/*! This file is auto-generated */ .wp-block-button__link{color:#fff;background-color:#32373c;border-radius:9999px;box-shadow:none;text-decoration:none;padding:calc(.667em + 2px) calc(1.333em + 2px);font-size:1.125em}.wp-block-file__button{background:#32373c;color:#fff;text-decoration:none} Problem 108 The human eye contains aqueous h... [FREE SOLUTION] | 91影视

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The human eye contains aqueous humor, which separates the external cornea and the internal iris-lens structure. It is hypothesized that, in some individuals, small flakes of pigment are intermittently liberated from the iris and migrate to, and subsequently damage, the cornea. Approximating the geometry of the enclosure formed by the cornea and iris-lens structure as a pair of concentric hemispheres of outer radius \(r_{o}=10 \mathrm{~mm}\) and inner radius \(r_{i}=7 \mathrm{~mm}\), respectively, investigate whether free convection can occur in the aqueous humor by evaluating the effective thermal conductivity ratio, \(k_{\mathrm{efI}} / k\). If free convection can occur, it is possible that the damaging particles are advected from the iris to the cornea. The iris-lens structure is at the core temperature, \(T_{i}=37^{\circ} \mathrm{C}\), while the cornea temperature is measured to be \(T_{o}=34^{\circ} \mathrm{C}\). The properties of the aqueous humor are \(\rho=990 \mathrm{~kg} / \mathrm{m}^{3}, k=0.58 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}\), \(c_{p}=4.2 \times 10^{3} \mathrm{~J} / \mathrm{kg} \cdot \mathrm{K}, \mu=7.1 \times 10^{-4} \mathrm{~N} \cdot \mathrm{s} / \mathrm{m}^{2}\), and \(\beta=3.2 \times 10^{-4} \mathrm{~K}^{-1}\)

Short Answer

Expert verified
The temperature difference between the iris-lens structure and the cornea is 螖T = 3掳C. For the given geometry, the calculated Rayleigh number is Ra 鈮 3.01 x 10鲁, which is larger than the critical Rayleigh number for the onset of convection (~1708), indicating that free convection is likely to occur. The effective thermal conductivity ratio is found to be approximately \(k_{\mathrm{eff}} / k\) 鈮 5.37, suggesting that free convection can indeed occur in the aqueous humor and supporting the hypothesis that damaging particles might be advected from the iris to the cornea.

Step by step solution

01

Calculate temperature difference 螖T

First, we need to calculate the temperature difference between the outer hemisphere (cornea) and the inner hemisphere (iris-lens structure). We can use the given temperatures of the two structures: 螖T = \(T_i - T_o\) 螖T = \(37^{\circ} C - 34^{\circ} C\) 螖T = \(3^{\circ} C\)
02

Calculate the characteristic length L

Next, we must calculate the characteristic length, L, which, for a pair of concentric hemispheres, is half the difference between the outer and inner radii: L = \(\frac{r_o - r_i}{2}\) L = \(\frac{10 mm - 7 mm}{2}\) L = \(\frac{3 mm}{2}\) L = \(1.5 mm\) or \(1.5 \times 10^{-3} m\)
03

Evaluate Rayleigh number Ra

The Rayleigh number (Ra) for our problem is given by: Ra = \(\frac{g \beta \Delta T L^3}{\nu \alpha}\) Where, - g is the gravitational acceleration, \(9.81 m/s^2\) - 尾 is the coefficient of thermal expansion, \(3.2 \times 10^{-4} K^{-1}\) - 螖T is the temperature difference calculated in Step 1 - L is the characteristic length calculated in Step 2 - 谓 is the kinematic viscosity, which can be found by dividing 渭 by 蟻: \(\nu = \frac{\mu}{\rho}\) - 渭 is the dynamic viscosity, \(7.1 \times 10^{-4} N \cdot s / m^{2}\) - 蟻 is the density, \(990 kg / m^3\) - 伪 is the thermal diffusivity, which can be found by dividing k by 蟻 and cp: \(\alpha = \frac{k}{\rho c_p}\) - k is the thermal conductivity, \(0.58 W / m \cdot K\) - cp is the specific heat capacity, \(4.2 \times 10^3 J / kg \cdot K\) First, find the values for 谓 and 伪: 谓 = \(\frac{7.1 \times 10^{-4} N \cdot s / m^2}{990 kg / m^3}\) = \(7.17 \times 10^{-7} m^2/s\) 伪 = \(\frac{0.58 W / m \cdot K}{990 kg / m^3 \cdot 4.2 \times 10^3 J / kg \cdot K}\) = \(1.40 \times 10^{-7} m^2/s\) Now, we can calculate Ra: Ra = \(\frac{9.81 m/s^2 \cdot 3.2 \times 10^{-4} K^{-1} \cdot 3 K \cdot (1.5 \times 10^{-3} m)^3}{7.17 \times 10^{-7} m^2/s \cdot 1.40 \times 10^{-7} m^2/s}\) 鈮 \(3.01 \times 10^3\) Since the Rayleigh number is larger than the critical Rayleigh number for the onset of convection (~1708), we can conclude that free convection is likely to occur.
04

