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    1.0 ABSTRACT

    Regarding to the experiment objectives which is to determine the diffusivity of the vapour of

    acetone and to study the effect of temperature on the diffusivity, this experiment is based on

    the mass transfer theory. The instrument used is the Gas Dispersion Apparatus that consists

    of an acrylic assembly which is sub-divided into two compartments. One compartment is

    constructed from clear acrylic and is used as a constant temperature water bath. The other

    compartment is incorporates an air pump and the necessary electrical controls for the

    equipment. The experiment is run by using two difference temperatures in order to study the

    effect of temperature on the diffusivity of the vapour of acetone. At temperature of40C, the

    diffusivity of acetone that obtained is 6.17 x m2/s. Meanwhile, at temperature of 50C,

    the diffusivity of acetone that obtained is 2.252 x m2/s. This experiment showed that

    gas diffusivity decreased with increasing temperature. However, supposedly the temperature

    increase with the diffusivity of the vapour of acetone increases as well.

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    2.0 INTRODUCTION

    Figure 1: Gaseous Diffusion Apparatus

    Gaseous diffusivity or gas dispersion apparatus which involves diffusion with bulk flow is

    one of the items of laboratory equipment that have been designed to allow measurement of

    molecular diffusivities and also to make the students become more familiar with the basic

    notions of mass transfer theory. This apparatus is a bench mounted apparatus for the

    determination of diffusion coefficients of a vapour in air, which uses the method

    of measuring the rate of evaporation of a liquid through a stagnant layer into a flowing

    air stream, comprising a precision bore capillary tube, which may be filled from a syringe and

    the top of which means are provided to pass air (or an inert gas) stream to remove vapour.

    The apparatus also comprise an air pump, a travelling microscope with accurate focus

    adjustment and mounted for vertical axis movement against a Vernier scale and a

    thermostatically controlled water bath, in which to place the capillary tube, capable

    of accurate temperature control.

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    The experimental capabilities of this apparatus are direct measurement of mass transfer rates

    in the absence convective effects, use of a gas laws to calculate concentrations differences in

    terms of partial pressures, use of Ficks Law to measure diffusion coefficients in the presence

    of a stationary gas, measurement of the effect of temperature on diffusion coefficients and

    gaining familiarity with the use of laboratory instruments to achieve accurate measurements

    of data required for industrial process design.

    The diffusivity of the vapour of a volatile liquid in air can be conveniently determined by

    Winklemanns method in which liquid is contained in a narrow diameter vertical tube,

    maintained at a constant temperature, and an air stream is passed over the top of the tube to

    ensure the partial pressure of the vapour is transferred from the surface of the liquid to the

    air stream by molecular diffusion. The molecular diffusivity, D, is a kinetic parameter

    associated with static and dynamic conditions of a process. All the complexity and

    unwieldiness of many calculations is, indeed, connected with the determination of this

    quantity.

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    3.0 OBJECTIVES

    The objective of this experiment is:

    3.1 To determine the diffusivity of the vapour of acetone.

    3.2 To study the effect of temperature on the diffusivity.

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    4.0 THEORY

    The diffusion of vapour A from a volatile liquid into another gas B can be conveniently

    studied by confining a small sample of the liquid in a narrow vertical tube and observing its

    rate of evaporation into a stream of gas B passed across the top of the tube. Normally, for

    simple instructional purposes, gas B is air and vapour A is an organic solvent such as acetone

    or methyl alcohol.

    The apparatus consist essentially of a glass capillary tube placed in a transparent-sided

    temperature controlled water bath. A horizontal glass tube is fixed to the upper end of the

    capillary tube and air is blown through this by a small air pump included within the unit. This

    arrangement allows the maintenance of a partial pressure difference within the capillary

    tube between the evaporating liquid surfaces and the flowing air stream. A travelling

    microscope, with sliding vernier scale, is mounted on a rigid stand alongside the thermostatic

    bath and is used to measure the rate of fall of the solvent or air meniscus within the capillary.

