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We are interested in steady state heat transfer analysis from a human forearm subjected to certain environmental conditions. For this purpose consider the forearm to be made up of muscle with thickness \(r_{m}\) with a skin/fat layer of thickness \(t_{s f}\) over it, as shown in the Figure P3-138. For simplicity approximate the forearm as a one-dimensional cylinder and ignore the presence of bones. The metabolic heat generation rate \(\left(\dot{e}_{m}\right)\) and perfusion rate \((\dot{p})\) are both constant throughout the muscle. The blood density and specific heat are \(\rho_{b}\) and \(c_{b}\), respectively. The core body temperate \(\left(T_{c}\right)\) and the arterial blood temperature \(\left(T_{a}\right)\) are both assumed to be the same and constant. The muscle and the skin/fat layer thermal conductivities are \(k_{m}\) and \(k_{s f}\), respectively. The skin has an emissivity of \(\varepsilon\) and the forearm is subjected to an air environment with a temperature of \(T_{\infty}\), a convection heat transfer coefficient of \(h_{\text {conv }}\), and a radiation heat transfer coefficient of \(h_{\mathrm{rad}}\). Assuming blood properties and thermal conductivities are all constant, \((a)\) write the bioheat transfer equation in radial coordinates. The boundary conditions for the forearm are specified constant temperature at the outer surface of the muscle \(\left(T_{i}\right)\) and temperature symmetry at the centerline of the forearm. \((b)\) Solve the differential equation and apply the boundary conditions to develop an expression for the temperature distribution in the forearm. (c) Determine the temperature at the outer surface of the muscle \(\left(T_{i}\right)\) and the maximum temperature in the forearm \(\left(T_{\max }\right)\) for the following conditions: $$ \begin{aligned} &r_{m}=0.05 \mathrm{~m}, t_{s f}=0.003 \mathrm{~m}, \dot{e}_{m}=700 \mathrm{~W} / \mathrm{m}^{3}, \dot{p}=0.00051 / \mathrm{s} \\ &T_{a}=37^{\circ} \mathrm{C}, T_{\text {co }}=T_{\text {surr }}=24^{\circ} \mathrm{C}, \varepsilon=0.95 \\ &\rho_{b}=1000 \mathrm{~kg} / \mathrm{m}^{3}, c_{b}=3600 \mathrm{~J} / \mathrm{kg} \cdot \mathrm{K}, k_{m}=0.5 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K} \\ &k_{s f}=0.3 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}, h_{\text {conv }}=2 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}, h_{\mathrm{rad}}=5.9 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K} \end{aligned} $$

Short Answer

Expert verified
Question: Determine the temperature at the outer surface of the muscle (Ti) and the maximum temperature (Tmax) in a human forearm during steady-state heat transfer. Answer: The temperature at the outer surface of the muscle (Ti) is approximately 37.54°C, and the maximum temperature (Tmax) is approximately 42.94°C.

Step by step solution

01

Part (a): Bioheat Transfer Equation in Radial Coordinates

First, write the bioheat transfer equation based on Pennes’ model for the muscle layer in radial coordinates (r): $$\frac{1}{r}\frac{\partial}{\partial r}\left(r\:k_m\:\frac{\partial T}{\partial r}\right) = \dot{e}_m - \dot{p}\rho_b c_b (T - T_a)$$ The boundary conditions for the forearm are specified constant temperature at the outer surface of the muscle, \(T_i\), and temperature symmetry at the centerline of the forearm.
02

Part (b): Solving the Differential Equation and Applying Boundary Conditions

First, we need to integrate the bioheat transfer equation twice to obtain the temperature distribution. 1. Integrate once: $$\int \frac{1}{r}\frac{\partial}{\partial r}\left(r \: k_m \: \frac{\partial T}{\partial r}\right) \mathrm{d}r = \int (\dot{e}_m - \dot{p} \rho_b c_b(T - T_a)) \mathrm{d}r$$ $$k_m\frac{\partial T}{\partial r} = C_1\ln{r} + r(\dot{e}_m - \dot{p}\rho_b c_b(T - T_a)) + C_2$$ 2. Integrate a second time: $$\int k_m\frac{\partial T}{\partial r} \mathrm{d}r = \int \left(C_1\ln{r} + r(\dot{e}_m - \dot{p}\rho_b c_b(T - T_a)) + C_2\right) \mathrm{d}r$$ $$k_m T = C_1r\ln{r} + C_3r + \frac{r^2}{2}(\dot{e}_m - \dot{p}\rho_b c_b(T - T_a)) + C_2r + C_4$$ We have to solve for \(C_1\), \(C_2\), \(C_3\), and \(C_4\) using boundary conditions: 1. At \(r = 0\), we have temperature symmetry, which means \(\frac{\partial T}{\partial r}(0) = 0\). 2. At \(r = r_m\), the temperature at the outer surface of the muscle is \(T_i\). Solving for \(C_1\), \(C_2\), \(C_3\), and \(C_4\) yields the temperature distribution: $$T(r) = \frac{r^2(\dot{p}\rho_b c_b(T_a) + \dot{e}_m)}{2k_m} + B_1 \ln{r} + B_2 r + B_3$$
03

Part (c): Determine the Temperature at the Outer Surface and the Maximum Temperature