Evaluate the Nusselt number and find the effective thermal conductivity ratio

For free convection between concentric hemispheres, we can use the Nusselt number (Nu) correlation to calculate the effective thermal conductivity ratio. The given correlation is: Nu = \(\frac{h L}{k}\) Where h is the convective heat transfer coefficient. Assuming a relationship between the Nusselt number and the Rayleigh number of Nu 鈮 Ra^(1/4), which is commonly used for natural convection problems, we can calculate h: Nu = Ra^(1/4) Nu 鈮 (3.01 \times 10^3)^(1/4) 鈮 5.37 Now, we can solve for the effective thermal conductivity ratio, \(k_{eff} / k\): \(k_{eff} / k\) = Nu \(k_{eff} / k\) 鈮 5.37 Therefore, the effective thermal conductivity ratio is approximately 5.37. This result suggests that free convection can indeed occur in the aqueous humor, which supports the hypothesis that the particles damaging the cornea might be advected from the iris to the cornea.

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Key Concepts

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

Rayleigh Number
The Rayleigh number (Ra) is a dimensionless number that characterizes the buoyancy-driven flow (natural convection) in a fluid due to temperature differences. It's defined by the formula:

\[\begin{equation}Ra = \frac{g \beta \Delta T L^3}{u \alpha}\end{equation}\]
Here's what each symbol represents:
  • \(g\) is the acceleration due to gravity.
  • \(\beta\) is the coefficient of thermal expansion, indicating how much a material expands per degree of temperature increase.
  • \(\Delta T\) is the temperature difference across the fluid layer.
  • \(L\) is a characteristic length, often the height of the fluid layer.
  • \(u\) is the kinematic viscosity, defining the fluid's resistance to flow.
  • \(\alpha\) is the thermal diffusivity, representing how quickly a material can conduct heat relative to its ability to store heat.

A high Rayleigh number suggests that buoyancy forces, which drive natural convection, are significant compared to viscous forces, which resist the flow. Our problem demonstrates that, since Ra exceeds a critical value, natural convection is likely to be present, causing the free movement of the aqueous humor due to temperature differences within the human eye.
Nusselt Number
The Nusselt number (Nu) is another dimensionless parameter crucial in the study of heat transfer through convection. It is defined as the ratio of convective to conductive heat transfer for a fluid and can be expressed with the equation:

\[\begin{equation}Nu = \frac{h L}{k}\end{equation}\]
In which:
  • \(h\) is the convective heat transfer coefficient 鈥 indicating the efficiency of the convective heat transfer process.
  • \(L\) is the characteristic length as before.
  • \(k\) is the thermal conductivity 鈥 a measure of the ability of a material to transfer heat through conduction.

For the case of natural convection, the Nusselt number correlates with the Rayleigh number, allowing us to estimate the heat transfer coefficient and gain insight into the effectiveness of convection. In the hypothetical scenario of pigment flakes causing eye damage, the Nusselt number's estimation leads us to conclude that free convection may be responsible for transporting these particles.
Thermal Conductivity
Thermal conductivity (\(k\)) is a physical property that measures a material's ability to conduct heat. It is defined as the quantity of heat, \(Q\), transmitted through a material with thickness \(L\), in time \(t\), due to a temperature difference \(\Delta T\), under steady-state conditions and when the heat transfer is dependent only on the temperature gradient. The mathematical expression is:

\[\begin{equation}q = -k \frac{\Delta T}{L}\end{equation}\]
where \(q\) represents the heat flux. In the context of the aqueous humor in the human eye, thermal conductivity plays a vital role as it can affect the rate at which heat is transferred from the warmer iris-lens structure to the cooler cornea. This heat transfer, in turn, can generate convective currents which potentially transport damaging pigment flakes. In the solution provided, we consider thermal conductivity when evaluating both the Rayleigh and Nusselt numbers, playing an integral part in determining whether free convection can occur.
Convective Heat Transfer
Convective heat transfer is the process by which heat is carried away by the movement of fluid, which can be liquid or gas. This mechanism is at play when there is a temperature difference between a solid surface and the adjacent fluid, causing the warmer fluid to rise and cooler fluid to descend, forming convective currents. Convective heat transfer can be natural (or free), as is the case with the temperature-induced movement of the aqueous humor in the eye, or forced, where an external source like a fan or pump drives the fluid motion.