    The relation between the measured molar mass transfer rate (N Aper unit area), the partial

    pressure gradient and the diffusion coefficient, D is deduced based on the following;

    ... Equation [1]

    Where D = Diffusivity (m2/s)

    CA = Saturation concentration at interface (kmol/ m3)

    L = Effective distance of mass transfer (mm)

    CBm = Logarithmic mean molecular concentration of vapour (kmol/ m3)

    CT = Total molar concentration = CA + CBm (kmol/ m3)

    N A = D {CA/L}{CT/CBM}

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    Considering the evaporation of the liquid:

    . Equation [2]

    Where is the density of liquid

    Thus,

    . Equation [3]

    Integrating and putting L - Lo at t = 0

    Equation [4]

    Lo and L cannot be measured accurately but L-Lo can be measured accurately using

    thevernier on the microscope

    . Equation [5]

    Or

    where:

    M = molecular weight (kg/mol)

    t = time(s)

    where

    s are the slopes of a graph t/(L-L0) against L - Lo then:

    NA = {L/M}{dL/dt}

    {L/M}{dL/dt} = D {CA/L}{CT/CBM}

    L2L20 = {2DM/L}{(CACT)/CBm}t

    (LL0)(L-L0+2L0) = {2DM/L}{(CACT)/CBm}t

    t/(L-L0) = {L/2MD}{ CBm/( CACT)}(L-L0) + {(L CBm)/( CACTMD)}L0

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    . Equation [6]

    .... Equation [7]

    s = (L CBm)/( CACT2MD)

    D = (L CBm)/( CACT2sM)

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    5.0 PROCEDURES

    1. The capillary tube is partially filled with acetone to a depth of approximately 35mm.the top nut was removed from metal fitting.

    2. Carefully, the capillary tube was inserted through the rubber ring, inside the metal nutuntil the top of the tube rests on the top of the nut.

    3. Gently the assembly is screwed onto the top plate, with the T piece normal to themicroscope. The flexible air tube was connected to one end of the T piece. The

    object lens is adjusted to within 20-30 mm from the tank.

    4. The vertical height of the microscope was adjusted until the capillary tube is visible.When the meniscus has been determined, the vernier scale should be aligned with asuitable graduation on the fixed scale.

    5. Then, the air pump was switched on.6. The level inside the capillary tube was recorded.7. The temperature controlled water bath was switched on and a steady temperature was

    obtained.

    8. The reading was taken every 5 minutes for 10 times. The experiment was done attemperature 45C and 50C.

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    6.0 APPARATUS AND MATERIALS

    6.1 Apparatus

    Figure 2: Gaseous Diffusion Apparatus

    1) TR 14 Membrane Test Unit apparatus.2) 500 mL beakers.3) Electronic balance.4) Gloves5) Ruler

    6.2 Materials

    1) Acetone2) Sodium Chloride3) Water

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    7.0 RESULTS

    Intial Length, Lo = 10.3

    Temperature, T = 45C

    Time, t (kilosecond, ks) (LoL) (mm)

    (ks/mm)

    0.3 0.3 1.00

    0.6 0.6 1.00

    0.9 1.0 0.90

    1.2 1.3 0.92

    1.5 1.8 0.83

    1.8 2.1 0.86

    2.1 2.4 0.88

    2.4 2.7 0.89

    2.7 3.0 0.90

    3.0 3.4 0.88

    Table 1

    Intial Length, Lo = 7.30

    Temperature, T = 50C

    Time, t (kilosecond, ks) (LoL) (mm)

    (ks/mm)

    0.3 0.3 1.00

    0.6 1.0 0.60

    0.9 1.6 0.56

    1.2 0.8 1.50

    1.5 1.3 1.15

    1.8 2.8 0.64

    2.1 2.8 0.75

    2.4 3.3 0.73

    2.7 3.8 0.71

    3.0 4.3 0.69

    Table 2

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    8.0 CALCULATIONS

    8.1 Sample calculations

    8.1.1 Time from commencement of experiment:

    x

    1000 = 0.3ks

    Liquid level (LLo) : = 0.3

    =

    = 1.0 ks/mm

    8.1.2 Calculation on diffusivity, D (T = 40 C )

    Figure 3: Graph of

    against LoL

    Density of acetone, = 790 kg/ Gas constant, R =

    Molecular weight of acetone =

    Vapor pressure, Pv = 56 kN/m3 Slope, s = 0.036 = 3.6 x

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    Assume standard conditions (P = 101.32 kN/, V=22.4 , T = 273 K) Tempereature, Ta = 40 C = 313 K

    CT = (1/V )(T / Ta ).. Equation [8]

    = (1/22.4)(273/313)

    = 0.0389 kmol/m3

    CB1 = CT = 0.0389 kmol/m3

    To find CB2 :

    CB2 = (PaPv / Pa)CT... Equation [9]

    = (101.32-56/ 101.32) 0.0389

    = 0.0174 kmol/m3

    To find CBM :

    CBM = (CB1-CB2)/ln (CB1/CB2).... Equation [10]

    = (0.03890.0174)/ln (0.0389/0.0174)

    = 0.0267

    To find Ca :

