As part of a process to fabricate materials with ordered pore arrays, the diffusion‐limited solvent etching process shown in the figure below is used to remove a contaminant (solid solute A, lithium carbonate) from an array of pores within a slab. There are presently 16 cylindrical pores, each of 0.10 cm diameter and 0.5 cm depth, and the overall dimensions of the slab are 4.0 cm per side and 0.60 cm deep. Liquid solvent (species B) flows over the surface of the slab at a high rate so that the concentration of dissolved solute A is essentially zero. Further, the dissolved solute A is not very soluble (sparingly soluble) in solvent B. The process is carried out at ambient conditions (25oC, 1.0 atm). Other potentially useful information: maximum solubility of solute A in solvent B, C*A = 90 µmole/cm3, density of solvent B, ρB = 1.0 g/cm3, ρA,solid = 2.1 g/cm3, MA = 74 g/gmole, MB = 18 g/gmole, DAB = 1.6 × 10–5 cm2/s. A. Initially, the solid solute A is loaded to a depth of 0.20 cm within each 0.5 cm length pore, as shown in the figure below. At this point, what the total transfer rate of solute A out of the entire slab, in units of µmole/s? B. How much time will it take for all the solid solute A to be removed from each pore, in units of hours? C. The process takes a long time. What changes to the process parameters such as (i) pore diameter, (ii) diffusion path length, and (iii) process temperature would likely reduce the time required? Justify your answer.

Introduction to Chemical Engineering Thermodynamics
8th Edition
ISBN:9781259696527
Author:J.M. Smith Termodinamica en ingenieria quimica, Hendrick C Van Ness, Michael Abbott, Mark Swihart
Publisher:J.M. Smith Termodinamica en ingenieria quimica, Hendrick C Van Ness, Michael Abbott, Mark Swihart
Chapter1: Introduction
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As part of a process to fabricate materials with ordered pore arrays, the diffusion‐limited solvent etching process shown in the figure below is used to remove a contaminant (solid solute A, lithium carbonate) from an array of pores within a slab. There are presently 16 cylindrical pores, each of 0.10 cm diameter and 0.5 cm depth, and the overall dimensions of the slab are 4.0 cm per side and 0.60 cm deep. Liquid solvent (species B) flows over the surface of the slab at a high rate so that the concentration of dissolved solute A is essentially zero. Further, the dissolved solute A is not very soluble (sparingly soluble) in solvent B. The process is carried out at ambient conditions (25oC, 1.0 atm). Other potentially useful information: maximum solubility of solute A in solvent B, C*A = 90 µmole/cm3, density of solvent B, ρB = 1.0 g/cm3, ρA,solid = 2.1 g/cm3, MA = 74 g/gmole, MB = 18 g/gmole, DAB = 1.6 × 10–5 cm2/s. A. Initially, the solid solute A is loaded to a depth of 0.20 cm within each 0.5 cm length pore, as shown in the figure below. At this point, what the total transfer rate of solute A out of the entire slab, in units of µmole/s? B. How much time will it take for all the solid solute A to be removed from each pore, in units of hours? C. The process takes a long time. What changes to the process parameters such as (i) pore diameter, (ii) diffusion path length, and (iii) process temperature would likely reduce the time required? Justify your answer.
Cross-section
view of pore
array
At the
final
time
ORD
Bulk fluid
CA≈ 0
w
4.0 cm
(not to scale)
Detail for one pore
CAO
0.1 cm
ΝΑ
Solid
A
4=
0.5 cm
↑
I
L₁ = 0.20 cm
N
Transcribed Image Text:Cross-section view of pore array At the final time ORD Bulk fluid CA≈ 0 w 4.0 cm (not to scale) Detail for one pore CAO 0.1 cm ΝΑ Solid A 4= 0.5 cm ↑ I L₁ = 0.20 cm N
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