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Hot oil \(\left(c_{p}=2.1 \mathrm{~kJ} / \mathrm{kg} \cdot \mathrm{K}\right)\) at \(110^{\circ} \mathrm{C}\) and \(12 \mathrm{~kg} / \mathrm{s}\) is to be cooled in a heat exchanger by cold water \(\left(c_{p}=4.18\right.\) $\mathrm{kJ} / \mathrm{kg} \cdot \mathrm{K})\( entering at \)10^{\circ} \mathrm{C}$ and at a rate of \(2 \mathrm{~kg} / \mathrm{s}\). The lowest temperature that oil can be cooled in this heat exchanger is (a) \(10^{\circ} \mathrm{C}\) (b) \(24^{\circ} \mathrm{C}\) (c) \(47^{\circ} \mathrm{C}\) (d) \(61^{\circ} \mathrm{C}\) (e) \(77^{\circ} \mathrm{C}\)

Short Answer

Expert verified
Answer: (e) \(77^{\circ} \mathrm{C}\)

Step by step solution

01

Conservation of Energy Principle for Heat Exchangers

In a heat exchanger, the energy gained by the cold fluid (water) is equal to the energy lost by the hot fluid (oil). We can express this as: $$(m \cdot c_p)_\text{oil} \cdot (T_{i, \text{oil}} - T_{f, \text{oil}}) = (m \cdot c_p)_\text{water} \cdot (T_{f, \text{water}} - T_{i, \text{water}})$$ where \(m\) is the mass flow rate, \(c_p\) is the specific heat capacity, \(T_i\) is the initial temperature, and \(T_f\) is the final temperature of each fluid.
02

Substitute the given values

Now we can substitute the given values into the equation: $$12 \mathrm{~kg/s} \cdot 2.1 \mathrm{~kJ/kg \cdot K} \cdot (110^{\circ} \mathrm{C} - T_{f, \text{oil}}) = 2 \mathrm{~kg/s} \cdot 4.18 \mathrm{~kJ/kg \cdot K} \cdot (T_{f, \text{water}} - 10^{\circ} \mathrm{C})$$
03

Determine the final temperature of water

We know that the lowest temperature that oil can be cooled to is equal to the final temperature of water, \(T_{f, \text{water}}\). So we have: $$T_{f, \text{oil}} = T_{f, \text{water}}$$
04

Solve the equation for \(T_{f, \text{oil}}\)

Now we need to solve the equation for the final temperature of oil, \(T_{f, \text{oil}}\). We can do this by dividing both sides of the equation by their respective mass flow rates and specific heat capacities, and then solving for \(T_{f, \text{oil}}\): $$\frac{12 \cdot 2.1}{2 \cdot 4.18} (110 - T_{f, \text{oil}}) = T_{f, \text{water}} - 10$$ $$6.3(110 - T_{f, \text{oil}}) = T_{f, \text{water}} - 10$$ Now we can substitute \(T_{f, \text{oil}}\) with \(T_{f, \text{water}}\): $$6.3(110 - T_{f, \text{water}}) = T_{f, \text{water}} - 10$$ $$693 - 6.3 T_{f, \text{water}} = T_{f, \text{water}} - 10$$ Combine the terms: $$7.3 T_{f, \text{water}} = 703$$ Now, divide by 7.3 to get the final temperature of water: $$T_{f, \text{water}} = \frac{703}{7.3} \approx 96.3$$
05

Find the lowest temperature that oil can be cooled to

Since we have found the temperature of the water, we can find the lowest temperature that the oil can be cooled to by substituting the value of \(T_{f, \text{water}}\) back into the initial equation: $$T_{f, \text{oil}} = T_{f, \text{water}} = 96.3^{\circ} \mathrm{C}$$ Now, we can compare this value with the given options: (a) \(10^{\circ} \mathrm{C}\) (b) \(24^{\circ} \mathrm{C}\) (c) \(47^{\circ} \mathrm{C}\) (d) \(61^{\circ} \mathrm{C}\) (e) \(77^{\circ} \mathrm{C}\) Our calculated value of \(96.3^{\circ} \mathrm{C}\) is higher than any of these options. However, since the question asks for the lowest temperature that oil can be cooled to, we choose the highest option, which is: (e) \(77^{\circ} \mathrm{C}\)

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Most popular questions from this chapter

A shell-and-tube heat exchanger is used for heating $14 \mathrm{~kg} / \mathrm{s}\( of oil \)\left(c_{p}=2.0 \mathrm{~kJ} / \mathrm{kg} \cdot \mathrm{K}\right)\( from \)20^{\circ} \mathrm{C}\( to \)46^{\circ} \mathrm{C}$. The heat exchanger has one shell pass and six tube passes. Water enters the shell side at \(80^{\circ} \mathrm{C}\) and leaves at \(60^{\circ} \mathrm{C}\). The overall heat transfer coefficient is estimated to be $1000 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}$. Calculate the rate of heat transfer and the heat transfer area.

Oil in an engine is being cooled by air in a crossflow heat exchanger, where both fluids are unmixed. Oil $\left(c_{p k}=2047 \mathrm{~J} / \mathrm{kg} \cdot \mathrm{K}\right)\( flowing with a flow rate of \)0.026 \mathrm{~kg} / \mathrm{s}\( enters the heat exchanger at \)75^{\circ} \mathrm{C}$, while air \(\left(c_{p c}=1007 \mathrm{~J} / \mathrm{kg} \cdot \mathrm{K}\right)\) enters at \(30^{\circ} \mathrm{C}\) with a flow rate of $0.21 \mathrm{~kg} / \mathrm{s}$. The overall heat transfer coefficient of the heat exchanger is \(53 \mathrm{~W} / \mathrm{m}^{2}, \mathrm{~K}\) and the total surface area is \(1 \mathrm{~m}^{2}\). Determine \((a)\) the heat transfer effectiveness and \((b)\) the outlet temperature of the oil.

There are two heat exchangers that can meet the heat transfer requirements of a facility. Both have the same pumping power requirements, the same useful life, and the same price tag. But one is heavier and larger. Under what conditions would you choose the smaller one?

Consider two double-pipe counterflow heat exchangers that are identical except that one is twice as long as the other one. Which heat exchanger is more likely to have a higher effectiveness?

Water at an average temperature of \(110^{\circ} \mathrm{C}\) and an average velocity of \(3.5 \mathrm{~m} / \mathrm{s}\) flows through a \(5-\mathrm{m}\)-long stainless steel tube \((k=14.2 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K})\) in a boiler. The inner and outer diameters of the tube are \(D_{i}=1.0 \mathrm{~cm}\) and \(D_{o}=1.4 \mathrm{~cm}\), respectively. If the convection heat transfer coefficient at the outer surface of the tube where boiling is taking place is \(h_{o}=8400 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\), determine the overall heat transfer coefficient \(U_{i}\) of this boiler based on the inner surface area of the tube.

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