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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.

Short Answer

Expert verified
a) To calculate the heat transfer effectiveness, first determine the maximum possible heat transfer rate using $$Q_{max} = \min{\left(\dot{m}_c c_{p_c}, \dot{m}_k c_{p_k}\right)} (T_{h,i} - T_{c,i})$$ Then, divide the actual heat transfer rate (Q) by the maximum possible heat transfer rate (Q_max): $$\epsilon = \frac{Q}{Q_{max}}$$ b) To find the outlet temperature of the oil, use the heat transfer rate (Q) and the formula $$T_{h,o} = T_{h,i} - \frac{Q}{\dot{m}_k c_{p_k}}$$

Step by step solution

01

Calculate the heat transfer rate

To calculate the heat transfer rate, we will use the formula $$Q = UA \Delta T_{lm} $$ where Q is the heat transfer rate, U is the overall heat transfer coefficient, A is the total surface area, and \(\Delta T_{lm}\) is the Log Mean Temperature Difference. The Log Mean Temperature Difference is calculated by $$ \Delta T_{lm} = \frac{T_{h,i} - T_{h,o}}{\ln{\frac{T_{h,i} - T_{c,i}}{T_{h,o} - T_{c,i}}}} $$ We know the inlet temperatures (\(T_{h,i}\) and \(T_{c,i}\)) and all other given values, but we need to find the outlet temperature of the oil \((T_{h,o})\) first to calculate the LMTD.
02

Calculate the heat transfer rate using the energy balance

To find the outlet temperature of the oil, we can use the energy balance, which states that the heat gained by the cold fluid is equal to the heat lost by the hot fluid, expressed as $$Q = \dot{m}_c c_{p_c} (T_{c,o} - T_{c,i}) = \dot{m}_k c_{p_k} (T_{h,i} - T_{h,o}) $$ where \(\dot{m}_c\) and \(\dot{m}_k\) are the mass flow rates of the cold and hot fluids, \(c_{p_c}\) and \(c_{p_k}\) are the specific heat capacities of the cold and hot fluids, and \(T_{c,o}\) is the outlet temperature of the cold fluid. We can express the outlet temperature of the cold fluid in terms of the heat transfer rate: $$T_{c,o} = T_{c,i} + \frac{Q}{\dot{m}_c c_{p_c}}$$ Substituting this expression into the energy balance equation, we get $$Q = \dot{m}_k c_{p_k} (T_{h,i} - T_{h,o}) + \frac{Q^2}{\dot{m}_c c_{p_c} \dot{m}_k c_{p_k}}$$ This is a quadratic equation in Q, which can be solved to find the heat transfer rate.
03

Find the outlet temperature of the oil

After solving the quadratic equation in step 2, we can find the outlet temperature of the oil using the formula $$T_{h,o} = T_{h,i} - \frac{Q}{\dot{m}_k c_{p_k}}$$
04

Calculate the heat transfer effectiveness

The heat transfer effectiveness is the ratio of the actual heat transfer rate to the maximum possible heat transfer rate, expressed as $$\epsilon = \frac{Q}{Q_{max}}$$ The maximum possible heat transfer rate can be found using the formula $$Q_{max} = \min{\left(\dot{m}_c c_{p_c}, \dot{m}_k c_{p_k}\right)} (T_{h,i} - T_{c,i})$$ Finally, we can find the heat transfer effectiveness by dividing the actual heat transfer rate by the maximum possible heat transfer rate. Now, we have the heat transfer effectiveness and the outlet temperature of the oil, which are the answers to \((a)\) and \((b)\), respectively.

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Most popular questions from this chapter

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?

The cardiovascular countercurrent heat exchanger mechanism is to warm venous blood from \(28^{\circ} \mathrm{C}\) to \(35^{\circ} \mathrm{C}\) at a mass flow rate of \(2 \mathrm{~g} / \mathrm{s}\). The artery inflow temperature is \(37^{\circ} \mathrm{C}\) at a mass flow rate of \(5 \mathrm{~g} / \mathrm{s}\). The average diameter of the vein is \(5 \mathrm{~cm}\) and the overall heat transfer coefficient is \(125 \mathrm{~W} / \mathrm{m}^{2}\). K. Determine the overall blood vessel length needed to warm the venous blood to $35^{\circ} \mathrm{C}$ if the specific heat of both arterial and venous blood is constant and equal to \(3475 \mathrm{~J} / \mathrm{kg} \cdot \mathrm{K}\).

Oil in an engine is being cooled by air in a crossflow heat exchanger, where both fluids are unmixed. Oil $\left(c_{p l}=2047 \mathrm{~J} / \mathrm{kg} \cdot \mathrm{K}\right)\( flowing with a flow rate of \)0.026 \mathrm{~kg} / \mathrm{s}\( enters the tube side at \)75^{\circ} \mathrm{C}$, while air \(\left(c_{p c}=1007 \mathrm{~J} / \mathrm{kg} \cdot \mathrm{K}\right)\) enters the shell side 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 \(1 \mathrm{~m}^{2}\). If the correction factor is \(F=0.96\), determine the outlet temperatures of the oil and air.

In a textile manufacturing plant, the waste dyeing water $\left(c_{p}=4295 \mathrm{~J} / \mathrm{kg} \cdot \mathrm{K}\right)\( at \)80^{\circ} \mathrm{C}$ is to be used to preheat fresh water $\left(c_{p}=4180 \mathrm{~J} / \mathrm{kg} \cdot \mathrm{K}\right)\( at \)10^{\circ} \mathrm{C}$ at the same flow rate in a double-pipe counterflow heat exchanger. The heat transfer surface area of the heat exchanger is \(1.65 \mathrm{~m}^{2}\), and the overall heat transfer coefficient is $625 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\(. If the rate of heat transfer in the heat exchanger is \)35 \mathrm{~kW}$, determine the outlet temperature and the mass flow rate of each fluid stream.

The National Sanitation Foundation (NSF) standard for commercial warewashing equipment (ANSL/NSF 3) requires that the final rinse water temperature be between 82 and \(90^{\circ} \mathrm{C}\). A shell-and-tube heat exchanger is to heat \(0.5 \mathrm{~kg} / \mathrm{s}\) of water $\left(c_{p}=4200 \mathrm{~J} / \mathrm{kg} \cdot \mathrm{K}\right)\( from 48 to \)86^{\circ} \mathrm{C}$ by geothermal brine flowing through a single shell pass. The heated water is then fed into commercial warewashing equipment. The geothermal brine enters and exits the heat exchanger at 98 and \(90^{\circ} \mathrm{C}\), respectively. The water flows through four thin-walled tubes, each with a diameter of $25 \mathrm{~mm}$, with all four tubes making the same number of passes through the shell. The tube length per pass for each tube is \(5 \mathrm{~m}\). The corresponding convection heat transfer coefficients on the outer and inner tube surfaces are 1050 and $2700 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}$, respectively. The estimated fouling factor caused by the accumulation of deposit from the geothermal brine is $0.0002 \mathrm{~m}^{2} . \mathrm{K} / \mathrm{W}$. Determine the number of passes required for the tubes inside the shell to heat the water to \(86^{\circ} \mathrm{C}\), within the temperature range required by the ANIS/NSF 3 standard.

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