How Can You Calculate the Drying Time of a Spherical Granule?

  • Thread starter Thread starter gfd43tg
  • Start date Start date
  • Tags Tags
    Drying Spherical
AI Thread Summary
The discussion centers on calculating the drying time of a porous spherical granule, focusing on the diffusion of water vapor as the granule dries. The drying time formula is derived, incorporating parameters such as granule radius, temperature, pressure, and vapor pressure. Participants discuss the integration of mass transfer equations, emphasizing the need to account for spherical geometry in the calculations. One user initially struggles with the problem but ultimately resolves it by correctly applying the principles of diffusion and pressure relationships. The conversation highlights the complexities of mass transfer in drying processes.
gfd43tg
Gold Member
Messages
947
Reaction score
48

Homework Statement


Fig. below shows the cross-section of a porous spherical granule of radius a. The pores are initially saturated with water. The granule dries in air at pressure P and temperature T. The drying rate is controlled by diffusion of water vapor through the dry region B; the shrinking core A has the original moisture content ##\rho## kmol per unit granule volume.

Using the equation within the region B, ##N_{1}c_{2} - N_{2}c_{1} = -DC \frac {dc_{1}}{dr}## show that the drying
time is
$$ \frac {\frac {\rho a^{2} R T}{6DP}}{ ln \Big(\frac {P}{P-P^{*}} \Big)} $$
where p* is the vapor pressure.

For a granule 10 mm in diameter, the drying time at 25 °C is 20 hours, the initial
water content being 50 mg; P = 1 bar, p* = 0.032 bar. Estimate D.

Homework Equations

The Attempt at a Solution


I am having a lot of problems solving these mass transfer problems, I am lacking intuition for the problem

So I start with the equation
$$N_{1}c_{2} - N_{2}c_{1} = -DC \frac {dc_{1}}{dr}$$
I am thinking 1 refers to water and 2 refers to air. I think the flux of air into the water, ##N_{2}##, is negligible since air is not very soluble in water, thus I am saying that term is zero, leaving me with
$$N_{1}c_{2} = -DC \frac {dc_{1}}{dr} $$
substituting ##c_{2} = C - c_{1}##
$$N_{1}(C - c_{1}) = -DC \frac {dc_{1}}{dr} $$
rearranging and integrating,
$$ \int_{\rho}^{0} \frac {dc_{1}}{C-c_{1}} = - \frac {N_{1}}{DC} \int_0^a dr $$
$$ln \Big(\frac {C}{C - \rho} \Big) = - \frac {N_{1}}{DC}a$$

From here I don't know where I will get those pressure terms
 

Attachments

  • 4.4.png
    4.4.png
    3.2 KB · Views: 429
Last edited:
Physics news on Phys.org
Maylis said:
I am having a lot of problems solving these mass transfer problems, I am lacking intuition for the problem

So I start with the equation
$$N_{1}c_{2} - N_{2}c_{1} = -DC \frac {dc_{1}}{dr}$$
I am thinking 1 refers to water and 2 refers to air. I think the flux of air into the water, ##N_{2}##, is negligible since air is not very soluble in water, thus I am saying that term is zero, leaving me with
$$N_{1}c_{2} = -DC \frac {dc_{1}}{dr} $$
substituting ##c_{2} = C - c_{1}##
$$N_{1}(C - c_{1}) = -DC \frac {dc_{1}}{dr} $$
You're good up to here. Nice job and nice reasoning.

But, N1 is a function of r in your problem (so the integrations are incorrect). This is very similar to the problem you were doing the other day for evaporation of a drop. The above equation applies in the region between r = x and r = a. You need to take into account the spherical geometry, just like the problem the other day. 4πr2N1 is constant in this region. You need to express the C and c in terms of the total pressure P and the partial pressure of water vapor (which is equal to the equilibrium vapor pressure at r = x), respectively. You need to solve for 4πr2N1, which is the rate at which water is leaving the inner core.

Chet
 
  • Like
Likes gfd43tg
Thanks, solved it now
 
Back
Top