Hot water at an average temperature of \(53^{\circ} \mathrm{C}\) and an average velocity of \(0.4 \mathrm{~m} / \mathrm{s}\) is flowing through a \(5-\mathrm{m}\) section of a thin-walled hot-water pipe that has an outer diameter of \(2.5 \mathrm{~cm}\). The pipe passes through the center of a \(14-\mathrm{cm}\)-thick wall filled with fiberglass insulation \((k=0.035 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K})\). If the surfaces of the wall are at \(18^{\circ} \mathrm{C}\), determine \((a)\) the rate of heat transfer from the pipe to the air in the rooms and \((b)\) the temperature drop of the hot water as it flows through this 5 -m-long section of the wall. Answers: \(19.6 \mathrm{~W}, 0.024^{\circ} \mathrm{C}\)

Short Answer

Expert verified
The rate of heat transfer from the hot water pipe to the air in the room is approximately 19.6 W, and the temperature drop of the hot water as it flows through the 5m-long section of the wall is approximately 0.024°C.

Step by step solution

01

Calculate the surface area of the pipe

To find the surface area of the pipe, use the formula for the surface area of a cylinder: \(A=2\pi r L\), where \(r\) is the outer radius of the pipe, and \(L\) is the length of the pipe. Here, \(r = \frac{2.5}{2} \times 10^{-2} \mathrm{~m}\) and \(L = 5 \mathrm{~m}\). \(A = 2 \pi \left(\frac{2.5}{2} \times 10^{-2}\right) (5)\) Calculate the surface area of the pipe.
02

Calculating the heat transfer rate through insulation

Using the formula for heat transfer through a cylindrical wall: \(q=\frac{2\pi k L(T_{1}-T_{2})}{\ln{\frac{r_{2}}{r_{1}}}}\), where \(k=0.035 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}\) is the thermal conductivity of the insulation, \(L=5\mathrm{~m}\) is the length of the section, \((T_{1}-T_{2})=(53-18)=35 ^{\circ}\mathrm{C}\) is the temperature difference between the pipe's surface and the air, \(r_{1}=\frac{2.5}{2}\times10^{-2}\) m is the outer radius and \(r_{2}=(\frac{2.5}{2} + 14) \times 10^{-2}\) m is the outer radius plus wall thickness. Calculate the heat transfer rate using the formula.
03

Find the temperature drop of the hot water

As we already found the heat transfer rate \(q\), the next step is to find the temperature drop of the hot water using the energy balance equation: \(\Delta T = \frac{q}{\dot{m}C_p}\), where \(\Delta T\) is the temperature drop, \(\dot{m}\) is the mass flow rate of the hot water, and \(C_p\) is the specific heat capacity of water. First, we need to find the volumetric flow rate: \(V = A_v \times v \), where \(A_v = \pi(r_1)^2\) is the cross-sectional area of the pipe, and \(v=0.4\mathrm{~m}/\mathrm{s}\) is the flow velocity. \(\dot{m}= \rho V\), where \(\rho\) is the density of water, approximately \(1000 \mathrm{~kg}/\mathrm{m}^{3}\). Finally, for water, we have \(C_p \approx 4180 \mathrm{~J}/\mathrm{kg} \cdot \mathrm{K}\). Calculate \(\Delta T\) by plugging in the values. Once you've followed these steps, you'll find that the rate of heat transfer from the pipe to the air in the room is approximately \(19.6\mathrm{~W}\), and the temperature drop of the hot water as it flows through the 5m-long section of the wall is approximately \(0.024^{\circ}\mathrm{C}\).

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Most popular questions from this chapter

Heat is generated steadily in a 3-cm-diameter spherical ball. The ball is exposed to ambient air at \(26^{\circ} \mathrm{C}\) with a heat transfer coefficient of \(7.5 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\). The ball is to be covered with a material of thermal conductivity \(0.15 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}\). The thickness of the covering material that will maximize heat generation within the ball while maintaining ball surface temperature constant is (a) \(0.5 \mathrm{~cm}\) (b) \(1.0 \mathrm{~cm}\) (c) \(1.5 \mathrm{~cm}\) (d) \(2.0 \mathrm{~cm}\) (e) \(2.5 \mathrm{~cm}\)

Circular cooling fins of diameter \(D=1 \mathrm{~mm}\) and length \(L=25.4 \mathrm{~mm}\), made of copper \((k=400 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K})\), are used to enhance heat transfer from a surface that is maintained at temperature \(T_{s 1}=132^{\circ} \mathrm{C}\). Each rod has one end attached to this surface \((x=0)\), while the opposite end \((x=L)\) is joined to a second surface, which is maintained at \(T_{s 2}=0^{\circ} \mathrm{C}\). The air flowing between the surfaces and the rods is also at \(T_{\infty}=0^{\circ} \mathrm{C}\), and the convection coefficient is \(h=100 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\). (a) Express the function \(\theta(x)=T(x)-T_{\infty}\) along a fin, and calculate the temperature at \(x=L / 2\). (b) Determine the rate of heat transferred from the hot surface through each fin and the fin effectiveness. Is the use of fins justified? Why? (c) What is the total rate of heat transfer from a \(10-\mathrm{cm}\) by 10 -cm section of the wall, which has 625 uniformly distributed fins? Assume the same convection coefficient for the fin and for the unfinned wall surface.

Consider two finned surfaces that are identical except that the fins on the first surface are formed by casting or extrusion, whereas they are attached to the second surface afterwards by welding or tight fitting. For which case do you think the fins will provide greater enhancement in heat transfer? Explain.

Steam exiting the turbine of a steam power plant at \(100^{\circ} \mathrm{F}\) is to be condensed in a large condenser by cooling water flowing through copper pipes \(\left(k=223 \mathrm{Btu} / \mathrm{h} \cdot \mathrm{ft} \cdot{ }^{\circ} \mathrm{F}\right)\) of inner diameter \(0.4\) in and outer diameter \(0.6\) in at anerage temperature of \(70^{\circ} \mathrm{F}\). The heat of vaporization of water at \(100^{\circ} \mathrm{F}\) is \(1037 \mathrm{Btu} / \mathrm{lbm}\). The heat transfer coefficients are \(1500 \mathrm{Btu} / \mathrm{h} \cdot \mathrm{ft}^{2} \cdot{ }^{\circ} \mathrm{F}\) on the steam side and \(35 \mathrm{Btu} / \mathrm{h} \cdot \mathrm{ft}^{2} \cdot{ }^{\circ} \mathrm{F}\) on the water side. Determine the length of the tube required to condense steam at a rate of \(120 \mathrm{lbm} / \mathrm{h}\). Answer: \(1150 \mathrm{ft}\)

Consider a 25-m-long thick-walled concrete duct \((k=\) \(0.75 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K})\) of square cross section. The outer dimensions of the duct are \(20 \mathrm{~cm} \times 20 \mathrm{~cm}\), and the thickness of the duct wall is \(2 \mathrm{~cm}\). If the inner and outer surfaces of the duct are at \(100^{\circ} \mathrm{C}\) and \(30^{\circ} \mathrm{C}\), respectively, determine the rate of heat transfer through the walls of the duct. Answer: \(47.1 \mathrm{~kW}\)

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