Evaluation of Mass Transfer coefficient in a wetted wall column
Objective: The rates of diffusion into gases flowing through pipes are studied in wetted wall column.
Principle/Theory:
A thin film of liquid falling down the inside of a vertical pipe through which the gas flows, constitutes a wetted wall column. Wetted wall columns have been used as absorbers for Hydrochloric acid, Ammonia, Acetone, Benzene and other volatile liquids. They have also been studied for theoretical studies for mass transfer because the interfacial surface between the phases is kept under control and is measurable.
The height of wetted wall column required for mass transfer operations is excessive and consequently this is not widely used, where large quantities of liquid or gas have to be handled, it would be necessary to arrange many vertical pipes in parallel and this leads to difficulties in the distribution of liquid into the inner surface of the tubes. The gas pressure drop for this is confined to skin friction effects, with few or no expansion or contraction losses
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The rates of diffusion into gases flowing through pipes have been studied in wetted wall columns.
A volatile liquid is submitted to flow down the inside surface of a circular tube, while a gas flows upward or downward through the center of the pipe. Measurement of the rate of evaporation of a liquid into the gas stream over known surface permits calculation of mass transfer coefficient for the diffusion of vapor into gas stream. Since the liquid is pure, the concentration gradient for diffusion exists entirely within the gas phase , the mass transfer coefficient Kg may be calculated. Sherwood and Gillard conducted a series of experiments using a variety of volatile liquids with air in turbulent flow.
The equation which describes all the data for both liquid and gas flow is
(K_{G} d/DW (P_{BM}/P) (K_{l}d/D) = 0.023 Re^{0.83 }Sc^{1/3}
^{ } This empirical relation is quite remarkable in the manner in which it generally confirms the relationship between heat mass and momentum transfer developed theoretically. However, the evaporation of the volatile liquids in a wetted wall column results in cooling of the liquids and consequent simultaneous heat transfer between liquid and gas. The heat transfer rates are given by the equation
hd / k = 0.023 Re^{0.8 }Pr^{0.3}
Equipment used: Wetted Wall column unit, Humidity meter
Material used: Water
EXPERIMENTAL PROCEDURE:
EXPERIMENTAL PROCEDURE:
2. The blower is started and minimum flow of air is maintained.
3. After about 5 minutes, when steady state condition reaches, the humidity of air at inlet and outlet are determined by the readings of the wet and dry bulb thermometers and by the use of a psychometric chart.
4. Water flow rates and inlet and outlet temperatures are noted.
5. Vapor pressure of water at different water temperatures is calculated.
6. Calculations are made at different flow rates and values of Kg Vs N_{Re} are plotted on a loglog scale.
OBSERVATIONS:
S.No

Air flow rate from M^{2} Qa lpm

Water flow rate Qw lpm

Air temperature

Water temperature ^{0}C

Air PD mm H_{2}0 across orifice
 
Inlet

Outlet

T1 T2

M1 M2
 
T_{d1}t_{w1}

T_{d2} t_{w2}
 
1
 
2

Length of the tube =
Diameter of tube =
From the readings, T_{d1, }t_{w1 }and T_{d2} , t_{w2 }and from a psychometric chart,_{ }
Partial pressure_{ }of water vapor at inlet = P1 KN/m2
Partial pressure of water at outlet = P_{B} KN/m2
DATA ANALYSIS:Partial pressure of water at outlet = P_{B} KN/m2
Mean air pressure in column P_{t }= P_{B} *(DP1/2)X1000/13600*1.013*100/760 KN/m2
Air flow rate =
9.22 X^{ }SQRTDP2/10^{6} kgmoles/sec
9.22 X^{ }SQRTDP2/10^{6} kgmoles/sec
Driving force at inlet of air= Dp_{W1} = PW1 –pw1
Where,
pw1 =pure component vapor pressure of water at outlet water temp T1
PW1 = Partial pressure of water at bottom
Driving force at outlet of air
DpW1 = PW2 –pw2
where,
pw1 =pure component vapor pressure of water at outlet water temp T2
PW2= Partial pressure of water at the top of column
DPwm = (DpW1  DpW2)/ ln (DpW1/DpW2)
Amount of water evaporated
NW = QA* (pw2/Pt – pw1/Pt)
In terms of mass transfer coefficient Kg, the rate of mass transfer is given by
Nw = KG * A* DPwm
where A = p DL m2 where d = i.d of column and L = Effective length of column
For each flow rate of air ,Kg can be calculated.
Pam = (Pt – pw1) – (Pt –Pw2)/ ln (Pt – pw1/ Pt –Pw2) is also calculated
To plot Gillard correlation, Kg * (d/DW)* (Pam/Pt) * (rADw/m_{air}) ^{0.44}
Where Dw = diffusivity of water vapor in air = 0.13X10^{4} m^{2}/sec
m_{air }=viscosity of air = 1.85X 103 kg/m/sec
Nre = dG/ mair = d.Q_{A}.A_{C}/m_{air }
Ac_{ }=cross section area of column
d = diameter of column
Kg * (d/DW)* (Pam/Pt) * (rADw/m_{air}) ^{0.44 } Vs N_{re} is plotted on a log –log sclae.
This value is compared with reported values.
RESULTS:
Reported value =
Calculated value =
Wetted Wall Column Set Up 
The above setup is used to calculate experimental mass transfer coefficient of the liquid and gas system at different temperature and different flow rates; of course the main application of wetted wall is to determine the data of the gas and liquid mass transfer coefficient.
Blower is provided with two valves at suction so that when the studies are focused on vapors of chemical substance which are
stored in a storage vessel and the vapors from the vessel are sucked by the blower and passed into the column or if the vapors are required to be mixed with air than an option at the discharge line of the blower which is facilitated with nozzle helps in mixing the vapor with air.
stored in a storage vessel and the vapors from the vessel are sucked by the blower and passed into the column or if the vapors are required to be mixed with air than an option at the discharge line of the blower which is facilitated with nozzle helps in mixing the vapor with air.
A heater is provided at the discharge line to supply heat to the vapor or air to maintain the temperature of the system and whole pipeline is insulated to prevent loss, by using the rotameter, flow rate of the vapor can be controlled.
PSYCHROMETRIC CHARTS 