.493!15148

    (h &ole area normally 10? o (a

    (h 0.4493!1515

    9eir Dimensions:

    ecommended val$es or col$mns operating aove atmospheric press$re o

    h/ 40-50mm

    h/ 50 mm

    Neir length o 0.77 times c is recommended or /e can $se graph or /eir l

    (d(c 0.1 or 1

    )rom graph the ratio

    m

    m

    m

    m

    m

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    l/c 0.77

    l/ .11!3934 m or

    Number of tra passes:

    or top section

    li+ 2o/ 370.!gpm

    /eir length l/ 83.1!00445 inatio 4.45!4!719! gpmin o /eir

    or ottom section

    li+ 2o/ 94.3gpm

    /eir length l/ 83.1!00445 in

    atio 11.114719!8 gpmin o /eir

    Both top and ottom li+$id 2o/ rate are in the given recommended range.

    Fo /e have selected singe pass cross 2o/ /ith sgmental do/ncomer.

    t.er tra spe"i;"ations:

    (ss$med tray spacing 0.5 m

    &ole diameter 5 mm

    @late thickness 5 mm or caron steel

    1ra

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    aim$m ho/ !8.53!3 mm o li+

    inim$m ho/ 54.01 mm o li+

    (t minim$m rate h/6ho/ 104.0mm

    )rom graph 31

    minim$m design vapor velocity P 3.39397!597!

    (ct$al minim$m vapor velocity inim$m #apor rate(h

    .11!98855

    late pressure drop:

    @late press$re drop is given y

    rst /e calc$late dry plate press$re drop

    @late thickness&ole diameter 1

    @ercent perorated area

    0.1 or

    rom graph 0.84

    maim$m vapor velocity thro$gh holes 3.04!9317

    no/ 1!.373478957

    esid$al head is given y

    hr .3148571 mm o li+

    The total plate drop is given y hthd6hr6%h/6ho/'

    ht 157.185337 mm o li+

    no/ Q@ 8!3.!9573!71 or

    or total press$re drop across all trays

    Do=n"omer li>uid ba"?up:

    "

    or orice coeAcient Co/e $se graph

    Co

    h

    hd

    ,m

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    1otal Number of .oles:

    ,$mer o holes (hah

    here ah area o one hole

    dh 5 mm

    ah

    ah 1.9!375*-005

    ,$mer o holes 87!.44310!

    877 holes

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    tilities are:

    tively.

    8elative Volatilit

    .79999!!!17

    .1341955!7

    1

    0.58381331!

    0.540717709

    0.47!543!!

    0.40477134

    0.3!815193

    0.94134!5

    0.3!45751940.137097595

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    o

    &'i ( Xid)*&'i - +)

    0.9578011419

    1.4!85400578

    -0.03975

    0

    0

    0

    0

    00

    0

    0

    0

    0

    0

    0

    0

    0

    00

    .38!5911998

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    m or constant "1

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    n rom &EFEF

    ,m

    ea

    m

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    t

    t

    n rom &EFEF

    ,m

    ea

    m

    m

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    t ro$gh o$t the col$mn.

    t

    Neir &eight

    ngth

    ?

    m

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    83.1!004453 in

    $tlet/eir .

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    ms

    ms

    10 ?

    ms

    mm o li+

    0.8!3!9573!7"@a

    50.9580484!!1 "@a

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    pM /hichever is smaller

    r area

    Fetisactory

    ty ased on net area'

    Fetisactory

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    m

    m

    m

    mmplate

    m

    m

    t

    t


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