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Consider laminar natural convection from a vertical hot plate. Will the heat flux be higher at the top or at the bottom of the plate? Why?

Short Answer

Expert verified
Answer: The heat flux will be higher at the bottom of the vertical heated plate in laminar natural convection. This is due to the steeper temperature gradient at the bottom of the plate, as the fluid in contact with the plate is continuously getting heated and rising upwards, promoting a more efficient heat transfer.

Step by step solution

01

Understanding Laminar Natural Convection

Laminar natural convection occurs when a fluid flows around a heated or cooled surface due to the difference in fluid density caused by the temperature differences. As fluid gets heated, it becomes less dense and rises up, while colder fluid nearby moves in to replace the rising heated fluid. This circulation creates a convection current that transfers heat from the surface to the surrounding fluid.
02

Analyzing the Vertical Heated Plate

In the case of a vertical heated plate, the fluid immediately in contact with the plate will get heated and become less dense, prompting it to rise upwards. As the heated fluid rises, it moves away from the plate, allowing colder fluid to move in and take its place near the plate. The fluid close to the bottom of the plate will have a higher temperature gradient compared to the fluid close to the top of the plate since the fluid at the bottom has not yet had time to rise up along the plate and transfer its heat.
03

Determining the Heat Flux Distribution

Heat flux is the amount of heat transferred per unit area within a respective direction. The heat flux will be higher where the temperature gradient is steeper. As mentioned previously, the temperature gradient near the bottom of the plate will be steeper compared to that near the top of the plate. This is due to the fact that the fluid near the bottom is getting continuously heated and is rising, whereas the fluid near the top has already transferred some of its heat and has had time to cool slightly as it moves upwards along the plate.
04

Conclusion

Based on the temperature gradient and fluid motion around the vertical heated plate, it can be concluded that the heat flux will be higher at the bottom of the plate compared to the top. This is because the temperature gradient is steeper near the bottom of the plate, and the fluid there is continuously getting heated and rising upwards in the laminar natural convection process.

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Most popular questions from this chapter

A 0.6-m \(\times 0.6-\mathrm{m}\) horizontal ASTM A240 410S stainless steel plate has its upper surface subjected to convection with cold, quiescent air. The minimum temperature suitable for the stainless steel plate is $-30^{\circ} \mathrm{C}$ (ASME Code for Process Piping, ASME B31.3-2014, Table \(\mathrm{A}-1 \mathrm{M}\) ). If heat is added to the plate at a rate of $70 \mathrm{~W}$, determine the lowest temperature that the air can reach without causing the surface temperature of the plate to cool below the minimum suitable temperature. Evaluate the properties of air at $-50^{\circ} \mathrm{C}$. Is this an appropriate temperature at which to evaluate the air properties?

A vertical 4-ft-high and 6-ft-wide double-pane window consists of two sheets of glass separated by a 1 -in air gap at atmospheric pressure. If the glass surface temperatures across the air gap are measured to be $65^{\circ} \mathrm{F}\( and \)40^{\circ} \mathrm{F}$, determine the rate of heat transfer through the window by \((a)\) natural convection and (b) radiation. Also, determine the \(R\)-value of insulation of this window such that multiplying the inverse of the \(R\)-value by the surface area and the temperature difference gives the total rate of heat transfer through the window. The effective emissivity for use in radiation calculations between two large parallel glass plates can be taken to be \(0.82\).

Consider a flat-plate solar collector placed horizontally on the flat roof of a house. The collector is \(1.5 \mathrm{~m}\) wide and \(4.5 \mathrm{~m}\) long, and the average temperature of the exposed surface of the collector is \(42^{\circ} \mathrm{C}\). Determine the rate of heat loss from the collector by natural convection during a calm day when the ambient air temperature is \(8^{\circ} \mathrm{C}\). Also, determine the heat loss by radiation by taking the emissivity of the collector surface to be \(0.85\) and the effective sky temperature to be \(-15^{\circ} \mathrm{C}\). Answers: $1314 \mathrm{~W}, 1762 \mathrm{~W}$

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Consider an industrial furnace that resembles a 13-ft-long horizontal cylindrical enclosure \(8 \mathrm{ft}\) in diameter whose end surfaces are well insulated. The furnace burns natural gas at a rate of 48 therms/h. The combustion efficiency of the furnace is 82 percent (i.e., 18 percent of the chemical energy of the fuel is lost through the flue gases as a result of incomplete combustion and the flue gases leaving the furnace at high temperature). If the heat loss from the outer surfaces of the furnace by natural convection and radiation is not to exceed 1 percent of the heat generated inside, determine the highest allowable surface temperature of the furnace. Assume the air and wall surface temperature of the room to be \(75^{\circ} \mathrm{F}\), and take the emissivity of the outer surface of the furnace to be \(0.85\).

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