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Using the analogy between heat and mass transfer, explain how the mass transfer coefficient can be determined from the relations for the heat transfer coefficient.

Short Answer

Expert verified
Answer: By using the analogy between heat and mass transfer, one can determine the mass transfer coefficient from the heat transfer coefficient relationship using dimensionless parameters such as the Nusselt number (Nu) and Sherwood number (Sh). An appropriate correlation for the heat transfer coefficient (Nu correlation) is found, and a similar correlation for the mass transfer coefficient (Sh correlation) is derived. Then, the known values (or calculated) for the heat transfer coefficient (h) are used to substitute into the Nu equation and solve for the unknown variables. Finally, these values are utilized to determine the mass transfer coefficient (k_m) using the Sh equation.

Step by step solution

01

Understand heat transfer

Heat transfer refers to the movement of heat (thermal energy) from one location to another due to temperature differences. There are three main modes of heat transfer: conduction (through solid materials), convection (in liquids and gases), and radiation (through empty space).
02

Understand mass transfer

Mass transfer refers to the movement of mass from one location to another due to concentration differences. Mass transfer is a common phenomenon in various engineering processes, such as chemical reactions, separation processes, and diffusion.
03

Define heat transfer coefficient

The heat transfer coefficient, represented by h [W/(m^2 * K)], is an important parameter that quantifies the ease of heat transfer between two media. It accounts for the combined effects of heat transfer mechanisms, including conduction, convection, and radiation. It is usually determined empirically or through correlations.
04

Define mass transfer coefficient

The mass transfer coefficient, represented by k [m/s], is an important parameter that quantifies the ease of mass transfer between two media. It accounts for factors such as diffusion, turbulent mixing, and other transport mechanisms. Similar to heat transfer coefficient, the mass transfer coefficient is determined empirically or through correlations.
05

Understand the analogy between heat and mass transfer coefficients

Although heat and mass transfer are different phenomena, they often share similar mechanisms, like boundary layer formation and turbulent mixing. The analogy between heat and mass transfer is based on the similar behavior of both processes in terms of their boundary layer formations and governing equations. In many cases, heat and mass transfer coefficients have similar values under similar conditions.
06

Determine the mass transfer coefficient from the heat transfer coefficient

Using the analogy between heat and mass transfer, one can determine the mass transfer coefficient from the heat transfer coefficient relationship using dimensionless parameters. Two of the most common dimensionless parameters in heat and mass transfer are the Nusselt number (Nu) and Sherwood number (Sh). Nu = hL/k_h, where L is a characteristic length, k_h is the thermal conductivity of the fluid, and h is the heat transfer coefficient. Sh = k_mL/D, where L is a characteristic length, D is the diffusivity of the species, and k_m is the mass transfer coefficient. Using these dimensionless parameters, one can relate the heat transfer coefficient (h) to the mass transfer coefficient (k_m) through a derived correlation using experimental data or theoretical analysis. For example, if we have a correlation between Nu and some variables, we can often find a similar correlation between Sh and the same (or similar) variables, allowing us to determine k_m from the known or calculated h. This approach can be summarized in the following steps: 1. Find an appropriate correlation for the heat transfer coefficient (Nu correlation) 2. Derive or find a similar correlation for the mass transfer coefficient (Sh correlation) 3. Use the known values (or calculate) the heat transfer coefficient (h) 4. Substitute the known values into the Nu equation and solve for the unknown variables 5. Use the values obtained in step 4 to determine the mass transfer coefficient (k_m) using the Sh equation The specific correlation and calculation for heat and mass transfer coefficients may vary, depending on the system and problem. However, the general approach of using the analogy between heat and mass transfer to determine the mass transfer coefficient from the relations for the heat transfer coefficient remains consistent.

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Key Concepts

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

Heat Transfer Coefficient
The heat transfer coefficient (often denoted as h) plays a vital role in understanding how heat energy moves between materials. It serves as an indicator of the efficiency of heat transfer across a boundary between a solid surface and a fluid or between two different fluids. Given in units of W/(m2 * K), it wraps together the effects of conduction, convection, and radiation into a single value. For example, a high heat transfer coefficient suggests that a system is very effective at transferring heat, making it an essential parameter in thermal engineering tasks like designing radiators, heat exchangers, or even in more common applications like cooking utensils. This coefficient is usually found through experimental data or by using empirical correlations, depending on the nuances of the physical situation.

When analyzing problems related to heat transfer, the heat transfer coefficient provides a simplified way to model complex thermal interactions without dealing with the detailed physics of heat transfer mechanisms. A firm grasp on this concept is a stepping stone for using analogies to understand mass transfer processes, as both phenomena exhibit parallel behavior in certain circumstances.
Mass Transfer Coefficient
Similar to its heat-related counterpart, the mass transfer coefficient (portrayed typically as km) quantifies the ease with which mass is transported from one place to another due to concentration differences. Its unit is meters per second (m/s), and it reflects the capability of a system to mix or separate different species through diffusion, convection, and other mass transport mechanisms. Whether dealing with pollution dispersion in the environment, extraction in a chemical process, or moisture absorption in food packaging, the mass transfer coefficient is a fundamental parameter.

