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A fuel oil is burned with air in a boiler furnace. The combustion produces \(813 \mathrm{kW}\) of thermal energy, of which \(65 \%\) is transferred as heat to boiler tubes that pass through the furnace. The combustion products pass from the furnace to a stack at \(550^{\circ} \mathrm{C}\). Water enters the boiler tubes as a liquid at \(30^{\circ} \mathrm{C}\) and leaves the tubes as saturated steam at 20 bar absolute. (a) Calculate the rate ( \(\mathrm{kg} / \mathrm{h}\) ) at which steam is produced. (b) Use the steam tables to estimate the volumetric flow rate of the steam produced. (c) Repeat the calculation of Part (b), only assume ideal-gas behavior instead of using the steam tables. Would you have more confidence in the estimate of Part (b) or Part (c)? Explain. (d) What happened to the \(35 \%\) of the thermal energy released by the combustion that did not go to produce the steam?

Short Answer

Expert verified
The steam is produced at a rate which can be calculated using the energy conversion calculations and steam tables. The volumetric flow rates of steam, estimated through steam tables and ideal-gas behavior, may show slight variations, with the steam table estimation being potentially more accurate. The remaining 35% of thermal energy not used in steam production escapes through the stack, causing inefficiency in the system.

Step by step solution

01

Calculation of Heat transferred to boiler tubes

Firstly, calculate the amount of thermal energy that is transferred as heat to the boiler tubes. It's given that this is 65% of the total thermal energy produced which is 813 kW. Use the formula: \[Q = \text{{percentage of heat transferred}} / 100 * \text{{total thermal energy produced}}\] where, Q is the heat energy transferred.
02

Calculate steam production rate

Now, use the first law of thermodynamics (energy conservation). The heat energy transferred to the water will be used to convert the water into steam. The heat energy required to convert unit mass of water at 30°C to saturated steam at 20 bar can be obtained using the steam table. This is termed the enthalpy of steam. Use this enthalpy to calculate the steam production rate: \[ \text{{Steam production rate}} = Q / \text{{enthalpy of steam}}\]
03

Calculate Volumetric flow rate

Use the steam tables to obtain the specific volume of saturated steam at 20 bar, then calculate the volumetric flow rate by multiplying the steam production rate by the specific volume of steam.
04

Calculate Volumetric flow rate (Ideal-gas behavior)

Assume ideal-gas behavior and use the ideal gas law to estimate the volumetric flow rate of the steam produced. The ideal gas law is \[PV = nRT\], where P is pressure, V is volume, n is number of moles, R is gas constant and T is temperature.
05

Analysis of Volumetric flow rate estimates

Compare the results of steps 3 and 4. Ideal gas laws tend to underestimate the volume, thus steam tables should be more accurate especially for near-saturated conditions.
06

Track Remaining Energy

Finally, the remaining 35% of the thermal energy that did not contribute to steam production is likely lost through heat transfer to the surroundings; this energy escapes through the stack, resulting in a less efficient system.

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Key Concepts

These are the key concepts you need to understand to accurately answer the question.

Steam Production
Steam production in boilers is a fundamental concept in thermodynamics and power generation. When fuel oil is burned in a boiler furnace, it generates thermal energy. This energy is then transferred to water flowing through the boiler's tubes, turning it into steam. By using the steam tables, we determine how much heat energy is required to convert water at a given pressure and temperature into steam. In the original exercise, the heat energy transferred to the water is calculated as 65% of the total thermal energy produced from burning, which in this case equals 813 kW.

The rate of steam production can then be found by dividing the transferred thermal energy by the enthalpy of the steam, which is derived from steam tables. The enthalpy of steam represents the total energy needed for this phase change. Thus, the steam production rate signifies how quickly steam is generated per hour under the given conditions. An accurate evaluation of this rate is key to operational efficiency in power plants and industrial settings.
Energy Conservation
Energy conservation is a principle rooted in the first law of thermodynamics. This law states that energy can neither be created nor destroyed, only transferred or changed from one form to another. In the context of steam production in a boiler, the energy released from fuel combustion is partly used to heat the water, converting it to steam. However, not all the energy is transferred efficiently. In the given exercise, 65% of the thermal energy is utilized for steam production, while the remaining 35% is lost.

This loss typically occurs due to several factors including:
  • Heat escaping through exhaust gases or the stack.
  • Ambient thermal radiation losses.
  • Inefficiencies in the boiler's design or insulation.

Understanding and minimizing these energy losses is crucial for improving the efficiency and cost-effectiveness of thermal systems. Optimization of energy utilization helps ensure a better return on energy investments and reduces waste.
Ideal Gas Law
The Ideal Gas Law is a fundamental equation in thermodynamics that relates the pressure, volume, temperature, and number of moles of a gas. It is expressed as: \[PV = nRT\]where:
  • \(P\) is the pressure.
  • \(V\) is the volume.
  • \(n\) is the number of moles.
  • \(R\) is the ideal gas constant.
  • \(T\) is the temperature in Kelvin.

In the exercise, this law is applied to estimate the volumetric flow rate of steam, assuming the steam behaves like an ideal gas. While the Ideal Gas Law is a good approximation for many gases, water vapor at high pressure and near the saturation point does not behave like an ideal gas. As a result, using the law in these conditions often underestimates the volume compared to calculations using the steam tables, which are more accurate for substances in non-ideal states.

Ultimately, for precise engineering calculations where accuracy is critical, it's recommended to rely on tools like steam tables or software simulations rather than the Ideal Gas Law alone.
Heat Transfer Efficiency
Heat transfer efficiency in boilers and steam systems is a critical aspect of thermodynamics. It refers to the proportion of thermal energy that successfully converts water into steam, within the confines of a boiler. In the example from the exercise, 65% of the thermal energy from combustion is effectively used for steam production, while 35% is lost.

