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Saturated water vapor at \(100^{\circ} \mathrm{C}\) condenses in the shell side of a one-shell and two-tube heat exchanger with a surface area of $0.5 \mathrm{~m}^{2}\( and an overall heat transfer coefficient of \)2000 \mathrm{~W} / \mathrm{m}^{2}\(. \)\mathrm{K}\(. If cold water \)\left(c_{p c}=4179 \mathrm{~J} / \mathrm{kg} \cdot \mathrm{K}\right.\( ) flowing at \)0.5 \mathrm{~kg} / \mathrm{s}\( enters the tube side at \)15^{\circ} \mathrm{C}$, determine the outlet temperature of the cold water and the heat transfer rate for the heat exchanger.

Short Answer

Expert verified
Answer: The outlet temperature of the cold water is 55.62°C, and the heat transfer rate is 85000 W.

Step by step solution

01

Calculate the heat transfer needed for the saturated water vapor to condense

First, we need to determine the heat transfer needed for the saturated water vapor to condense at \(100^{\circ}\mathrm{C}\). We can do this by using the heat transfer formula: $$q = U \cdot A \cdot(T_{hot} - T_{cold})$$ Where, \(q\) is the heat transfer, \(U\) is the overall heat transfer coefficient, \(A\) is the surface area of the heat exchanger, \(T_{hot}\) is the temperature of the hot fluid (saturated water vapor), and \(T_{cold}\) is the inlet temperature of the cold fluid (water). From the problem statement, we have the values: \(U = 2000 \frac{W}{m^2 K}\) \(A = 0.5 m^2\) \(T_{hot}=100^{\circ}\mathrm{C}\) \(T_{cold}=15^{\circ}\mathrm{C}\) Using these values, we can calculate the heat transfer needed for the saturated water vapor to condense: $$ q = 2000 \frac{W}{m^2 K} \cdot 0.5 m^2 \cdot (100^{\circ}\mathrm{C} - 15^{\circ}\mathrm{C})$$ $$ q = 85000 W$$
02

Apply the energy balance equation to determine the outlet temperature

Now that we have the heat transfer, we can apply the energy balance equation to the cold water. The energy balance equation can be expressed as: $$\dot{m}c_p (T_{out} - T_{in}) = q$$ Where, \(\dot{m}\) is the mass flow rate of the cold water, \(c_p\) is the specific heat capacity of the cold water, \(T_{out}\) is the outlet temperature of the cold water, and \(T_{in}\) is the inlet temperature of the cold water. From the problem statement, we have the values: \(\dot{m} = 0.5 \frac{kg}{s}\) \(c_p = 4179 \frac{J}{kg \cdot K}\) \(T_{in} = 15^{\circ}\mathrm{C}\) Re-arrange the equation to solve for \(T_{out}\): $$T_{out} = T_{in} + \frac{q}{\dot{m}c_p}$$ Now, plug in the values to calculate the outlet temperature: $$T_{out} = 15^{\circ}\mathrm{C} + \frac{85000 W}{0.5 \frac{kg}{s} \cdot 4179 \frac{J}{kg \cdot K}}$$ $$T_{out} = 15^{\circ}\mathrm{C} + 40.62^{\circ}\mathrm{C}$$ $$T_{out} = 55.62^{\circ}\mathrm{C}$$
03

Calculate the heat transfer rate

Since we have already calculated the heat transfer in step 1, the heat transfer rate for the heat exchanger is: $$q = 85000 W$$ So, the outlet temperature of cold water is \(55.62^{\circ}\mathrm{C}\), and the heat transfer rate is \(85000 W\).

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Most popular questions from this chapter

A one-shell and two-tube-type heat exchanger has an overall heat transfer coefficient of $300 \mathrm{Btu} / \mathrm{h} \cdot \mathrm{ft}^{2}{ }^{\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.

In a one-shell and two-tube heat exchanger, cold water with inlet temperature of \(20^{\circ} \mathrm{C}\) is heated by hot water supplied at the inlet at \(80^{\circ} \mathrm{C}\). The cold and hot water flow rates are $5000 \mathrm{~kg} / \mathrm{h}\( and \)10,000 \mathrm{~kg} / \mathrm{h}$, respectively. If the shell-andtube heat exchanger has a \(U A_{s}\) value of \(11,600 \mathrm{~W} / \mathrm{K}\), determine the cold water and hot water outlet temperatures. Assume $c_{p c}=4178 \mathrm{~J} / \mathrm{kg} \cdot \mathrm{K}\( and \)c_{p t}=4188 \mathrm{~J} / \mathrm{kg} \cdot \mathrm{K}$.

Consider a closed-loop heat exchanger that carries exit water $\left(c_{p}=1 \mathrm{Btu} / \mathrm{lbm} \cdot{ }^{\circ} \mathrm{F}\right.$ and \(\left.\rho=62.4 \mathrm{lbm} / \mathrm{ft}^{3}\right)\) of a condenser side initially at \(100^{\circ} \mathrm{F}\). The water flows through a 500 -ft-long stainless steel pipe of 1 in inner diameter immersed in a large lake. The temperature of lake water surrounding the heat exchanger is $45^{\circ} \mathrm{F}$. The overall heat transfer coefficient of the heat exchanger is estimated to be $250 \mathrm{Btu} / \mathrm{h} \cdot \mathrm{ft}^{2}{ }^{\circ} \mathrm{F}$. What is the exit temperature of the water from the immersed heat exchanger if it flows through the pipe at an average velocity of \(9 \mathrm{ft} / \mathrm{s}\) ? Use the \(\varepsilon-N T U\) method for analysis.

Saturated water vapor at \(40^{\circ} \mathrm{C}\) is to be condensed as it flows through the tubes of an air-cooled condenser at a rate of $0.2 \mathrm{~kg} / \mathrm{s}$. The condensate leaves the tubes as a saturated liquid at \(40^{\circ} \mathrm{C}\). The rate of heat transfer to air is (a) \(34 \mathrm{~kJ} / \mathrm{s}\) (b) \(268 \mathrm{~kJ} / \mathrm{s}\) (c) \(453 \mathrm{~kJ} / \mathrm{s}\) (d) \(481 \mathrm{~kJ} / \mathrm{s}\) (e) \(515 \mathrm{~kJ} / \mathrm{s}\)

A shell-and-tube heat exchanger with two shell passes and 12 tube passes is used to heat water $\left(c_{p}=4180 \mathrm{~J} / \mathrm{kg} \cdot \mathrm{K}\right)\( with ethylene glycol \)\left(c_{p}=2680 \mathrm{~J} / \mathrm{kg} \cdot \mathrm{K}\right)\(. Water enters the tubes at \)22^{\circ} \mathrm{C}\( at a rate of \)0.8 \mathrm{~kg} / \mathrm{s}$ and leaves at \(70^{\circ} \mathrm{C}\). Ethylene glycol enters the shell at $110^{\circ} \mathrm{C}\( and leaves at \)60^{\circ} \mathrm{C}$. If the overall heat transfer coefficient based on the tube side is $280 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}$, determine the rate of heat transfer and the heat transfer surface area on the tube side.

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