Understanding the mass transfer coefficient provides insight into many industrial processes and natural phenomena. To determine this coefficient, one often relies on empirical relationships similar to those for the heat transfer coefficient. Mastering this concept enables students and engineers to design and analyze processes that involve the transport of substances, such as in chemical reactors or air purification systems.
Nusselt Number (Nu)
The Nusselt number (Nu) is a dimensionless parameter symbolizing the ratio of convective to conductive heat transfer across a boundary. Defined as Nu = hL/kh, where L is a characteristic length, kh is the thermal conductivity of the fluid, and h is the heat transfer coefficient, it encapsulates the heat transfer characteristics of a system into a non-dimensional form. This pioneering concept allows engineers to compare heat transfer performance across different systems regardless of their scales.

For instance, a high Nusselt number implies that convection dominates the heat transfer process, while a low Nusselt number indicates that conduction is more significant. While the concept might seem abstract, it is used to devise correlations that facilitate the computation of the heat transfer coefficient from known physical parameters, greatly simplifying the process of thermal design.
Sherwood Number (Sh)
The Sherwood number (Sh), akin to the Nusselt number in heat transfer, is a dimensionless value used in mass transfer analyses. It is described by the equation Sh = kmL/D, where L is the characteristic length, D is the diffusivity of the species, and km is the mass transfer coefficient. The Sherwood number signifies the ratio of convective to diffusive mass transfer, thus serving as a yardstick for the efficacy of mass transfer in a system.

High values of Sherwood number indicate that convection is the principal means of mass transfer, as often observed in stirred tank reactors or packed columns. Understanding the Sherwood number allows one to derive the mass transfer coefficient using analogous relations from heat transfer, which can be invaluable for engineering applications like designing separation units and improving reaction kinetics.

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Most popular questions from this chapter

A recent attempt to circumnavigate the world in a balloon used a helium-filled balloon whose volume was \(7240 \mathrm{~m}^{3}\) and surface area was \(1800 \mathrm{~m}^{2}\). The skin of this balloon is \(2 \mathrm{~mm}\) thick and is made of a material whose helium diffusion coefficient is \(1 \times 10^{-9} \mathrm{~m}^{2} / \mathrm{s}\). The molar concentration of the helium at the inner surface of the balloon skin is \(0.2 \mathrm{kmol} / \mathrm{m}^{3}\) and the molar concentration at the outer surface is extremely small. The rate at which helium is lost from this balloon is (a) \(0.26 \mathrm{~kg} / \mathrm{h}\) (b) \(1.5 \mathrm{~kg} / \mathrm{h}\) (c) \(2.6 \mathrm{~kg} / \mathrm{h}\) (d) \(3.8 \mathrm{~kg} / \mathrm{h}\) (e) \(5.2 \mathrm{~kg} / \mathrm{h}\)

A rubber object is in contact with nitrogen \(\left(\mathrm{N}_{2}\right)\) at \(298 \mathrm{~K}\) and \(250 \mathrm{kPa}\). The solubility of nitrogen gas in rubber is \(0.00156 \mathrm{kmol} / \mathrm{m}^{3}\).bar. The mass density of nitrogen at the interface is (a) \(0.049 \mathrm{~kg} / \mathrm{m}^{3}\) (b) \(0.064 \mathrm{~kg} / \mathrm{m}^{3}\) (c) \(0.077 \mathrm{~kg} / \mathrm{m}^{3}\) (d) \(0.092 \mathrm{~kg} / \mathrm{m}^{3}\) (e) \(0.109 \mathrm{~kg} / \mathrm{m}^{3}\)

14-45 Consider a rubber membrane separating carbon dioxide gas that is maintained on one side at \(2 \mathrm{~atm}\) and on the opposite at \(1 \mathrm{~atm}\). If the temperature is constant at \(25^{\circ} \mathrm{C}\), determine (a) the molar densities of carbon dioxide in the rubber membrane on both sides and \((b)\) the molar densities of carbon dioxide outside the rubber membrane on both sides.

The average heat transfer coefficient for air flow over an odd-shaped body is to be determined by mass transfer measurements and using the Chilton-Colburn analogy between heat and mass transfer. The experiment is conducted by blowing dry air at \(1 \mathrm{~atm}\) at a free stream velocity of \(2 \mathrm{~m} / \mathrm{s}\) over a body covered with a layer of naphthalene. The surface area of the body is \(0.75 \mathrm{~m}^{2}\), and it is observed that \(100 \mathrm{~g}\) of naphthalene has sublimated in \(45 \mathrm{~min}\). During the experiment, both the body and the air were kept at \(25^{\circ} \mathrm{C}\), at which the vapor pressure and mass diffusivity of naphthalene are \(11 \mathrm{~Pa}\) and \(D_{A B}=0.61 \times\) \(10^{-5} \mathrm{~m}^{2} / \mathrm{s}\), respectively. Determine the heat transfer coefficient under the same flow conditions over the same geometry.

The diffusion coefficient of carbon in steel is given as $$ D_{A B}=2.67 \times 10^{-5} \exp (-17,400 / T) \quad\left(\mathrm{m}^{2} / \mathrm{s}\right) $$ where \(T\) is in \(\mathrm{K}\). Determine the diffusion coefficient from \(300 \mathrm{~K}\) to \(1500 \mathrm{~K}\) in \(100 \mathrm{~K}\) increments and plot the results.

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