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Steam is to be condensed on the shell side of a 1 -shellpass and 8-tube-passes condenser, with 50 tubes in each pass, at \(30^{\circ} \mathrm{C}\left(h_{f g}=2431 \mathrm{~kJ} / \mathrm{kg}\right)\). Cooling water \(\left(c_{p}=4180 \mathrm{~J} / \mathrm{kg} \cdot \mathrm{K}\right)\) enters the tubes at \(15^{\circ} \mathrm{C}\) at a rate of \(1800 \mathrm{~kg} / \mathrm{h}\). The tubes are thin-walled, and have a diameter of \(1.5 \mathrm{~cm}\) and length of \(2 \mathrm{~m}\) per pass. If the overall heat transfer coefficient is \(3000 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\), determine \((a)\) the rate of heat transfer and \((b)\) the rate of condensation of steam.

Short Answer

Expert verified
Question: Calculate (a) the rate of heat transfer and (b) the rate of condensation of steam in a condenser. Solution: (a) The rate of heat transfer is 169113.3 W. (b) The rate of condensation of steam is 250.2 kg/h.

Step by step solution

01

Calculate the rate of heat transfer

The rate of heat transfer (Q) can be found using the following formula: \[ Q = U \cdot A \cdot \Delta T \] Where: - Q is the rate of heat transfer - U is the overall heat transfer coefficient - A is the surface area of the tubes - ΔT is the temperature difference between the cooling water and the steam First, let's calculate the total surface area of the tubes (A) using the given diameter (D) and length (L) per pass, as well as the total number of tubes (N_tubes): \[ A = N_{tubes} \cdot \pi D \cdot L \] Using the given values, we have: \[ A = 8 \times 50 \times \pi \times 0.015 \mathrm{m} \times 2\mathrm{m} = 3.7699\mathrm{m}^2 \] Next, we need to calculate the temperature difference (ΔT) between the water and the steam. As the initial temperature of the cooling water is given, and we know the condensing temperature of the steam, we can use these directly: \[ \Delta T = 30^{\circ} \mathrm{C} - 15^{\circ} \mathrm{C} = 15 \mathrm{K} \] Now, we can substitute these values into the heat transfer equation to obtain the rate of heat transfer (Q): \[ Q = 3000 \frac{\mathrm{W}}{\mathrm{m}^2 \cdot \mathrm{K}} \cdot 3.7699 \mathrm{m}^2 \cdot 15\mathrm{K} = 169113.3\mathrm{W} \] So, \((a)\) the rate of heat transfer is 169113.3 W.
02

Calculate the rate of condensation of steam

The rate of condensation of steam (m) can be found by dividing the rate of heat transfer by the specific enthalpy of vaporization (h_fg): \[ m = \frac{Q}{h_{fg}} \] We are given that the specific enthalpy of vaporization is 2431 kJ/kg, which we can convert to W/kg: \[ h_{fg} = 2431 \frac{\mathrm{kJ}}{\mathrm{kg}} \cdot \frac{1000 \mathrm{W}}{1 \mathrm{kJ}} = 2431000 \frac{\mathrm{W}}{\mathrm{kg}} \] Now, we can substitute these values into the above formula to obtain the rate of condensation of steam (m): \[ m = \frac{169113.3\mathrm{W}}{2431000 \frac{\mathrm{W}}{\mathrm{kg}}} = 0.0695 \frac{\mathrm{kg}}{\mathrm{s}} \] To convert the rate of condensation to kg/h, we multiply by the conversion factor between seconds and hours: \[ m_{\mathrm{h}} = 0.0695 \frac{\mathrm{kg}}{\mathrm{s}} \cdot \frac{3600 \mathrm{s}}{1 \mathrm{h}} = 250.2 \frac{\mathrm{kg}}{\mathrm{h}} \] So, \((b)\) the rate of condensation of steam is 250.2 kg/h.

