CALCULATIONS Gas Difussion

download CALCULATIONS Gas Difussion

of 11

Transcript of CALCULATIONS Gas Difussion

  • 8/18/2019 CALCULATIONS Gas Difussion

    1/11

  • 8/18/2019 CALCULATIONS Gas Difussion

    2/11

    * - effective distance of mass transfer /m0

    T - total molar concentration

    kmol

    m3

    ¿0

    BM - logarithmic mean value of B / 

    kmol

    m3 0

    1vaporation of the liquid ,

     !’A -( ρ L

     M  )dL

    dt    %B'

    Where "  p* - density of liquid /kg

    m3 ¿

      M - molecular eight /kg

    kmol 0

    ombination of equation A and B ,

    % ρ L

     M  ¿

     

    dL

    dt    - ( %C  A

     L  ' %C T 

    C BM  '

    The *2 is at t - 2" the slope of plotting the graph oft 

     L− L0

     against % * # *2 ',

     3 - % ρ L

    2 MD ' %

    C BM 

    C  AC T 

    '

    The diffusivity ,

  • 8/18/2019 CALCULATIONS Gas Difussion

    3/11

    ( -

     ρ LC BM 

    2 MC  AC T s

  • 8/18/2019 CALCULATIONS Gas Difussion

    4/11

    4.0 DIAGRAM AND DESCRIPTION OF APPARATUS

    The 34*T15 6aseous (iffusion oefficient Apparatus consists of ater bath tank" capillary

    tube" air pump and travelling telescope. 7n ater bath tank" there are some additional parts that

    help this experiment orks such as heater W8" temperature sensor" temperature controller and

    level sitch. The purpose of heater W8 is to heat up the ater in the ater bath to the

    temperature desired. Temperature sensor is to measure the temperature by correlating the

    resistance of the element ith the temperature. Temperature controller is about controlling the

    temperature folloing the experimental temperature and ater bath itself can maintain a steady

    temperature so that there is no eddy current in the vertical tube and mass transfer takes place

    from the surface by molecular diffusion alone. !ext" the T9shape vertical capillary tube is used

    ith the air pump hich has been attached to the one end of the T9Tube. The purpose is to allo

    the maintenance of a partial pressure difference ithin the capillary tube beteen the evaporating

    liquid surface and the floing air stream. The travelling telescope equipped ith a vernier scale

    is used to measure the level of the acetone meniscus ithin the capillary

  • 8/18/2019 CALCULATIONS Gas Difussion

    5/11

    )76:;1 8

  • 8/18/2019 CALCULATIONS Gas Difussion

    6/11

    RESULTS

     Temperature = 50   ℃

     Lo=9mm  

     Time (ks) Time from

    commencem

    ent of 

    experiment, t

    (min)

    Liquid level (

     L− LO )

    (mm)

    t/(   L− LO )

    (ks/mm)

    Reading of 

    vernier, L

    (mm)

    000 000 000 000 000!"0 "00 !50 0#0 !05"$0 $00 %50 0&' !"5%&0 &00 500 0" !$0$#0 #00 #$0 05 !$&00 !00 !0& 05 !'&"0 !"0 !"0 0&0 "!0

    CALCULATIONS

    olecular *eig+t, = 5#0# kg/mol

     Temperature, T a  = 50   ℃  = %"% 

    -ressure,  Pa  = !0!% k./m

    mol volume = ""$ m

    ensit1,  ρ L  = '! kg/m

    2apour pressure,  Pv  = 5& n/m3

  • 8/18/2019 CALCULATIONS Gas Difussion

    7/11

    4solute temperature,|¿|T ¿  = "% 

    T |¿|

    T a¿

    C T =(   1 Kmol volume )¿

    ¿(   122.4mᶾ )( 273 K 323 K  )=0.03773 kmol /mᶾ

    Logarit+mic mean molecular concentration of vapour, C BM   (kmol/m)

    C B1=C T 

    C B1=0.03773 kmol /mᶾ

    C B2=( Pa− Pv

     Pa

    )C T 

    C B2=( 101.3kN /m²−56kN /m²101.3kN /m ²   )0.03773 kmolmᶾ  =0.01687 kmolmᶾ

    C BM =(C B1−C B2)

    ln

    (C B1

    C B2

    )

      =(0.03773

     kmol

    mᶾ −0.01687

     kmol

    mᶾ  )

    ln

    (0.03773kmol /mᶾ

    0.01687 kmolmᶾ   )

      =0.02592kmol

    mᶾ

    6aturation concentration at interp+ase, C  A kmol/mᶾ

  • 8/18/2019 CALCULATIONS Gas Difussion

    8/11

    C  A=( P v P a )C T 

    C  A=(  56kN /m²101.3 kN /m² )

    0.03773kmol

    mᶾ   =0.002086

    kmol

    mᶾ

    Graph of t versus liquid level

    0 " $ & # !0 !" !$0

    0!

    0"

    0%

    0$

    05

    0&

    0

    0#

    0'

    Liquid level (L-Lo) ()

    t!( L-Lo) ("s!)

  • 8/18/2019 CALCULATIONS Gas Difussion

    9/11

  • 8/18/2019 CALCULATIONS Gas Difussion

    10/11

    #ISCUSSION $

      T+is experiment *as conducted to otain t+e gas di7usion

    coe8cient of acetone using t+e 9inkelmann:s met+od ;n t+is experiment,t+e volatile liquid is +eated until it evaporated into free air stream T+e rateof di7usion can e oserved 1 t+e rate of decreasing of acetone level in t+etue 1 using a telescope i7usion is t+e movement of molecules from areaof +ig+ concentration to area of lo*er concentration and t+is is increased*it+ increasing temperature *+ic+ means *+en t+e temperature increaset+e di7usion *ill also rising up ;n t+e ot+er *ord, *+en temperature is+ig+er, t+en t+e rate of di7usion *ould proal1 increase caused 1increasing kinetic activit1 of t+e solution

    axis of t+e grap+ is t+e time taken divide 1 t+e di7erenceet*een t+e levels of acetone ;n addition, t+e trend of t+e grap+ isincreased proportionall1 T+e increasing t+e di7erence et*een t+e levels of 

    acetone, t+e increasing t+e time divide 1 t+e di7erence et*een t+e levelsof t+e acetone rom t+e calculation and t+e data from t+e tale, t+e value of di7usivit1 *as determined *+ic+ is %$$ m"/s

     T+e temperature controller *as set up at 50@A t+roug+ along t+eexperiment and it not een set e1ond 0@A ;t is ecause t+e oiling pointof t+e acetone is at 5&@A *+ere t+e process *+ere t+e p+ase of acetone

  • 8/18/2019 CALCULATIONS Gas Difussion

    11/11

    c+ange from liquid to vapor 9+en t+e temperature exceeds 0@A, t+e rate of evaporation is faster compare to temperature at t+e oiling point T+issituation can cause t+e prolem to t+e experimenter to collect t+e data ordi7erence of acetone level inall1, t+e discrepanc1 from t+e experimentaldata is t+e value of t+e time divide 1 di7erence et*een levels of acetoneet*een intervals is not increased constantl1 due to some errors suc+ asparallax error and t+e initial value of t+e acetone in t+e capillar1 tue *asnot read accuratel1