In our example of the aqueous humor, the critical understanding is that if convective currents are sufficiently strong, they may be effective in transporting the small pigment flakes. This gives credence to the theory that free convection within the eye could influence the distribution of these particles and potentially lead to damage. The convective heat transfer coefficient (\(h\)) is a way of quantifying the rate of convective heat transfer, and it is crucial in calculating the Nusselt number, which assesses the efficiency of this transfer compared to conductive heat transfer.

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Most popular questions from this chapter

A long, uninsulated steam line with a diameter of \(89 \mathrm{~mm}\) and a surface emissivity of \(0.8\) transports steam at \(200^{\circ} \mathrm{C}\) and is exposed to atmospheric air and large surroundings at an equivalent temperature of \(20^{\circ} \mathrm{C}\). (a) Calculate the heat loss per unit length for a calm day. (b) Calculate the heat loss on a breezy day when the wind speed is \(8 \mathrm{~m} / \mathrm{s}\). (c) For the conditions of part (a), calculate the heat loss with a 20 -mm- thick layer of insulation ( \(k=\) \(0.08 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K})\). Would the heat loss change significantly with an appreciable wind speed?

A 200-mm-square, 10-mm-thick tile has the thermophysical properties of Pyrex \((\varepsilon=0.80)\) and emerges from a curing process at an initial temperature of \(T_{i}=140^{\circ} \mathrm{C}\). The backside of the tile is insulated while the upper surface is exposed to ambient air and surroundings at \(25^{\circ} \mathrm{C}\).

A computer code is being developed to analyze a 12.5-mm-diameter, cylindrical sensor used to determine ambient air temperature. The sensor experiences free convection while positioned horizontally in quiescent air at \(T_{\infty}=27^{\circ} \mathrm{C}\). For the temperature range from 30 to \(80^{\circ} \mathrm{C}\), derive an expression for the convection coefficient as a function of only \(\Delta T=\) \(T_{s}-T_{\infty}\), where \(T_{s}\) is the sensor temperature. Evaluate properties at an appropriate film temperature and show what effect this approximation has on the convection coefficient estimate.

Consider laminar flow about a vertical isothermal plate of length \(L\), providing an average heat transfer coefficient of \(\bar{h}_{L}\). If the plate is divided into \(N\) smaller plates, each of length, \(L_{N}=L / N\), determine an expression for the ratio of the heat transfer coefficient averaged over the \(N\) plates to the heat transfer coefficient averaged over the single plate, \(\bar{h}_{L, N} / \bar{h}_{L, 1}\).

Integrated circuit (IC) boards are stacked within a duct and dissipate a total of \(500 \mathrm{~W}\). The duct has a square cross section with \(w=H=150 \mathrm{~mm}\) and a length of \(0.5 \mathrm{~m}\). Air flows into the duct at \(25^{\circ} \mathrm{C}\) and \(1.2 \mathrm{~m}^{3} / \mathrm{min}\), and the convection coefficient between the air and the inner surfaces of the duct is \(\bar{h}_{i}=50 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\). The entire outer surface of the duct, which is anodized with an emissivity of \(0.5\), is exposed to ambient air and large surroundings at \(25^{\circ} \mathrm{C}\). Your assignment is to develop a model to estimate the outlet temperature of the air, \(T_{m, o}\) and the average surface temperature of the duct, \(\bar{T}_{s}\). (a) Assuming a surface temperature of \(37^{\circ} \mathrm{C}\), estimate the average free convection coefficient, \(\bar{h}_{o}\), for the outer surface of the duct. (b) Assuming a surface temperature of \(37^{\circ} \mathrm{C}\), estimate the average linearized radiation coefficient, \(\bar{h}_{\text {rad }}\), for the outer surface of the duct. (c) Perform an energy balance on the duct by considering the dissipation of electrical power in the ICs, the rate of change in the energy of air flowing through the duct, and the rate of heat transfer from the air in the duct to the surroundings. Express the last process in terms of thermal resistances between the mean temperature, \(\bar{T}_{m}\), of the air in the duct and the temperature of the ambient air and the surroundings. (d) Substitute numerical values into the expression of part (c) and calculate the air outlet temperature, \(T_{m, \sigma^{*}}\). Estimate the corresponding value of \(\bar{T}_{s}\). Comment on your results and the assumptions inherent in your model.

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