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Cold water \(\left(c_{p}=4.18 \mathrm{~kJ} / \mathrm{kg} \cdot \mathrm{K}\right)\) enters a counterflow heat exchanger at \(18^{\circ} \mathrm{C}\) at a rate of \(0.7 \mathrm{~kg} / \mathrm{s}\) where it is heated by hot air \(\left(c_{p}=1.0 \mathrm{~kJ} / \mathrm{kg} \cdot \mathrm{K}\right)\) that enters the heat exchanger at \(50^{\circ} \mathrm{C}\) at a rate of \(1.6 \mathrm{~kg} / \mathrm{s}\) and leaves at \(25^{\circ} \mathrm{C}\). The maximum possible outlet temperature of the cold water is (a) \(25.0^{\circ} \mathrm{C}\) (b) \(32.0^{\circ} \mathrm{C}\) (c) \(35.5^{\circ} \mathrm{C}\) (d) \(39.7^{\circ} \mathrm{C}\) (e) \(50.0^{\circ} \mathrm{C}\)

Short Answer

Expert verified
Answer: The maximum possible outlet temperature of the cold water is 32.0°C.

Step by step solution

01

Calculate heat gained by the cold water and heat lost by the hot air

In a heat exchanger, the heat gained by the cold medium is equal to the heat lost by the hot medium. We can calculate the heat gained by the cold water (Q_cw) and the heat lost by the hot air (Q_ha) using the following formula: Q = mass_flow_rate * c_p * ΔT Where Q is the heat transfer, mass_flow_rate is the mass flow rate of the medium, c_p is the heat capacity of the medium, and ΔT is the change in temperature of the medium. First, let's calculate the heat gained by the cold water (Q_cw): Q_cw = mass_flow_rate_cw * c_p_cw * ΔT_cw Where mass_flow_rate_cw = 0.7 kg/s, c_p_cw = 4.18 kJ/kg·K, and ΔT_cw = T_out_cw - 18°C. Now, let's calculate the heat lost by the hot air (Q_ha): Q_ha = mass_flow_rate_ha * c_p_ha * ΔT_ha Where mass_flow_rate_ha = 1.6 kg/s, c_p_ha = 1.0 kJ/kg·K, and ΔT_ha = 50°C - 25°C.
02

Apply energy conservation principle

As the heat gained by the cold water is equal to the heat lost by the hot air, we can equate the above equations: mass_flow_rate_cw * c_p_cw * ΔT_cw = mass_flow_rate_ha * c_p_ha * ΔT_ha From the given data, we can plug in the values: 0.7 * 4.18 * (T_out_cw - 18) = 1.6 * 1.0 * (50 - 25)
03

Solve for the maximum possible outlet temperature of the cold water (T_out_cw)

Now, we will solve this equation to find the maximum possible outlet temperature of the cold water (T_out_cw): 2.924 * (T_out_cw - 18) = 40 T_out_cw - 18 = 13.69189 T_out_cw = 31.69189 ≈ 32.0°C Therefore, the maximum possible outlet temperature of the cold water is 32.0°C, which corresponds to option (b).

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Key Concepts

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

Counterflow Heat Exchanger
In a counterflow heat exchanger, two fluids flow in opposite directions, allowing for efficient heat transfer. This design improves the efficiency of the heat exchange process because the temperature gradient between the fluids remains more consistent throughout the exchanger. For example, in our exercise, cold water and hot air are the two fluids exchanging heat. The cold water is heated up by the hot air as both fluids pass each other in opposite directions. This setup can achieve higher temperatures of the heated fluid close to the incoming temperature of the hot fluid, which is an inherent benefit over other designs, like parallel flow heat exchangers.

Another benefit of a counterflow heat exchanger is that it can approach the temperature of the hot fluid more closely than other types. In the scenario provided, achieving a significant temperature rise in the cold water would be primarily due to the effectiveness of the counterflow design.
Heat Capacity
Heat capacity, often denoted as cp, is the amount of thermal energy required to raise the temperature of a unit mass of a substance by one degree Celsius (or Kelvin, as the scale increment is the same). It is a fundamental property that depends on the material's physical composition. In the context of our exercise, the cold water has a cp of 4.18 kJ/kg·K, meaning each kilogram of water requires 4.18 kJ of heat to raise its temperature by one Kelvin. Conversely, the hot air has a cp of 1.0 kJ/kg·K. These values play a pivotal role in determining how much thermal energy is transferred between substances in the heat exchanger.
Mass Flow Rate
Mass flow rate is a measure of the amount of mass passing through a cross-section per unit of time, usually denoted in kilograms per second (kg/s). It is a crucial factor in heat exchanger calculations, as it determines the potential amount of heat that can be transferred between the hot and cold fluids. In our exercise, the mass flow rate of cold water is 0.7 kg/s, while the hot air has a flow rate of 1.6 kg/s. When we multiply the mass flow rate by the fluid's heat capacity and the temperature change (∆T), it gives us the rate of heat transfer for that fluid, which allows us to apply the principle of thermal energy conservation.
Thermal Energy Conservation
Thermal energy conservation is a principle stating that, in the absence of external work being done or mass transfer, the total amount of heat energy within a closed system remains constant. In the context of a heat exchanger, this means that the heat lost by one fluid must be equal to the heat gained by the other fluid. Our exercise required us to apply this principle by equating the heat gained by the cold water to the heat lost by the hot air.