Improving heat transfer efficiency entails minimizing these energy losses by:
  • Enhancing boiler insulation.
  • Optimizing heat exchanger surfaces.
  • Utilizing advanced combustion technologies to better mix fuel and air.

A thorough understanding of heat transfer mechanisms, such as conduction, convection, and radiation, is also essential. Energy efficiency translates to cost savings, reduced environmental impact, and higher system reliability. Systems that maximize heat capture and utilization not only meet operational demands more effectively but also set higher standards for energy consumption in industrial practices.

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Most popular questions from this chapter

Water is to be pumped from a lake to a ranger station on the side of a mountain (see figure). The length of pipe immersed in the lake is negligible compared to the length from the lake surface to the discharge point. The flow rate is to be \(95 \mathrm{gal} / \mathrm{min}\), and the flow channel is a standard 1-inch. Schedule 40 steel pipe (ID \(=1.049\) inch). A pump capable of delivering \(8 \mathrm{hp}\left(=\dot{W}_{\mathrm{s}}\right)\) is available. The friction loss \(\tilde{F}\left(\mathrm{ft} \cdot \mathrm{lb}_{\mathrm{f}} / \mathrm{lb}_{\mathrm{m}}\right)\) equals \(0.041 L,\) where \(L(\mathrm{ft})\) is the length of the pipe. (a) Calculate the maximum elevation, \(z\), of the ranger station above the lake if the pipe rises at an angle of \(30^{\circ}\) (b) Suppose the pipe inlet is immersed to a significantly greater depth below the surface of the lake, but it discharges at the elevation calculated in Part (a). The pressure at the pipe inlet would be greater than it was at the original immersion depth, which means that \(\Delta P\) from inlet to outlet would be greater, which in turn suggests that a smaller pump would be sufficient to move the water to the same elevation. In fact, however, a larger pump would be needed. Explain (i) why the pressure at the inlet would be greater than in Part (a), and (ii) why a larger pump would be needed.

Arsenic contamination of aquifers is a major health problem in much of the world and is particularly severe in Bangladesh. One method of removing the arsenic is to pump water from an aquifer to the surface and through a bed packed with granular material containing iron oxide, which binds the arsenic. The purified water is then either used or allowed to seep back through the ground into the aquifer. In an installation of the type just described, a pump draws 69.1 gallons per minute of contaminated water from an aquifer through a 3 -inch ID pipe and then discharges the water through a 2-inch ID pipe to an open overhead tank filled with granular material. The water leaves the end of the discharge line 80 feet above the water in the aquifer. The friction losses in the piping system are \(10 \mathrm{ft} \cdot \mathrm{lb}_{\mathrm{f}} / \mathrm{lb}_{\mathrm{m}}\) (a) If the pump is \(70 \%\) efficient (i.e., \(30 \%\) of the electrical energy delivered to the pump is not used in pumping the water), what is the required pump horsepower? (b) Even if we assume that the iron oxide binds \(100 \%\) of the arsenic, what other factors limit the effectiveness of this operation?

Saturated steam at \(100^{\circ} \mathrm{C}\) is heated to \(350^{\circ} \mathrm{C}\). Use the steam tables to determine (a) the required heat input (J/s) if a continuous stream flowing at \(100 \mathrm{kg} / \mathrm{s}\) undergoes the process at constant pressure and (b) the required heat input (J) if \(100 \mathrm{kg}\) undergoes the process in a constant-volume container. What is the physical significance of the difference between the numerical values of these two quantities?

Liquid ethanol is pumped from a large storage tank through a 1 -inch ID pipe at a rate of 3.00 gal/min. (a) At what rate in (i) \(\mathrm{ft} \cdot \mathrm{lb}_{\mathrm{f}} / \mathrm{s}\) and (ii) hp is kinetic energy being transported by the ethanol in the pipe? (b) The electrical power input to the pump transporting the ethanol must be greater than the amount you calculated in Part (a). What would you guess becomes of the additional energy? (There are several possible answers.)

A steam trap is a device to purge steam condensate from a system without venting uncondensed steam. In one of the crudest trap types, the condensate collects and raises a float attached to a drain plug. When the float reaches a certain level, it "pulls the plug," opening the drain valve and allowing the liquid to discharge. The float then drops down to its original position and the valve closes, preventing uncondensed steam from escaping. (a) Suppose saturated steam at 25 bar is used to heat \(100 \mathrm{kg} / \mathrm{min}\) of an oil from \(135^{\circ} \mathrm{C}\) to \(185^{\circ} \mathrm{C}\). Heat must be transferred to the oil at a rate of \(1.00 \times 10^{4} \mathrm{kJ} / \mathrm{min}\) to accomplish this task. The steam condenses on the exterior of a bundle of tubes through which the oil is flowing. Condensate collects in the bottom of the exchanger and exits through a steam trap set to discharge when 1200 g of liquid is collected. How often does the trap discharge? (b) Especially when periodic maintenance checks are not performed, steam traps often fail to close completely and so leak steam continuously. Suppose a process plant contains 1000 leaking traps (not an unrealistic supposition for some plants) operating at the condition of Part (a), and that on the average 10\% additional steam must be fed to the condensers to compensate for the uncondensed steam venting through the leaks. Further suppose that the cost of generating the additional steam is \$7.50 per million Btu, where the denominator refers to the enthalpy of the leaking steam relative to liquid water at \(20^{\circ} \mathrm{C}\). Estimate the yearly cost of the leaks based on \(24 \mathrm{h} /\) day, 360 day/yr operation.

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