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

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SUMMARY

The drying time of a spherical granule can be calculated using the equation $$ \frac {\frac {\rho a^{2} R T}{6DP}}{ ln \Big(\frac {P}{P-P^{*}} \Big)} $$, where P is the pressure, P* is the vapor pressure, and D is the diffusion coefficient. For a granule with a diameter of 10 mm and an initial water content of 50 mg, the drying time at 25 °C is determined to be 20 hours. The discussion highlights the importance of understanding mass transfer principles and the role of spherical geometry in the drying process.

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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
 

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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
 
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Thanks, solved it now
 

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