In a cogeneration plant, combustion gases at 1 atm and \(800 \mathrm{~K}\) are used to preheat water by passing them through 6-m-long, 10-cm-diameter tubes. The inner surface of the tube is black, and the partial pressures of \(\mathrm{CO}_{2}\) and \(\mathrm{H}_{2} \mathrm{O}\) in combustion gases are \(0.12\) atm and \(0.18\) atm, respectively. If the tube temperature is \(500 \mathrm{~K}\), determine the rate of radiation heat transfer from the gases to the tube.

Short Answer

Expert verified
Answer: The rate of radiation heat transfer from the combustion gases to the tube, denoted by \(q\), can be calculated by following these steps: 1. Calculate the emissivity of the combustion gases (\(ε_{gas}\)) using Hottel's correlation. 2. Calculate the heat transfer coefficient for radiation (\(h_R\)) using the formula: \(h_R = ε_{gas} \cdot σ \cdot (T_{gas}^4 - T_{tube}^4) / (T_{gas} - T_{tube})\). 3. Determine the heat transfer rate (\(q\)) using the formula: \(q = h_R \cdot A \cdot (T_{gas} - T_{tube})\), where \(A\) represents the area of the tubes, calculated as \(A = πDL\). Once all the necessary values are calculated and substituted into the equation, the value of \(q\) will represent the rate of radiation heat transfer from the combustion gases to the tube.

Step by step solution

01

Calculate the emissivity of the combustion gases.

The emissivity of the combustion gases can be estimated using the Hottel's correlation: \(ε_{gas} = ε_{\mathrm{CO}_{2}} + ε_{\mathrm{H}_{2}\mathrm{O}} - \epsilon_{\mathrm{CO}_{2}}ε_{\mathrm{H}_{2}\mathrm{O}}\) where: \(ε_{\mathrm{CO}_{2}} = 1 - exp\left[-1.22 \cdot 10^{3} \cdot P_{\mathrm{CO}_{2}}x_{\mathrm{CO}_{2}}L\right]\) \(ε_{\mathrm{H}_{2}\mathrm{O}} = 1 - exp\left[-1.73 \cdot 10^{3} \cdot P_{\mathrm{H}_{2}\mathrm{O}}x_{\mathrm{H}_{2}\mathrm{O}}L\right]\) Here, \(P_{\mathrm{CO}_{2}}\) and \(P_{\mathrm{H}_{2}\mathrm{O}}\) denote the partial pressures of \(\mathrm{CO}_{2}\) and \(\mathrm{H}_{2}\mathrm{O}\) in the combustion gases, respectively. The value of \(L\) represents the length of the tubes. The values are given by: \(P_{\mathrm{CO}_{2}} = 0.12 \,\text{atm}\) \(P_{\mathrm{H}_{2}\mathrm{O}} = 0.18\, \text{atm}\) \(L = 6\,\text{m}\) We can calculate the emissivity of the combustion gases as follows: \(ε_{\mathrm{CO}_{2}} = 1 - exp[-1.22 \cdot 10^{3} \times 0.12 \times 6]\) \(ε_{\mathrm{H}_{2}\mathrm{O}} = 1 - exp[-1.73 \cdot 10^{3} \times 0.18 \times 6]\) \(ε_{gas} = ε_{\mathrm{CO}_{2}} + ε_{\mathrm{H}_{2}\mathrm{O}} - \epsilon_{\mathrm{CO}_{2}}ε_{\mathrm{H}_{2}\mathrm{O}}\)
02

Calculate the heat transfer coefficient for radiation.

The heat transfer coefficient for radiation is given by: \(h_R = ε_{gas} \cdot σ \cdot (T_{gas}^4 - T_{tube}^4) / (T_{gas} - T_{tube})\) Here, \(σ\) denotes the Stefan-Boltzmann constant (\(5.67 \times 10^{-8} W/m^2K^4\)), and \(T_{gas}\) and \(T_{tube}\) are the temperatures of the combustion gases and tube, respectively. We have: \(T_{gas} = 800\,\text{K}\) \(T_{tube} = 500\,\text{K}\) Substituting the values, we get: \(h_R = ε_{gas} \cdot 5.67 \times 10^{-8} \cdot (800^4 - 500^4) / (800 - 500)\)
03

Determine the heat transfer rate.

