Mass Transfer in a wetted-wall column

Click For Summary
SUMMARY

The discussion focuses on mass transfer in a wetted-wall column, specifically the mass flux (φ) in relation to the mass transfer coefficients (k_L and k_g), partial pressures (p and p_∞), and concentrations (C and C_∞) of ammonia. The correct equations for mass flux are established as φ = k_i (C - C_α) and φ = k_ρ (P_α - P), with the relationship between concentration and partial pressure defined by Henry's law as C = PH. The final goal is to express φ as a function of C_α and P_α by eliminating C and P from the equations.

PREREQUISITES
  • Understanding of mass transfer coefficients (k_L and k_g)
  • Familiarity with Henry's law and its application
  • Knowledge of gas-liquid interface dynamics
  • Basic proficiency in algebraic manipulation of equations
NEXT STEPS
  • Study the derivation of mass transfer equations in wetted-wall columns
  • Explore the application of Henry's law in gas-liquid systems
  • Learn about the significance of mass transfer coefficients in chemical engineering
  • Investigate methods for calculating partial pressures in gas-liquid interactions
USEFUL FOR

Chemical engineers, process engineers, and students studying mass transfer phenomena in gas-liquid systems will benefit from this discussion.

Rogue
Messages
44
Reaction score
1
Homework Statement
Ammonia in gas is being absorbed by water in a wtted-wall column. At one level of the column, the following data applies:
Gas phase mass transfer co-efficient:
5.22 x 10^-9 kmol m^-2s^-1Pa^-1

Liquid Phase mass transfer coefficient:
3.88 x 10^-5 m s^-1

Henrys constant 0.955kPa (kmol m^-3)^-1


Use the following additional information to find the mass transfer flux in the column:

mole fraction of ammonia in liquid* 1.351 x 10^-3
mole fraction of ammonia in gas* 0.065
total pressure of system 1.013 bar
mole mass of ammonia 17
Relevant Equations
Attempt at solution

Using Ca =55.51xa

Ammonia in liquid:
55.51 x 1.351 x 10^-3
=0.075kmol^-3

Ammonia in gas:
55.51 x 0.065
=3.608kmol^-3


I know my end equation needs to be in the order of:
Na = kc x (Ca1 - Ca2)


I attempted:

=(4.42 x 10^-6) x (3.608 - 0.075)

= 1.562 x 10^-5


But have since been advised that I need to be calculating partial pressure, molar mass transfer flux and equivalent molar concentration and to substitute these into my final equation.
At this point, I am finding myself to be very confused.
Please can someone assist me as this particular question seems to have me completely confounded?
 
Physics news on Phys.org
Let:

##k_L## = mass transfer coefficient of ammonia in the liquid phase
##k_g## = mass transfer coefficient of ammonia in the gas phase
##p_{\infty}## = partial pressure of ammonia in the bulk of the gas phase
##p## = partial pressure of ammonia in the gas phase at the gas-liquid interface
##C_{\infty}## = concentration of ammonia in the bulk of the liquid phase
##C## = concentration of ammonia in the liquid phase at the gas-liquid interface
H = Henry's law constant

What is the mass flux ##\phi## in terms of ##k_L##, ##C_{\infty}##, and C?
What is the same mass flux ##\phi## interns of ##k_g##, ##p_{\infty}##, and p?
What is the relationship between p, C, and H?
 
Thanks for the response Chester.

Am I right in thinking?:

## \phi = k \iota (C - C \alpha)##

Answer = 1.371 x10^-4

## \phi = k \varrho (P - P \alpha)##

In terms of calculating partial pressure - I'll have to re-visit this to refresh my memory along with the relationship between p, C and H.
 
Rogue said:
Thanks for the response Chester.

Am I right in thinking?:

## \phi = k \iota (C - C \alpha)##
This equation is correct
## \phi = k \varrho (P - P \alpha)##
This equation is incorrect. It should read:$$\phi = k \varrho ( P \alpha-P)$$

So you have $$\phi = k_{\iota} (C - C _{\alpha})=k _{\rho} ( P _{\alpha}-P)$$
In terms of calculating partial pressure - I'll have to re-visit this to refresh my memory along with the relationship between p, C and H.
Henry's law relates C and P by: $$C = PH$$
Now, please eliminate C and P between these three equations, and express ##\phi## as a function of ##C_{\alpha}## and ##P_{\alpha}##.
 

Similar threads

  • · Replies 4 ·
Replies
4
Views
3K
Replies
7
Views
3K
  • · Replies 6 ·
Replies
6
Views
2K
  • · Replies 4 ·
Replies
4
Views
2K
  • · Replies 14 ·
Replies
14
Views
3K
  • · Replies 9 ·
Replies
9
Views
4K
  • · Replies 8 ·
Replies
8
Views
2K
  • · Replies 16 ·
Replies
16
Views
2K
  • · Replies 1 ·
Replies
1
Views
2K
  • · Replies 3 ·
Replies
3
Views
4K