The formula involves the mass flow rate, heat capacity, and temperature change (∆T) for both fluids. Since energy is being conserved and no heat is lost to the environment, the equation from the cold water's perspective must balance with the one from the hot air's perspective. This understanding allows us to solve for unknown variables such as the maximum possible outlet temperature of the cold water.

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Most popular questions from this chapter

A performance test is being conducted on a double pipe counter flow heat exchanger that carries engine oil and water at a flow rate of \(2.5 \mathrm{~kg} / \mathrm{s}\) and \(1.75 \mathrm{~kg} / \mathrm{s}\), respectively. Since the heat exchanger has been in service over a long period of time it is suspected that the fouling might have developed inside the heat exchanger that might have affected the overall heat transfer coefficient. The test to be carried out is such that, for a designed value of the overall heat transfer coefficient of \(450 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\) and a surface area of \(7.5 \mathrm{~m}^{2}\), the oil must be heated from \(25^{\circ} \mathrm{C}\) to \(55^{\circ} \mathrm{C}\) by passing hot water at \(100^{\circ} \mathrm{C}\left(c_{p}=4206 \mathrm{~J} / \mathrm{kg} \cdot \mathrm{K}\right)\) at the flow rates mentioned above. Determine if the fouling has affected the overall heat transfer coefficient. If yes, then what is the magnitude of the fouling resistance?

A single-pass cross-flow heat exchanger is used to cool jacket water \(\left(c_{p}=1.0 \mathrm{Btu} / \mathrm{lbm} \cdot{ }^{\circ} \mathrm{F}\right)\) of a diesel engine from \(190^{\circ} \mathrm{F}\) to \(140^{\circ} \mathrm{F}\), using air \(\left(c_{p}=0.245 \mathrm{Btu} / \mathrm{lbm} \cdot{ }^{\circ} \mathrm{F}\right)\) with inlet temperature of \(90^{\circ} \mathrm{F}\). Both air flow and water flow are unmixed. If the water and air mass flow rates are \(92,000 \mathrm{lbm} / \mathrm{h}\) and \(400,000 \mathrm{lbm} / \mathrm{h}\), respectively, determine the log mean temperature difference for this heat exchanger.

11-100 E(S) Reconsider Prob. 11-99. Using EES (or other) software, investigate the effects of the inlet temperature of hot water and the heat transfer coefficient on the rate of heat transfer and the surface area. Let the inlet temperature vary from \(60^{\circ} \mathrm{C}\) to \(120^{\circ} \mathrm{C}\) and the overall heat transfer coefficient from \(750 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\) to \(1250 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\). Plot the rate of heat transfer and surface area as functions of the inlet temperature and the heat transfer coefficient, and discuss the results. 11-101E A thin-walled double-pipe, counter-flow heat exchanger is to be used to cool oil \(\left(c_{p}=0.525 \mathrm{Btu} / \mathrm{lbm} \cdot{ }^{\circ} \mathrm{F}\right)\) from \(300^{\circ} \mathrm{F}\) to \(105^{\circ} \mathrm{F}\) at a rate of \(5 \mathrm{lbm} / \mathrm{s}\) by water \(\left(c_{p}=\right.\) \(1.0 \mathrm{Btu} / \mathrm{lbm} \cdot{ }^{\circ} \mathrm{F}\) ) that enters at \(70^{\circ} \mathrm{F}\) at a rate of \(3 \mathrm{lbm} / \mathrm{s}\). The diameter of the tube is 5 in and its length is \(200 \mathrm{ft}\). Determine the overall heat transfer coefficient of this heat exchanger using (a) the LMTD method and \((b)\) the \(\varepsilon-\mathrm{NTU}\) method.

Hot water coming from the engine is to be cooled by ambient air in a car radiator. The aluminum tubes in which the water flows have a diameter of \(4 \mathrm{~cm}\) and negligible thickness. Fins are attached on the outer surface of the tubes in order to increase the heat transfer surface area on the air side. The heat transfer coefficients on the inner and outer surfaces are 2000 and \(150 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\), respectively. If the effective surface area on the finned side is 10 times the inner surface area, the overall heat transfer coefficient of this heat exchanger based on the inner surface area is (a) \(150 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\) (b) \(857 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\) (c) \(1075 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\) (d) \(2000 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\) (e) \(2150 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\)

Cold water \(\left(c_{p}=4.18 \mathrm{~kJ} / \mathrm{kg} \cdot \mathrm{K}\right)\) enters a cross-flow heat exchanger at \(14^{\circ} \mathrm{C}\) at a rate of \(0.35 \mathrm{~kg} / \mathrm{s}\) where it is heated by hot air \(\left(c_{p}=1.0 \mathrm{~kJ} / \mathrm{kg} \cdot \mathrm{K}\right)\) that enters the heat exchanger at \(65^{\circ} \mathrm{C}\) at a rate of \(0.8 \mathrm{~kg} / \mathrm{s}\) and leaves at \(25^{\circ} \mathrm{C}\). Determine the maximum outlet temperature of the cold water and the effectiveness of this heat exchanger.

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