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Write three boundary conditions for mass transfer (on a mass basis) for species \(A\) at \(x=0\) that correspond to specified temperature, specified heat flux, and convection boundary conditions in heat transfer.

Short Answer

Expert verified
Q: Write three boundary conditions for mass transfer for species A at x=0 that correspond to specified temperature, specified heat flux, and convection boundary conditions in heat transfer. A: The three boundary conditions for mass transfer for species A at x=0 that correspond to specified temperature, specified heat flux, and convection boundary conditions in heat transfer are: 1. Specified concentration: \(C_A(x=0)=C_{A0}\) 2. Specified mass flux: \(j_A(x=0)=j_{A0}\) 3. Convective mass transfer: \(j_A(x=0) = k_c(C_{Af}-C_{A 0})\)

Step by step solution

01

Understanding the Mass Transfer Analogies for Heat Transfer Boundary Conditions

We will first understand the mass transfer analogies for the different heat transfer boundary conditions: - Specified temperature: This is analogous to a specified concentration condition in mass transfer, where the concentration of species \(A\) at \(x=0\) is specified. - Specified heat flux: This corresponds to a specified mass flux condition in mass transfer, where the mass flux of species \(A\) at \(x=0\) is specified. - Convection boundary condition: This corresponds to a convective mass transfer boundary condition, where the mass transfer between the boundary (\(x=0\)) and the fluid is dictated by a convective mass transfer coefficient and the concentration difference between the surface and the fluid.
02

Boundary condition for a specified concentration

When the boundary condition is given for specified temperature, the mass transfer equivalent is a specified concentration at \(x=0\). The boundary condition can be written as: $$ C_A(x=0)=C_{A0} $$ Where \(C_A\) is the concentration of species \(A\) and \(C_{A0}\) is the specified concentration at \(x=0\).
03

Boundary condition for a specified mass flux

When the boundary condition is given for specified heat flux, the mass transfer equivalent is a specified mass flux at \(x=0\). The boundary condition can be written as: $$ j_A(x=0)=j_{A0} $$ Where \(j_A\) is the mass flux of species \(A\) (in \(\text{kg m}^{-2} \text{s}^{-1}\)) and \(j_{A0}\) is the specified mass flux at \(x=0\).
04

Boundary condition for convective mass transfer

When the boundary condition is given for convection heat transfer, mass transfer equivalent is a convective mass transfer boundary condition. The boundary condition can be written as: $$ j_A(x=0) = k_c(C_{Af}-C_{A 0}) $$ Where \(k_c\) is the mass transfer coefficient at \(x=0\) (in \(\text{kg m}^{-2} \text{s}^{-1}\)), \(C_{Af}\) is the concentration of species \(A\) in the fluid, and \(C_{A0}\) is the concentration of species \(A\) at the surface \(x=0\).

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Key Concepts

These are the key concepts you need to understand to accurately answer the question.

Specified Concentration
In mass transfer, a specified concentration boundary condition means that at a certain location, the concentration of a species is known and fixed. This is similar to how in heat transfer, you might specify a certain temperature at a boundary.
For example, consider a boundary at position \( x = 0 \) where the concentration \( C_A \) of species \( A \) is specified. We express this using the equation:
  • \( C_A(x=0) = C_{A0} \)
This boundary condition is quite straightforward because it sets a clear, defined value for the concentration of species \( A \) right at the boundary.
Such specified concentration conditions serve essential roles in problems where boundary behavior dictates the rest of the solution. They are often used in cases like chemical reactors or separation processes where a particular composition needs to be maintained or established at the boundary.
Specified Mass Flux
A specified mass flux boundary condition in mass transfer specifies the rate at which mass flows across a boundary. It is the counterpart to specifying heat flux in thermal problems.
In terms of math, at the boundary \( x = 0 \), the mass flux \( j_A \) of species \( A \), is given as:
  • \( j_A(x=0) = j_{A0} \)
Here, \( j_A \) represents the mass flux usually in units of \( \text{kg m}^{-2} \text{s}^{-1} \).
This boundary condition is crucial when we need to maintain a certain mass transfer rate at the interface, which can be encountered in systems involving membranes, or in industrial operations where a precise mass input or output is critical.
Specified mass flux conditions ensure control over the transport rate, making them indispensable for achieving desired operational efficiencies.
Convective Mass Transfer
Convective mass transfer boundary conditions arise in systems where the mass transfer is influenced by movement of fluid, analogous to how convection impacts heat transfer.
The boundary condition reflects a situation where mass transfer between the boundary at \( x = 0 \) and the surrounding fluid is driven by a convective process.
The mass transfer rate is calculated using the mass transfer coefficient \( k_c \) and the concentration difference between the fluid and the boundary:
  • \( j_A(x=0) = k_c(C_{Af} - C_{A0}) \)
Where:
  • \( j_A \) is the mass flux at \( x = 0 \).
  • \( C_{Af} \) is the fluid concentration of species \( A \).
  • \( C_{A0} \) is the concentration at the boundary.
Convective mass transfer conditions are profound in many practical applications, such as when cooling a hot gas with a liquid spray, or in designing reactors where the fluid flow has a significant effect on the transfer of mass.

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Most popular questions from this chapter

Consider a 15-cm-internal-diameter, 10-m-long circular duct whose interior surface is wet. The duct is to be dried by forcing dry air at \(1 \mathrm{~atm}\) and \(15^{\circ} \mathrm{C}\) through it at an average velocity of \(3 \mathrm{~m} / \mathrm{s}\). The duct passes through a chilled room, and it remains at an average temperature of \(15^{\circ} \mathrm{C}\) at all times. Determine the mass transfer coefficient in the duct.

An 8-cm-internal-diameter, 30-cm-high pitcher halffilled with water is left in a dry room at \(15^{\circ} \mathrm{C}\) and \(87 \mathrm{kPa}\) with its top open. If the water is maintained at \(15^{\circ} \mathrm{C}\) at all times also, determine how long it will take for the water to evaporate completely.

Air at \(40^{\circ} \mathrm{C}\) and 1 atm flows over a \(5-\mathrm{m}\)-long wet plate with an average velocity of \(2.5 \mathrm{~m} / \mathrm{s}\) in order to dry the surface. Using the analogy between heat and mass transfer, determine the mass transfer coefficient on the plate.

Dry air whose molar analysis is \(78.1\) percent \(\mathrm{N}_{2}\), \(20.9\) percent \(\mathrm{O}_{2}\), and 1 percent Ar flows over a water body until it is saturated. If the pressure and temperature of air remain constant at \(1 \mathrm{~atm}\) and \(25^{\circ} \mathrm{C}\) during the process, determine (a) the molar analysis of the saturated air and \((b)\) the density of air before and after the process. What do you conclude from your results?

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