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The condenser of a room air conditioner is designed to reject heat at a rate of \(22,500 \mathrm{~kJ} / \mathrm{h}\) from refrigerant- \(134 \mathrm{a}\) as the refrigerant is condensed at a temperature of \(40^{\circ} \mathrm{C}\). Air \(\left(c_{p}=1005 \mathrm{~J} / \mathrm{kg} \cdot \mathrm{K}\right)\) flows across the finned condenser coils, entering at \(25^{\circ} \mathrm{C}\) and leaving at \(32^{\circ} \mathrm{C}\). If the overall heat transfer coefficient based on the refrigerant side is $150 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}$, determine the heat transfer area on the refrigerant side.

Short Answer

Expert verified
Answer: The heat transfer area on the refrigerant side of the finned condenser coils is approximately 3.6232 square meters.

Step by step solution

01

Convert the units of heat rejection rate to the same units as the heat transfer coefficient

The heat rejection rate is given in kJ/h, while the heat transfer coefficient is given in W/m²·K. To make them consistent, we need to convert the heat rejection rate to W (1 kW = 1,000 W and 1 h = 3600 s). $$ Q = 22,500 \frac{kJ}{h}\cdot\frac{1000 W}{kJ}\cdot\frac{1h}{3,600s} = 6,250 W $$ Now that we have \(Q = 6,250 W\), we can move to the next step.
02

Determine the temperature difference between the refrigerant and air

To find the temperature difference, we should first calculate the average air temperature as it flows across the condenser coils. Avg air temperature = \(\frac{T_{inlet} + T_{outlet}}{2}\) Avg air temperature = \(\frac{25 + 32}{2} = 28.5 ^\circ C\) The refrigerant is condensed at 40 degrees Celsius. So, the temperature difference is: $$\Delta T = T_{refrigerant} - T_{avg\,air} = 40 - 28.5 = 11.5 K$$ Now that we have the temperature difference, we can move to the next step.
03

Calculate the mass flow rate of air

Given \(Q = mc_{p}\Delta T\), where \(m\) is the mass flow rate of air, \(c_{p}\) is the specific heat capacity of air (\(1005 J/kg·K\)), and \(\Delta T\) is the temperature difference between the air entering and leaving the condenser coils. We can rearrange the equation to find \(m\): $$ m = \frac{Q}{c_{p}\Delta T} = \frac{6,250}{1005 \times(32 - 25)} = \frac{6,250}{1005 \times 7} = 0.9009\, kg/s $$ Now, we know the mass flow rate of air. We can move to the next step.
04

Determine the heat transfer area on the refrigerant side

We can now use the overall heat transfer coefficient (\(U = 150 W/m²·K\)) to find the heat transfer area (\(A\)). The heat transfer equation is: $$ Q = UA\Delta T $$ We can rearrange this equation to solve for the heat transfer area \(A\): $$ A = \frac{Q}{U\Delta T} = \frac{6,250}{150 \times 11.5} = 3.6232\, m^{2} $$ Therefore, the heat transfer area on the refrigerant side is approximately 3.6232 square meters.

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Most popular questions from this chapter

Air \(\left(c_{p}=1005 \mathrm{~J} / \mathrm{kg} \cdot \mathrm{K}\right)\) enters a crossflow heat exchanger at \(20^{\circ} \mathrm{C}\) at a rate of $3 \mathrm{~kg} / \mathrm{s}$, where it is heated by a hot water stream \(\left(c_{p}=4190 \mathrm{~J} / \mathrm{kg} \cdot \mathrm{K}\right)\) that enters the heat exchanger at \(70^{\circ} \mathrm{C}\) at a rate of $1 \mathrm{~kg} / \mathrm{s}$. Determine the maximum heat transfer rate and the outlet temperatures of both fluids for that case.

Glycerin \(\left(c_{p}=2400 \mathrm{~J} / \mathrm{kg} \cdot \mathrm{K}\right)\) at \(20^{\circ} \mathrm{C}\) and \(0.5 \mathrm{~kg} / \mathrm{s}\) is to be heated by ethylene glycol $\left(c_{p}=2500 \mathrm{~J} / \mathrm{kg} \cdot \mathrm{K}\right)\( at \)60^{\circ} \mathrm{C}$ and the same mass flow rate in a thin-walled double-pipe parallelflow heat exchanger. If the overall heat transfer coefficient is \(380 \mathrm{~W} / \mathrm{m}^{2}\). \(\mathrm{K}\) and the heat transfer surface area is \(6.5 \mathrm{~m}^{2}\), determine \((a)\) the rate of heat transfer and \((b)\) the outlet temperatures of the glycerin and the glycol.

Consider a double-pipe counterflow heat exchanger. In order to enhance heat transfer, the length of the heat exchanger is now doubled. Do you think its effectiveness will also double?

Consider a condenser unit (shell and tube heat exchanger) of an HVAC facility where saturated refrigerant \(\mathrm{R}-134 \mathrm{a}\) at a saturation pressure of \(1318.6 \mathrm{kPa}\) and at a rate of $2.5 \mathrm{~kg} / \mathrm{s}$ flows through thin-walled copper tubes. The refrigerant enters the condenser as saturated vapor and we wish to have a saturated liquid refrigerant at the exit. The cooling of refrigerant is carried out by cold water that enters the heat exchanger at \(10^{\circ} \mathrm{C}\) and exits at \(40^{\circ} \mathrm{C}\). Assuming the initial overall heat transfer coefficient of the heat exchanger to be $3500 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}$, determine the surface area of the heat exchanger and the mass flow rate of cooling water for complete condensation of the refrigerant. In practice, over a long period of time, fouling occurs inside the heat exchanger that reduces its overall heat transfer coefficient and causes the mass flow rate of cooling water to increase. Increase in the mass flow rate of cooling water will require additional pumping power, making the heat exchange process uneconomical. To prevent the condenser unit from underperforming, assume that fouling has occurred inside the heat exchanger and has reduced its overall heat transfer coefficient by 20 percent. For the same inlet temperature and flow rate of refrigerant, determine the new flow rate of cooling water to ensure complete condensation of the refrigerant at the heat exchanger exit.

Consider a water-to-water double-pipe heat exchanger whose flow arrangement is not known. The temperature measurements indicate that the cold water enters at \(20^{\circ} \mathrm{C}\) and leaves at \(50^{\circ} \mathrm{C}\), while the hot water enters at \(80^{\circ} \mathrm{C}\) and leaves at \(45^{\circ} \mathrm{C}\). Do you think this is a parallel-flow or counterflow heat exchanger? Explain.

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