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

Air \(\left(c_{p}=1005 \mathrm{~J} / \mathrm{kg} \cdot \mathrm{K}\right)\) enters a cross-flow 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.

A counterflow double-pipe heat exchanger with \(A_{s}=\) \(9.0 \mathrm{~m}^{2}\) is used for cooling a liquid stream \(\left(c_{p}=3.15 \mathrm{~kJ} / \mathrm{kg} \cdot \mathrm{K}\right)\) at a rate of \(10.0 \mathrm{~kg} / \mathrm{s}\) with an inlet temperature of \(90^{\circ} \mathrm{C}\). The coolant \(\left(c_{p}=4.2 \mathrm{~kJ} / \mathrm{kg} \cdot \mathrm{K}\right)\) enters the heat exchanger at a rate of \(8.0 \mathrm{~kg} / \mathrm{s}\) with an inlet temperature of \(10^{\circ} \mathrm{C}\). The plant data gave the following equation for the overall heat transfer coefficient in W/m \({ }^{2} \cdot \mathrm{K}: U=600 /\left(1 / \dot{m}_{c}^{0.8}+2 / \dot{m}_{h}^{0.8}\right)\), where \(\dot{m}_{c}\) and \(\dot{m}_{h}\) are the cold-and hot-stream flow rates in kg/s, respectively. (a) Calculate the rate of heat transfer and the outlet stream temperatures for this unit. (b) The existing unit is to be replaced. A vendor is offering a very attractive discount on two identical heat exchangers that are presently stocked in its warehouse, each with \(A_{s}=5 \mathrm{~m}^{2}\). Because the tube diameters in the existing and new units are the same, the above heat transfer coefficient equation is expected to be valid for the new units as well. The vendor is proposing that the two new units could be operated in parallel, such that each unit would process exactly one-half the flow rate of each of the hot and cold streams in a counterflow manner; hence, they together would meet (or exceed) the present plant heat duty. Give your recommendation, with supporting calculations, on this replacement proposal.

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.

A cross-flow heat exchanger with both fluids unmixed has an overall heat transfer coefficient of \(200 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\), and a heat transfer surface area of \(400 \mathrm{~m}^{2}\). The hot fluid has a heat capacity of \(40,000 \mathrm{~W} / \mathrm{K}\), while the cold fluid has a heat capacity of \(80,000 \mathrm{~W} / \mathrm{K}\). If the inlet temperatures of both hot and cold fluids are \(80^{\circ} \mathrm{C}\) and \(20^{\circ} \mathrm{C}\), respectively, determine (a) the exit temperature of the hot fluid and \((b)\) the rate of heat transfer in the heat exchanger.

A 1 -shell and 2-tube type heat exchanger has an overall heat transfer coefficient of \(300 \mathrm{Btu} / \mathrm{h} \cdot \mathrm{ft}^{2} \cdot{ }^{\circ} \mathrm{F}\). The shell side fluid has a heat capacity rate of \(20,000 \mathrm{Btu} / \mathrm{h} \cdot{ }^{\circ} \mathrm{F}\), while the tube side fluid has a heat capacity rate of \(40,000 \mathrm{Btu} / \mathrm{h} \cdot{ }^{\circ} \mathrm{F}\). The inlet temperatures on the shell side and tube side are \(200^{\circ} \mathrm{F}\) and \(90^{\circ} \mathrm{F}\), respectively. If the total heat transfer area is \(100 \mathrm{ft}^{2}\), determine \((a)\) the heat transfer effectiveness and \((b)\) the actual heat transfer rate in the heat exchanger.

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