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A \(0.5-\mathrm{m} \times 0.5-\mathrm{m}\) vertical ASTM A240 410S stainless steel plate has one surface subjected to convection with a cold, quiescent gas at \(-70^{\circ} \mathrm{C}\). The type of cold gas that the plate surface is exposed to alternates between carbon dioxide and hydrogen. The minimum temperature suitable for the stainless steel plate is \(-30^{\circ} \mathrm{C}\) (ASME Code for Process Piping, ASME B31.3-2014, Table A-1M). Determine the heat addition rate necessary for keeping the plate surface temperature from dropping below the minimum suitable temperature, such that it is applicable to both carbon dioxide gas and hydrogen gas.

Short Answer

Expert verified
Answer: The main goal is to ensure that the surface temperature of the steel plate does not drop below -30°C for both carbon dioxide and hydrogen gases.

Step by step solution

01

State the convection heat transfer equation

The convection heat transfer equation is given by: \(q = hA(T_s - T_\infty)\) where \(q\) is the heat transfer rate, \(h\) is the convection heat transfer coefficient, \(A\) is the surface area, \(T_s\) is the surface temperature, and \(T_\infty\) is the fluid temperature.
02

Calculate the convective heat transfer coefficient for carbon dioxide and hydrogen

Before we calculate the needed heat addition rate, we would need the heat transfer coefficients for carbon dioxide and hydrogen. However, this exercise does not provide sufficient information to directly compute these coefficients. You must be provided with additional values, such as fluid properties (thermal conductivity, viscosity, etc.) or relationships that allow calculating the heat transfer coefficients. Assuming that we have these heat transfer coefficients for carbon dioxide and hydrogen (\(h_{CO_2}\), and \(h_{H_2}\)), we can proceed to the next step.
03

Calculate the surface area of the steel plate

Given that the steel plate dimensions are 0.5 m x 0.5 m, we can calculate its surface area as follows: \(A = 0.5\,\text{m} \times 0.5\,\text{m} = 0.25\,\text{m}^2\)
04

Determine the convective heat transfer rate for carbon dioxide and hydrogen

Now, we can determine the convective heat transfer rate for both gases using the convection equation: 1. Carbon dioxide: \(q_{CO_2} = h_{CO_2} A (T_s - T_\infty)\) 2. Hydrogen: \(q_{H_2} = h_{H_2} A (T_s - T_\infty)\)
05

Determine the heat addition rate required for both gases

As we need to determine the heat addition rate such that it is applicable to both gases, we would choose the maximum heat transfer rate found in step 4: \(q_{required} = \max\{q_{CO_2},\,q_{H_2}\}\) The heat addition rate required to keep the plate surface temperature from dropping below -30°C for both carbon dioxide gas and hydrogen gas will be \(q_{required}\).

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Most popular questions from this chapter

A \(0.5-\mathrm{m} \times 0.5-\mathrm{m}\) vertical ASTM B152 copper plate has one surface subjected to convection with hot, quiescent air. The maximum use temperature for the ASTM B152 copper plate is \(260^{\circ} \mathrm{C}\) (ASME Code for Process Piping, ASME B31.3-2014, Table A-1M). If the rate of heat removal from the plate is \(90 \mathrm{~W}\), determine the maximum temperature that the air can reach without causing the surface temperature of the copper plate to increase above \(260^{\circ} \mathrm{C}\). Evaluate the properties of air at \(300^{\circ} \mathrm{C}\). Is this an appropriate temperature to evaluate the air properties?

The upper and lower compartments of a wellinsulated container are separated by two parallel sheets of glass with an airspace between them. One of the compartments is to be filled with a hot fluid and the other with a cold fluid. If it is desired that heat transfer between the two compartments be minimal, would you recommend putting the hot fluid into the upper or the lower compartment of the container? Why?

A \(0.6-\mathrm{m} \times 0.6-\mathrm{m}\) horizontal ASTM A203 B steel plate has its lower surface subjected to convection with cold, quiescent hydrogen gas at \(-70^{\circ} \mathrm{C}\). The minimum temperature suitable for the steel plate is \(-30^{\circ} \mathrm{C}\) (ASME Code for Process Piping, ASME B31.3-2014, Table A-1M). The lower plate surface has an emissivity of \(0.3\), and thermal radiation exchange occurs between the lower plate surface and the surroundings at \(-70^{\circ} \mathrm{C}\). Determine the heat addition rate necessary for keeping the lower plate surface temperature from dropping below the minimum suitable temperature.

Hot engine oil is being transported in a horizontal pipe $\left(k=15 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}, D_{i}=5 \mathrm{~cm}\right)$ with a wall thickness of \(5 \mathrm{~mm}\). The pipe is covered with a \(5-\mathrm{mm}\)-thick layer of insulation $(k=0.15 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K})\(. A length of \)2 \mathrm{~m}$ of the outer surface is exposed to cool air at \(10^{\circ} \mathrm{C}\). If the pipe inner surface temperature is at \(90^{\circ} \mathrm{C}\), determine the outer surface temperature. Hint: The pipe outer surface temperature has to be found iteratively. Begin the calculations by using a film temperature of $50^{\circ} \mathrm{C}$.

Consider a double-pane window whose airspace is flashed and filled with argon gas. How will replacing the air in the gap with argon affect \((a)\) convection and \((b)\) radiation heat transfer through the window?

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