Question

Ammonia gas is diffusing at constant rate through a layer of stagnant air 1 mm thick....

Ammonia gas is diffusing at constant rate through a layer of stagnant air 1 mm thick. Conditions are fixed so that the gas contains 50% by volume of ammonia at one boundary of the stagnant layer. The ammonia at the other boundary is quickly absorbed and the concentration is zero. The temperature is 295 K and the pressure is 1 atm. If the diffusivity of ammonia in air is 0.18 cm2/s calculate the rate of diffusion of ammonia through the layer.

Homework Answers

Answer #1

The convective flux NA= XA*(NA+NB)+JA

where JA= flux due to diffusion =-DAB*dCA/dZ

given NB=0 ( stagnant film), CA=C*XA= Overall concentration*mole fraction

NA*(1-XA) =- DAB*dCA/dX =-DAB*C*dXA/dZ

which on integration gives

NA= DAB*C ln {(1-XA2)/(1-XA1)}/z

XA1 and XA2 are mole fractinos at point 1 and 2 respectively

where DAB= 0.18 cm2/s C=P/RT= 1/82.06cm3.atm/mole.K*298=4.089*10-5 moles/cm3

z= 1mm =0.1cm XA2= O and XA1=0.5 ( volume fraction =mole fraction)

N = 0.18cm2/s*4.089*10-5 moles/cm3*ln{(1/0.5)}/ 0.1= 5.101*10-5moles/cm2.sec

Know the answer?
Your Answer:

Post as a guest

Your Name:

What's your source?

Earn Coins

Coins can be redeemed for fabulous gifts.

Not the answer you're looking for?
Ask your own homework help question
Similar Questions
1. (a) For the diffusion of solute A through a layer of gas to an absorbing...
1. (a) For the diffusion of solute A through a layer of gas to an absorbing liquid, where the initial mole fraction (yAo) is 0.10 and the final mole fraction (yA) is 0.20. What is the transfer rate for one way diffusion? How does this compared to equimolar diffusion? (b) What is the value of the final mole fraction yA halfway through the layer if it is one way diffusion? 2.An open circular tank is 8 m in diameter contains...
Ammonia gas (A) and nitrogen gas (B) are diffusing in counterdiffusion through a straight glass tube...
Ammonia gas (A) and nitrogen gas (B) are diffusing in counterdiffusion through a straight glass tube 0.61m long at 298K and 101.32 kPa. The partial pressure of MH3is constant at 20.0kPa in one chamber and 6.666kPa in the other. If the diffusivity at 298K and 101.32kPa is 2.3*10^(-5)m^2/s a)What is the flux of ammonia b) Calculate the diffusion of ammonia if the diameter of the tube is 24.4mm.
Ammonia gas (A) is diffusing at steady-state through N2 (B) by equimolar counter-diffusion in a circular...
Ammonia gas (A) is diffusing at steady-state through N2 (B) by equimolar counter-diffusion in a circular conduit 1.22 m long at 25 degrees celsius and a total pressure of 101.32 kPa absolute. The partial pressure of ammonia at the left end is 25.33 kPa and 5.066 kPa at the other end. The conduit has a diameter of 0.0305 m at the left end and tapering uniformly to 0.0610 m at the right end. The diffusivity is 0.023 x 10–4 m2...
Ammonia gas is diffusing through N2 under steady-state conditions with N2 nondiffusing since its insoluble in...
Ammonia gas is diffusing through N2 under steady-state conditions with N2 nondiffusing since its insoluble in one boundary. The total pressure is 1.013 x 104 Pa and the temperature is 298 k. The partial pressure of NH3 at one point is 1.333 Pa and at the other point 20 mm away it is 6.666 x 103 Pa. The DAB for the mixture at 1.013 x 105 Pa and 298 K is2.30 x 10-5 m2/s. a) Calculate the flux of NH3...
4.1A membrane made of 0.1 mm thick soft rubber separates pure O2 at 1 atm and...
4.1A membrane made of 0.1 mm thick soft rubber separates pure O2 at 1 atm and 25oC from air at 1.2 atm pressure. Determine the mass flow rate of O2 through the membrane per unit area and the direction of flow. Molar flow rate of oxygen is given by: ???? = ???????? / ??? (????1 ? ????2 ) where S is solubility of oxygen in rubber. The mass diffusivity of oxygen in rubber at 298 K is DAB = 2.1...
The Noyes-Whitney equation is often used to predict the rate at which a solid substance dissolves...
The Noyes-Whitney equation is often used to predict the rate at which a solid substance dissolves into water. One form of this equation is: dC/Dt = k(CS-C) where k=DA/Vh . Here D is the diffusivity of the dissolving substance in the electrolyte, A is the area of the sample dissolving, h is the thickness of the diffusion boundary layer, V is the volume of electrolyte, C is the time-dependent concentration of the substance in the electrolyte and Cs is the...
ADVERTISEMENT
Need Online Homework Help?

Get Answers For Free
Most questions answered within 1 hours.

Ask a Question
ADVERTISEMENT