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When prescribing a boundary condition for mass transfer at a solid-gas interface, why do we need to specify the side of the surface (whether the solid or the gas side)? Why did we not do it in heat transfer?

Short Answer

Expert verified
Answer: In mass transfer, specifying the side of the surface (solid or gas side) is important because mass transfer relies on different substance concentrations and properties between the solid and gas phases. Thus, it ensures correct boundary conditions are applied for accurate results. In heat transfer, there is no need to specify the side of the surface because heat transfer is primarily driven by temperature differences, not substance properties or phases. All substances, regardless of their phase, will have the same temperature at the boundary.

Step by step solution

01

Understanding boundary conditions in mass transfer

In mass transfer, boundary conditions are essential to model the behavior of a system correctly. These conditions describe how the mass transfer occurs at the interface between the solid and the gas phase, including the concentration or flux of substances at the surface. Since mass transfer at the interface involves substances from both phases, it is crucial to specify which side of the surface we are referring to.
02

Significance of specifying the side of the surface in mass transfer

The mass transfer phenomenon is heavily dependent on the concentration gradients and the properties of the substances involved, which can significantly vary between the solid and gas phases. Thus, specifying the side of the surface (solid or gas side) is necessary as it ensures that the correct boundary condition is applied. It avoids confusion during problem-solving and helps in obtaining accurate results.
03

Understanding boundary conditions in heat transfer

In heat transfer, boundary conditions usually involve specifying the temperature or heat flux at a particular surface. The temperature is a scalar property, and heat flow is governed by temperature gradients. Unlike mass transfer, where the solid and gas phases have different substance concentrations, the heat transfer is mainly driven by the difference in temperature and not the substance properties or their phases.
04

Reason for not specifying the side of the surface in heat transfer

Since heat transfer is primarily driven by temperature differences, the focus is not on which phase the heat is being transferred through. Therefore, there is no need to specify the side of the surface when describing boundary conditions for heat transfer as all substances, regardless of their phase, will have the same temperature at the boundary.

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Most popular questions from this chapter

Air at \(52^{\circ} \mathrm{C}, 101.3 \mathrm{kPa}\), and 20 percent relative humidity enters a \(5-\mathrm{cm}\)-diameter tube with an average velocity of $6 \mathrm{~m} / \mathrm{s}$. The tube inner surface is wetted uniformly with water, whose vapor pressure at \(52^{\circ} \mathrm{C}\) is \(13.6 \mathrm{kPa}\). While the temperature and pressure of air remain constant, the partial pressure of vapor in the outlet air is increased to \(10 \mathrm{kPa}\). Detemine \((a)\) the average mass transfer coefficient in $\mathrm{m} / \mathrm{s}\(, \)(b)$ the log-mean driving force for mass transfer in molar concentration units, \((c)\) the water evaporation rate in $\mathrm{kg} / \mathrm{h}\(, and \)(d)$ the length of the tube.

The surface of an iron component is to be hardened by carbon. The diffusion coefficient of carbon in iron at \(1000^{\circ} \mathrm{C}\) is given to be $3 \times 10^{-11} \mathrm{~m}^{2} / \mathrm{s}$. If the penetration depth of carbon in iron is desired to be \(1.0 \mathrm{~mm}\), the hardening process must take at least (a) \(1.10 \mathrm{~h}\) (b) \(1.47 \mathrm{~h}\) (c) \(1.86 \mathrm{~h}\) (d) \(2.50 \mathrm{~h}\) (e) \(2.95 \mathrm{~h}\)

Consider a wet concrete patio covered with a thin film of water. At the surface, mass convection of water to air occurs at an average mass transfer coefficient of \(0.03 \mathrm{~m} / \mathrm{s}\). If the air is at $1 \mathrm{~atm}, 15^{\circ} \mathrm{C}$ and 35 percent relative humidity, determine the mass fraction concentration gradient of water at the surface.

Consider one-dimensional mass transfer in a moving medium that consists of species \(A\) and \(B\) with \(\rho=\) \(\rho_{A}+\rho_{B}=\) constant. Mark these statements as being True or False. (a) The rates of mass diffusion of species \(A\) and \(B\) are equal in magnitude and opposite in direction. (b) \(D_{A B}=D_{B A^{-}}\) (c) During equimolar counterdiffusion through a tube, equal numbers of moles of \(A\) and \(B\) move in opposite directions, and thus a velocity measurement device placed in the tube will read zero. (d) The lid of a tank containing propane gas (which is heavier than air) is left open. If the surrounding air and the propane in the tank are at the same temperature and pressure, no propane will escape the tank, and no air will enter.

The local convection heat transfer coefficient for air flowing parallel over a 1 -m-long plate with irregular surface topology is experimentally determined to be \(h_{x}=0.5+12 x-0.7 x^{3}\), where \(h_{x}\) is in $\mathrm{W} / \mathrm{m}^{2} \cdot \mathrm{K}$. If the plate surface is coated with water, determine the corresponding average mass convection coefficient over the entire plate. Assume properties can be evaluated at \(298 \mathrm{~K}\) and $1 \mathrm{~atm}$.

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