    Ca = (Pv/Pa)CT.. Equation [11]

    = (56/101.32) 0.0389

    = 0.0215 kmol/m3

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    To find diffusivity,D :

    ......... Equation [7]

    D = (790)(0.0267/3.6 x (2x58.08x0.0215x0.0389)

    D = 6.17 x m2/s

    Calculation steps is repeated to find diffusivity, D at T = 50 C

    D = (L CBm)/( CACT2sM)

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    8.1.3 Calculation on diffusivity, D (T = 50 C )

    Figure 4: Graph of

    against LoL

    Assume standard conditions (P = 101.32 kN/, V=22.4 , T = 273 K) Tempereature, Ta = 50 C = 323 K

    CT = (1/V )(T / Ta ).. Equation [1]

    = (1/22.4)(273/323)

    = 0.0377 kmol/m3

    Density of acetone, = 790 kg/ Gas constant, R =

    Molecular weight of acetone =

    Vapor pressure, Pv = 56 kN/m3 Slope, s = 0.1 = 1.0 x

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    CB1 = CT = 0.0377 kmol/m3 .. Equation [2]

    To find CB2 :

    CB2 = (PaPv / Pa)CT..Equation [3]

    = (101.32-56/ 101.32) 0.0377

    = 0.0169 kmol/m3

    To find CBM :

    CBM = (CB1-CB2)/ln (CB1/CB2) Equation [4]

    = (0.0377 - 0.0169)/ln (0.0377/0.0169)

    = 0.02597

    To find Ca :

    Ca = (Pv/Pa)CT.. Equation [5]

    = (56/101.32) 0.0377

    = 0.0208 kmol/m3

    To find diffusivity,D :

    D = CBM /s(2MCa CT)... Equation [6]

    D = (790)(0.02597/1.0 x (2x58.08x0.0208x0.0377)

    D = 2.252 x m2/s

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    9.0 DISCUSSIONS

    In this gas diffusion experiment, equipment used was the Gaseous Diffusion Apparatus

    [Model: CER-A (ARMFIEL)]. This equipment has been designed to study the application of

    mass transfer focussing on the gas diffusion.

    This experiment was conducted to realize the main objectives which are to study the gas

    diffusion coefficient and its relationship with the change in temperature. The manipulating

    variable involved is the temperature and the responding variable was the level inside the

    capillary tube, L which was taken every 0.3 ks until 3.0 ks was reached. This experiment was

    carried out for two different temperatures which are at 40 C and 50 C with respect to gas

    diffusivity. In particular, gas diffusivity of vapour acetone is calculated.

    Utilizing the data obtained, graph of

    against LoL was plottedas shown in Figure 3 and 4.

    From both of these graph, the gradient or also known as the slope,s was calculated. However,

    due to the present of errors, data collected has shown to deviate variedly. A linear graph was

    not able to be obtained and thus to overcome this problem the slope,s was calculated taking

    from two points relative to the line obtained.

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    The calculations were proceeds with the aim to find the diffusivity of vapour acetone at

    different temperature. It was based on the data collected for T = 40 C, D equivalent to 6.17 x

    m2/s while at T = 50 C, D was found to be 2.252 x m2/s. This result has proven

    that as the temperature increase, the diffusivity decreases which opposes the principle of gas

    diffusion from this experiment. Supposedly, the diffusivity of vapor acetone increase with

    increasing temperature. Diffusion is the movement of molecules from area of high

    concentration to area of lower concentration and this is increased with increasing

    temperature which means when the temperature increase the diffusion will speeds up. This

    explained when temperature is higher, then the rate of diffusion would probably increase

    caused by increasing kinetic activity of the solution. However, due to this

    inaccuracy, values for gas diffusivity calculated using Equation [7] may not explain correctly

    the definition of gas diffusion.

    It has then clearly proved that errors arose during this experiment. Firstly, error mentioned

    may be classified as a parallax error. This occurence is especially when data taken for the

    level inside the capillary tube was performed. Besides that, inaccurate time relay may causes

    human error due to lack in focus in conducting the experiment. Stabilizing of temperature

    was also unable to achieve during the experimnent therefore deviating the data obtained.

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    10.0 CONCLUSION

    As a conclusion, the result for diffusivity coefficient at 40 C is -2504.53 m 2/s and the

    diffusivity coefficient at 45 C is -3650.55 m

    2

    /s. There are some errors when the experiment

    was done. Some of recommendations step should be taken otherwise the result for diffusivity

    would not be accurate. To sum up, the experiment had been done with quite accurate results

    although some error happened.