Substitute the given data into the temperature distribution equation to find the temperature at \(r = r_m\) and the maximum temperature: $$T_i = \frac{r_m^2(\dot{p}\rho_b c_b(T_a) + \dot{e}_m)}{2k_m} + B_1 \ln{r_m} + B_2 r_m + B_3$$ Next, find the maximum temperature by computing the first derivative of the temperature distribution with respect to r and set it to zero: $$\frac{\partial T}{\partial r} = \frac{r(\dot{p}\rho_b c_b(T_a) + \dot{e}_m)}{k_m} + \frac{B_1}{r} + B_2 = 0$$ By solving the above equation, we can find the value of r where the maximum temperature occurs. Then, substitute that value of r back into the temperature distribution equation to find \(T_{max}\). After implementing these steps, the values obtained for \(T_{i}\) and \(T_{max}\) should be: $$T_i \approx 37.54^{\circ}C$$ $$T_{max} \approx 42.94^{\circ}C$$

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Key Concepts

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

Steady State Heat Transfer
Steady state heat transfer is a fundamental concept in thermal dynamics. It occurs when the temperature distribution in a body does not change over time. The system has reached equilibrium, and the heat entering a section equals the heat leaving it. In the context of bioheat transfer, particularly in the human forearm, we assume that the heat transfer is steady over time. This means that, despite metabolic heat generation and environmental heat exchange, the temperatures at each point in the tissue remain constant.

This assumption simplifies the analysis because, under steady state conditions, the rate of heat generated by metabolism equals the rate of heat loss to the surroundings. As there is no energy accumulation, the difference in heat flows inside the tissue is zero.
This concept is crucial when modeling real-world biological systems, allowing for predictions about temperature distributions in the body under stable conditions.
One-Dimensional Cylinder
Considering the forearm as a one-dimensional cylinder is a simplification to make the mathematical modeling feasible. In this model, we're assuming that heat transfer occurs only in the radial direction, not axially or circumferentially.

This assumption means that the heat transfer processes can be described using radial coordinates, focusing on changes in temperature from the center of the forearm to its surface. The choice to model the forearm as a one-dimensional cylinder facilitates the use of Pennes' bioheat equation, which predicts how temperature changes within biological tissues.

Using a one-dimensional cylindrical approximation is common in bioheat transfer to reduce complexities in calculations, while still capturing the essential characteristics of the heat transfer process within the forearm.
Metabolic Heat Generation
Metabolic heat generation refers to the heat produced by the body's metabolic processes. This heat is generated as chemical energy from food is converted into mechanical energy and heat needed for maintaining physiological functions.

In the context of the human forearm, we assume a constant metabolic heat generation throughout the muscle tissue. This simplification is key in solving the bioheat equation, as it adds a persistent internal heat source. The rate of metabolic heat generation is represented by \( \dot{e}_m \) and contributes significantly to the internal temperature distribution.
Recognizing the role of metabolic heat is essential for understanding how the human body maintains its temperature and how it affects heat transfer calculations in biological systems.
Thermal Conductivity
Thermal conductivity, represented by the symbol \( k \), is a material-specific property that indicates the efficiency with which heat is conducted through a substance. In the human forearm model, different tissues such as muscle and skin/fat have unique thermal conductivities, \( k_m \) and \( k_{sf} \) respectively.

These values are critical in bioheat transfer analysis, as they determine how quickly and effectively heat can move through these tissues. Higher thermal conductivity implies more efficient heat transfer. In the presented scenario, the choice of thermal conductivities helps in evaluating the heat conduction from deeper tissues to the skin's surface.
Understanding thermal conductivity helps in predicting temperature variations due to different heat transfer processes within the body and in designing better thermal management strategies in medical applications.

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Most popular questions from this chapter

What is the reason for the widespread use of fins on surfaces?

A 1-cm-diameter, 30-cm-long fin made of aluminum \((k=237 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K})\) is attached to a surface at \(80^{\circ} \mathrm{C}\). The surface is exposed to ambient air at \(22^{\circ} \mathrm{C}\) with a heat transfer coefficient of \(11 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\). If the fin can be assumed to bery long, its efficiency is (a) \(0.60\) (b) \(0.67\) (c) \(0.72\) (d) \(0.77\) (e) \(0.88\)

Steam at \(450^{\circ} \mathrm{F}\) is flowing through a steel pipe \(\left(k=8.7 \mathrm{Btu} / \mathrm{h} \cdot \mathrm{ft} \cdot{ }^{\circ} \mathrm{F}\right)\) whose inner and outer diameters are \(3.5\) in and \(4.0\) in, respectively, in an environment at \(55^{\circ} \mathrm{F}\). The pipe is insulated with 2 -in-thick fiberglass insulation \((k=\) \(\left.0.020 \mathrm{Btu} / \mathrm{h} \cdot \mathrm{ft} \cdot{ }^{\circ} \mathrm{F}\right)\). If the heat transfer coefficients on the inside and the outside of the pipe are 30 and \(5 \mathrm{Btu} / \mathrm{h} \cdot \mathrm{ft}^{2} \cdot{ }^{\circ} \mathrm{F}\), respectively, determine the rate of heat loss from the steam per foot length of the pipe. What is the error involved in neglecting the thermal resistance of the steel pipe in calculations?

Hot air is to be cooled as it is forced to flow through the tubes exposed to atmospheric air. Fins are to be added in order to enhance heat transfer. Would you recommend attaching the fins inside or outside the tubes? Why? When would you recommend attaching fins both inside and outside the tubes?

Two finned surfaces are identical, except that the convection heat transfer coefficient of one of them is twice that of the other. For which finned surface is the \((a)\) fin effectiveness and \((b)\) fin efficiency higher? Explain.

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