The heat transfer rate can be calculated using the formula: \(q = h_R \cdot A \cdot (T_{gas} - T_{tube})\) First, calculate the area of the tubes, where \(A = πDL\), wherein \(D\) represents the diameter of the tubes. \(D = 0.10\,\text{m}\) \(L = 6\,\text{m}\) \(A = π \times 0.10 \times 6\,\text{m}^2\) Finally, calculate the heat transfer rate: \(q = h_R \cdot A \cdot (800 - 500)\) The calculated \(q\) value will represent the rate of radiation heat transfer from the combustion gases to the tube.

Unlock Step-by-Step Solutions & Ace Your Exams!

  • Full Textbook Solutions

    Get detailed explanations and key concepts

  • Unlimited Al creation

    Al flashcards, explanations, exams and more...

  • Ads-free access

    To over 500 millions flashcards

  • Money-back guarantee

    We refund you if you fail your exam.

Over 30 million students worldwide already upgrade their learning with Vaia!

One App. One Place for Learning.

All the tools & learning materials you need for study success - in one app.

Get started for free

Most popular questions from this chapter

Two square plates, with the sides \(a\) and \(b\) (and \(b>a\) ), are coaxial and parallel to each other, as shown in Fig. P13-132, and they are separated by a center-to-center distance of \(L\). The radiation view factor from the smaller to the larger plate, \(F_{a b}\), is given by $$ F_{a b}=\frac{1}{2 A}\left\\{\left[(B+A)^{2}+4\right]^{0.5}-\left[(B-A)^{2}+4\right]^{0.5}\right\\} $$ where, \(A=a / L\) and \(B=b / L\). (a) Calculate the view factors \(F_{a b}\) and \(F_{b a}\) for \(a=20 \mathrm{~cm}\), \(b=60 \mathrm{~cm}\), and \(L=40 \mathrm{~cm}\). (b) Calculate the net rate of radiation heat exchange between the two plates described above if \(T_{a}=800^{\circ} \mathrm{C}\), \(T_{b}=200^{\circ} \mathrm{C}, \varepsilon_{a}=0.8\), and \(\varepsilon_{b}=0.4\). (c) A large square plate (with the side \(c=2.0 \mathrm{~m}, \varepsilon_{c}=0.1\), and negligible thickness) is inserted symmetrically between the two plates such that it is parallel to and equidistant from them. For the data given above, calculate the temperature of this third plate when steady operating conditions are established.

A thermocouple shielded by aluminum foil of emissivity \(0.15\) is used to measure the temperature of hot gases flowing in a duct whose walls are maintained at \(T_{w}=380 \mathrm{~K}\). The thermometer shows a temperature reading of \(T_{\text {th }}=530 \mathrm{~K}\). Assuming the emissivity of the thermocouple junction to be \(\varepsilon=0.7\) and the convection heat transfer coefficient to be \(h=120 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\), determine the actual temperature of the gas. What would the thermometer reading be if no radiation shield was used?

An average person produces \(0.50 \mathrm{lbm}\) of moisture while taking a shower and \(0.12 \mathrm{lbm}\) while bathing in a tub. Consider a family of four who shower once a day in a bathroom that is not ventilated. Taking the heat of vaporization of water to be \(1050 \mathrm{Btu} / \mathrm{lbm}\), determine the contribution of showers to the latent heat load of the air conditioner in summer per day.

Give examples of radiation effects that affect human comfort. 13-84 A thin aluminum sheet with an emissivity of \(0.15\) on both sides is placed between two very large parallel plates, which are maintained at uniform temperatures \(T_{1}=900 \mathrm{~K}\) and \(T_{2}=650 \mathrm{~K}\) and have emissivities \(\varepsilon_{1}=0.5\) and \(\varepsilon_{2}=0.8\), respectively. Determine the net rate of radiation heat transfer between the two plates per unit surface area of the plates and compare the result with that without the shield.Give examples of radiation effects that affect human comfort.

Consider an enclosure consisting of eight surfaces. How many view factors does this geometry involve? How many of these view factors can be determined by the application of the reciprocity and the summation rules?

See all solutions

Recommended explanations on Physics Textbooks

View all explanations

What do you think about this solution?

We value your feedback to improve our textbook solutions.

Study anywhere. Anytime. Across all devices.

Sign-up for free