    11.0 RECOMMENDATIONS

    Some recommendations should be implements in this experiment. One of them is insulating

    the glass container. It will maintain the temperature through the experiment and the heat will

    not loss to the surrounding. Next, the reading meter should be stabilized with the person who

    read the meter. The person who read it should be at the same level to the meter. By doing

    this, parallax and reading error can be minimized.

    12.0 APPLICATIONS

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    All gas diffusion methods are based on interfacing the donor stream containing the analytic,

    with an acceptor stream containing a reagent. The porous hydrophobic membrane serves as a

    barrier that allows only the gaseous species passed through. This makes the gas diffusion

    methods very selective, since the non-volatile species will not reach the detector. The

    instrumental setup can be configured in two ways:

    1. The continuous programmable flow method where both donor and acceptor streamare continuously pumped.

    2. The stopped flow technique where both donor and acceptor stream are controlled bysyringe pumps.

    The gas diffusion unit for continuous flow has diffusion path 2 cm long and 2 mm wide. The

    acceptor stream is monitored by a flow cell with 10 cm long light path. The flow injection

    system is operated at a programmable flow rate of 0.75mL/min per channel while the sample

    passes through the diffusion unit and at a flow rate of 3.0mL/min during flush period. The

    injection volume is 300 microliters of sample and sampling frequency is 40 injections per

    hour.

    The stop flow method uses the sandwich gas sensor, where the injected analytic is in contact

    with the gas diffusion membrane during the stopped flow period. It yields higher sensitivity

    and consumes far less of sample and reagents then continuous flow method.

    The Sandwich Gas Diffusion Sensor uses a pair of optical fibres that monitor the acceptor

    solution adjacent to the diffusion membrane. The stop flow FI technique is robust, since it

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    uses syringe pumps, and therefore suitable also for continuous monitoring. Sensitivity of this

    method is easily adjusted by selecting the duration of the stopped flow time, while using the

    same experimental setup and reagent concentrations. The Sandwich Sensor provides response

    in real time, since it monitors the kinetics of the diffusion and of the subsequent chemical

    reaction and uses smaller volumes of sample than the continuous flow method.

    Figure 6

    Figure 5

    13.0 REFFERNCES

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    Journal of Physical and Chemical Reference Data. Gaseous Diffusion Coefficients.Retrieved November 15, 2012 from

    http://jpcrd.aip.org/resource/1/jpcrbu/v1/i1/p3_s1?isAuthorized=no

    Gases: Grahams Laws of Diffusion and Effusion. Grahams Law. RetrievedNovember 15, 2012 from

    http://www.chem.tamu.edu/class/majors/tutorialnotefiles/graham.htm

    Diffusion of Gases. Diffusion and Effusion. Retrieved November 16 2012 fromhttp://chem.salve.edu/chemistry/diffusion.asp

    USEC. Gaseous Diffusion. RetrievedNovember 16, 2012 fromhttp://www.usec.com/gaseous-diffusion

    Advancing the Chemical Sciences. Learn Chemistry: Diffusion of gases of ammoniaand hydrogen chloride. Retrieved November 16, 2012 from http://www.rsc.org/learn-

    chemistry/wiki/TeacherExpt:Diffusion_of_gases_-_ammonia_and_hydrogen_chloride

    14.0 APPENDIX

    Refer attachment on the next page (page 22)

    http://jpcrd.aip.org/resource/1/jpcrbu/v1/i1/p3_s1?isAuthorized=nohttp://www.chem.tamu.edu/class/majors/tutorialnotefiles/graham.htmhttp://chem.salve.edu/chemistry/diffusion.asphttp://www.usec.com/gaseous-diffusionhttp://www.rsc.org/learn-chemistry/wiki/TeacherExpt:Diffusion_of_gases_-_ammonia_and_hydrogen_chloridehttp://www.rsc.org/learn-chemistry/wiki/TeacherExpt:Diffusion_of_gases_-_ammonia_and_hydrogen_chloridehttp://www.rsc.org/learn-chemistry/wiki/TeacherExpt:Diffusion_of_gases_-_ammonia_and_hydrogen_chloridehttp://www.rsc.org/learn-chemistry/wiki/TeacherExpt:Diffusion_of_gases_-_ammonia_and_hydrogen_chloridehttp://www.usec.com/gaseous-diffusionhttp://chem.salve.edu/chemistry/diffusion.asphttp://www.chem.tamu.edu/class/majors/tutorialnotefiles/graham.htmhttp://jpcrd.aip.org/resource/1/jpcrbu/v1/i1/p3_s1?isAuthorized=no