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Key Concepts

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

Condenser Design
In a thermal system, a condenser plays a vital role by converting vapor into liquid, primarily by heat removal through a cooling medium. A well-designed condenser, such as the one in this exercise, maximizes heat exchangement effectiveness. This particular design involves a 1-shell pass and 8-tube passes configuration, which means the steam flows once through the shell, while the cooling water passes through the tubes eight times.
This setup enhances heat transfer efficiency by maximizing contact time and area between the steam and cooling water. With 50 tubes per pass, a total of 400 tubes facilitate efficient heat dissipation.
Key design parameters include tube diameter, length, and material, all contributing to effective heat transfer. Proper selection of these parameters ensures efficient energy transfer and optimal condensation performance.
Rate of Condensation
The rate of condensation is a measure of how quickly vapor, like steam, is converted into liquid. This process is heavily reliant on the rate of heat transfer within the system.
To calculate the condensation rate, the heat removed from the steam must be known, as this determines how much steam is condensed. Dividing this rate of heat transfer by the latent heat of vaporization provides the amount of steam converted to liquid per unit time.
This exercise showed a condensation rate of 0.0695 kg/s, equating to 250.2 kg/h. By understanding this rate, engineers can optimize condenser operations, ensuring that the cooling system meets the required performance without exceeding water capacity or energy costs.
Overall Heat Transfer Coefficient
In a heat exchanger, the overall heat transfer coefficient, symbolized as 'U', is crucial for determining how effectively heat is conducted through the materials separating hot and cold fluids.
This coefficient is affected by factors like material conductivity, surface area, and temperature differences. In the exercise, a U-value of 3000 W/m²•K signifies efficient thermal conductance, indicating that the condenser's design supports rapid heat exchange.
An accurate determination of 'U' helps in calculating the heat transfer rate, crucial for sizing components and optimizing thermal efficiency. Such precision allows for predictability in system performance, ensuring that heat exchangers provide the desired cooling effects.
Latent Heat of Vaporization
Latent heat of vaporization represents the amount of energy required to convert a unit mass of a liquid into vapor without changing its temperature. This property is fundamental in processes involving phase change, such as condensation.
In the given exercise, the latent heat of vaporization for steam at 30°C is 2431 kJ/kg. This value informs the heat energy necessary to convert each kilogram of steam to water.
Understanding this concept allows engineers to calculate exactly how much heat needs to be removed in the process of condensation, which in turn dictates the condenser capacity and performance requirements, balancing energy efficiency with system demands.

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Most popular questions from this chapter

A test is conducted to determine the overall heat transfer coefficient in a shell-and-tube oil-to-water heat exchanger that has 24 tubes of internal diameter \(1.2 \mathrm{~cm}\) and length \(2 \mathrm{~m}\) in a single shell. Cold water \(\left(c_{p}=4180 \mathrm{~J} / \mathrm{kg} \cdot \mathrm{K}\right)\) enters the tubes at \(20^{\circ} \mathrm{C}\) at a rate of \(3 \mathrm{~kg} / \mathrm{s}\) and leaves at \(55^{\circ} \mathrm{C}\). Oil \(\left(c_{p}=2150 \mathrm{~J} / \mathrm{kg} \cdot \mathrm{K}\right)\) flows through the shell and is cooled from \(120^{\circ} \mathrm{C}\) to \(45^{\circ} \mathrm{C}\). Determine the overall heat transfer coefficient \(U_{i}\) of this heat exchanger based on the inner surface area of the tubes.

Consider a double-pipe heat exchanger with a tube diameter of \(10 \mathrm{~cm}\) and negligible tube thickness. The total thermal resistance of the heat exchanger was calculated to be \(0.025 \mathrm{~K} / \mathrm{W}\) when it was first constructed. After some prolonged use, fouling occurs at both the inner and outer surfaces with the fouling factors \(0.00045 \mathrm{~m}^{2} \cdot \mathrm{K} / \mathrm{W}\) and \(0.00015 \mathrm{~m}^{2} \cdot \mathrm{K} / \mathrm{W}\), respectively. The percentage decrease in the rate of heat transfer in this heat exchanger due to fouling is (a) \(2.3 \%\) (b) \(6.8 \%\) (c) \(7.1 \%\) (d) \(7.6 \%\) (e) \(8.5 \%\)

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 a rate of \(2.5 \mathrm{~kg} / \mathrm{s}\) flows through thin-walled copper tubes. The refrigerant enters the condenser as saturated vapor and it is desired 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 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 under performance, assume that fouling has occurred inside the heat exchanger and has reduced its overall heat transfer coefficient by \(20 \%\). 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.

Write an essay on the static and dynamic types of regenerative heat exchangers and compile information about the manufacturers of such heat exchangers. Choose a few models by different manufacturers and compare their costs and performance.

Hot exhaust gases of a stationary diesel engine are to be used to generate steam in an evaporator. Exhaust gases \(\left(c_{p}=1051 \mathrm{~J} / \mathrm{kg} \cdot \mathrm{K}\right)\) enter the heat exchanger at \(550^{\circ} \mathrm{C}\) at a rate of \(0.25 \mathrm{~kg} / \mathrm{s}\) while water enters as saturated liquid and evaporates at \(200^{\circ} \mathrm{C}\left(h_{f g}=1941 \mathrm{~kJ} / \mathrm{kg}\right)\). The heat transfer surface area of the heat exchanger based on water side is \(0.5 \mathrm{~m}^{2}\) and overall heat transfer coefficient is \(1780 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\). Determine the rate of heat transfer, the exit temperature of exhaust gases, and the rate of evaporation of water.

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