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The Biot number can be thought of as the ratio of (a) the conduction thermal resistance to the convective thermal resistance (b) the convective thermal resistance to the conduction thermal resistance (c) the thermal energy storage capacity to the conduction thermal resistance (d) the thermal energy storage capacity to the convection thermal resistance (e) none of the above

Short Answer

Expert verified
Answer: The correct representation of the Biot number is the conduction thermal resistance to the convective thermal resistance.

Step by step solution

01

Definition of Biot Number

Biot number (Bi) is a dimensionless number that represents the relative importance of convective heat transfer to conductive heat transfer within a solid. It is given by the formula: Bi = h * Lc / k Where: - Bi: Biot number - h: convective heat transfer coefficient (W/m^2.K) - Lc: characteristic length (m) (usually taken as the smallest dimension) - k: thermal conductivity of the solid (W/m.K)
02

Option (a) Analysis

In option (a), the Biot number is presented as the ratio of the conduction thermal resistance to the convective thermal resistance. To analyze this option, let's define the conduction and convective thermal resistance: - Thermal resistance due to conduction (Rc) is given by: Rc = Lc / k; - Thermal resistance due to convection (Rcv) is given by: Rcv = 1 / (h * A); The Biot number (Bi) can also be expressed as: Bi = (Rc / Rcv) = (Rc * h * A) / (1); Since option (a) presents the Biot number in this form, option (a) is a correct representation of the Biot number.
03

Option (b) Analysis

In option (b), the Biot number is presented as the ratio of the convective thermal resistance to the conduction thermal resistance. This option is the inverse of option (a). Thus, Option (b) is incorrect.
04

Option (c) Analysis

In option (c), the Biot number is presented as the ratio of the thermal energy storage capacity to the conduction thermal resistance. This option does not correspond to the definition and formula of the Biot number. Thus, Option (c) is incorrect.
05

Option (d) Analysis

In option (d), the Biot number is presented as the ratio of the thermal energy storage capacity to the convection thermal resistance. This option also does not correspond to the definition and formula of the Biot number. Thus, Option (d) is incorrect.
06

Option (e) Analysis

Option (e) states that none of the above options are correct. Since we have already identified option (a) as the correct representation of the Biot number, option (e) is incorrect.
07

Answer

The correct option that represents the Biot number is: (a) the conduction thermal resistance to the convective thermal resistance.

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Most popular questions from this chapter

A long nickel alloy (ASTM B335) cylindrical rod is used as a component in high-temperature process equipment. The rod has a diameter of $5 \mathrm{~cm}\(; its thermal conductivity, specific heat, and density are \)11 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}, 380 \mathrm{~J} / \mathrm{kg} \cdot \mathrm{K}\(, and \)9.3 \mathrm{~g} / \mathrm{cm}^{3}$, respectively. Occasionally, the rod is submerged in hot fluid for several minutes, where the fluid temperature is \(500^{\circ} \mathrm{C}\) with a convection heat transfer coefficient of \(440 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\). The ASME Code for Process Piping limits the maximum use temperature for ASTM B335 rod to \(427^{\circ} \mathrm{C}\) (ASME B31.32014 , Table A-1M). If the initial temperature of the rod is \(20^{\circ} \mathrm{C}\), how long can the rod be submerged in the hot fluid before reaching its maximum use temperature?

A long 18-cm-diameter bar made of hardwood \((k=\) $\left.0.159 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}, \alpha=1.75 \times 10^{-7} \mathrm{~m}^{2} / \mathrm{s}\right)\( is exposed to air at \)30^{\circ} \mathrm{C}$ with a heat transfer coefficient of \(8.83 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\). If the center temperature of the bar is measured to be \(15^{\circ} \mathrm{C}\) after \(3 \mathrm{~h}\), the initial temperature of the bar is (a) \(11.9^{\circ} \mathrm{C}\) (b) \(4.9^{\circ} \mathrm{C}\) (c) \(1.7^{\circ} \mathrm{C}\) (d) \(0^{\circ} \mathrm{C}\) (e) \(-9.2^{\circ} \mathrm{C}\)

Stainless steel ball bearings $\left(\rho=8085 \mathrm{~kg} / \mathrm{m}^{3}\right.\(, \)k=15.1 \mathrm{~W} / \mathrm{m} \cdot{ }^{\circ} \mathrm{C}, \quad c_{p}=0.480 \mathrm{KJ} / \mathrm{kg} \cdot{ }^{\circ} \mathrm{C}, \quad\( and \)\quad \alpha=3.91 \times\( \)10^{-6} \mathrm{~m}^{2} / \mathrm{s}\( ) having a diameter of \)1.2 \mathrm{~cm}$ are to be quenched in water. The balls leave the oven at a uniform temperature of $900^{\circ} \mathrm{C}\( and are exposed to air at \)30^{\circ} \mathrm{C}$ for a while before they are dropped into the water. If the temperature of the balls is not to fall below \(850^{\circ} \mathrm{C}\) prior to quenching and the heat transfer coefficient in the air is $125 \mathrm{~W} / \mathrm{m}^{2},{ }^{\circ} \mathrm{C}$, determine how long they can stand in the air before being dropped into the water.

What is an infinitely long cylinder? When is it proper to treat an actual cylinder as being infinitely long, and when is it not? For example, is it proper to use this model when finding the temperatures near the bottom or top surfaces of a cylinder? Explain.

Consider the freezing of packaged meat in boxes with refrigerated air. How do \((a)\) the temperature of air, \((b)\) the velocity of air, \((c)\) the capacity of the refrigeration system, and \((d)\) the size of the meat boxes affect the freezing time?

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