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A crossflow 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 the exit temperature of the cold fluid.

Short Answer

Expert verified
Answer: The exit temperature of the cold fluid is 80°C.

Step by step solution

01

Calculate the heat transfer rate

In a heat exchanger, the heat transfer rate (\(Q\)) can be calculated using the overall heat transfer coefficient (\(U\)), the heat transfer surface area (\(A\)) and the temperature difference between the hot and cold fluids (\(\Delta T\)). The formula is as follows: $$Q = UA \Delta T$$ For our problem, we have \(U = 200 \mathrm{~W/m^2\cdot K}\), \(A = 400 \mathrm{~m^2}\), and the temperature difference between the hot and cold fluids at the inlet is given as \(80^{\circ} \mathrm{C} - 20^{\circ} \mathrm{C} = 60^{\circ} \mathrm{C}\). Substitute these values into the formula above: $$Q = 200 \mathrm{~W/m^2\cdot K} \times 400 \mathrm{~m^2} \times (60^{\circ} \mathrm{C})$$
02

Calculate the exit temperature of the cold fluid

Now we will apply the energy balance equation to find the exit temperature of the cold fluid (\(T_{c,out}\)). The energy balance equation is as follows: $$Q = C_{c}(T_{c,out} - T_{c,in})$$ Where \(C_{c}\) is the heat capacity of the cold fluid, and \(T_{c,in}\) is the inlet temperature of the cold fluid. For our problem, \(C_{c} = 80,000 \mathrm{~W/K}\) and \(T_{c,in} = 20^{\circ} \mathrm{C}\). Plugging values from step 1: $$200 \mathrm{~W/m^2\cdot K} \times 400 \mathrm{~m^2} \times (60^{\circ} \mathrm{C}) = 80,000 \mathrm{~W/K}(T_{c,out} - 20^{\circ} \mathrm{C})$$ Now we will solve for \(T_{c,out}\): $$T_{c,out} = \frac{200 \mathrm{~W/m^2\cdot K} \times 400 \mathrm{~m^2} \times 60^{\circ} \mathrm{C}}{80,000 \mathrm{~W/K}} + 20^{\circ} \mathrm{C}$$ $$T_{c,out} = \frac{4800000 \mathrm{~W}}{80000 \mathrm{~W/K}} + 20^{\circ} \mathrm{C}$$ $$T_{c,out} = 60^{\circ} \mathrm{C} + 20^{\circ} \mathrm{C}$$
03

Conclusion

The exit temperature of the cold fluid is: $$T_{c,out} = 80^{\circ} \mathrm{C}$$

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Most popular questions from this chapter

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.

Can the temperature of the cold fluid rise above the inlet temperature of the hot fluid at any location in a heat exchanger? Explain.

How is the NTU of a heat exchanger defined? What does it represent? Is a heat exchanger with a very large NTU (say, 10 ) necessarily a good one to buy?

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)\( in the tubes from \)20^{\circ} \mathrm{C}\( to \)70^{\circ} \mathrm{C}\( at a rate of \)4.5 \mathrm{~kg} / \mathrm{s}$. Heat is supplied by hot oil \(\left(c_{p}=2300 \mathrm{~J} / \mathrm{kg} \cdot \mathrm{K}\right)\) that enters the shell side at \(170^{\circ} \mathrm{C}\) at a rate of $10 \mathrm{~kg} / \mathrm{s}$. For a tube-side overall heat transfer coefficient of \(350 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\), determine the heat transfer surface area on the tube side. Answer: \(25.7 \mathrm{~m}^{2}\)

Consider a heat exchanger that has an NTU of \(0.1\). Someone proposes to triple the size of the heat exchanger and thus triple the NTU to \(0.3\) in order to increase the effectiveness of the heat exchanger and thus save energy. Would you support this proposal?

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