/*! This file is auto-generated */ .wp-block-button__link{color:#fff;background-color:#32373c;border-radius:9999px;box-shadow:none;text-decoration:none;padding:calc(.667em + 2px) calc(1.333em + 2px);font-size:1.125em}.wp-block-file__button{background:#32373c;color:#fff;text-decoration:none} Problem 36 Steam produced in a boiler is fr... [FREE SOLUTION] | 91Ó°ÊÓ

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Steam produced in a boiler is frequently "wet"-that is, it is a mist composed of saturated water vapor and entrained liquid droplets. The quality of a wet steam is defined as the fraction of the mixture by mass that is vapor. A wet steam at a pressure of 5.0 bar with a quality of 0.85 is isothermally "dried" by evaporating the entrained liquid. The flow rate of the dried steam is \(52.5 \mathrm{m}^{3} / \mathrm{h}\). (a) Use the steam tables to determine the temperature at which this operation occurs, the specific enthalpies of the wet and dry steams, and the total mass flow rate of the process stream. (b) Calculate the heat input (kW) required for the evaporation process. (c) Suppose leaks developed in the feed pipe to the dryer and in the dryer exit pipe. Speculate on what you would see at each location.

Short Answer

Expert verified
The saturation temperature, 151.83°C. The specific enthalpy of the wet steam is 317.07 kJ/kg and of the dry steam is 2,113.8 kJ/kg. The heat input (kW) required for evaporation is calculated using the energy balance equation. As for leaks, there would be wet steam at the feed pipe and dry steam at the dryer exit pipe.\n

Step by step solution

01

Determine the temperature

Consult the steam tables for properties of saturated steam at 5 bar pressure. The saturation temperature is 151.83°C.
02

Calculate Specific Enthalpies

Using steam tables, the specific enthalpy of saturated vapor, \(h_{fg}\), and specific enthalpies of wet steam \(h_w\) and dry steam \(h_d\) can be computed. \(h_{fg}(5\, \text{bar}) = 2,113.8 \, \text{kJ/kg}\), \(h_w = (1-0.85) \times h_{fg} = 0.15 \times 2,113.8 = 317.07 \, \text{kJ/kg}\), and \(h_d = h_{fg} = 2,113.8 \, \text{kJ/kg}\)
03

Compute the Mass Flow Rate and Energy Input

The mass flow rate of steam can be obtained from the volume flow rate and the specific volume of steam (from steam tables). After calculating the mass flow rate, the energy required is calculated using the energy balance equation: \(Q = \dot{m}(h_d - h_w)\), where \(Q\) represents the heat input, and \(\dot{m}\) is the mass flow rate.
04

Analyze the Impact of Leaks

If leaks developed in the feed pipe to the dryer and in the dryer exit pipe, at the feed pipe, wet steam (containing water droplets) would be observed while at the dryer exit pipe, one may observe dry steam. The leak at the dryer would also reduce the efficiency of the drying process.

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Key Concepts

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

Steam Quality
The quality of steam is an important aspect in thermodynamics, especially in applications involving heat engines and HVAC systems.
It refers to the proportion of steam in a wet steam mixture, given as a ratio between 0 and 1. A quality of 0 indicates pure saturated liquid, while a quality of 1 suggests pure saturated vapor.
For a wet steam with a quality of 0.85, this means 85% of the mixture is in the form of vapor, and the remaining 15% is liquid. Understanding steam quality helps in correctly analyzing energy requirements and efficiency of heat transfer processes.
This is crucial in systems where precise control of thermal energy is needed, such as power generation and food processing.
Enthalpy Calculation
Enthalpy is a measure of total energy within a system, including internal energy and pressure-volume work. When dealing with steam, specific enthalpy is a key factor to consider.
In calculations, specific enthalpy is often derived from steam tables, which list values for both the liquid and vapor phases.
For wet steam, the specific enthalpy can be calculated using a combination of the enthalpies of the liquid and vapor states depending on its quality. The formula often used combines the saturated liquid enthalpy and the enthalpy of vaporization, defined as:
  • h_w = (1-x) imes h_{f} + x imes h_{fg}
  • h_d = h_{fg}
where:
  • x is the steam quality
  • h_{f} is the enthalpy of the liquid state
  • h_{fg} is the enthalpy change from liquid to vapor
Proper enthalpy calculation is essential for determining the energy input/output in thermal systems.
Heat Transfer
Heat transfer is a fundamental concept in thermodynamics and engineering.
It involves the transfer of thermal energy from one system or material to another. In our example, it specifically refers to the energy required to convert entrained liquid into vapor.
The heat input needed for this process is calculated using an energy balance equation:
  • Q = \(\dot{m}(h_d - h_w)\)
where:
  • Q is the heat input,
  • \(\dot{m}\) is the mass flow rate,
  • h_d is the enthalpy of dry steam,
  • h_w is the enthalpy of wet steam.
Understanding and calculating the heat required for phase changes helps maintain system efficiency and predict operational costs.
Saturated Steam
Saturated steam is a term used to describe steam that is in equilibrium with water at a certain pressure and temperature.
In the steam tables, saturated steam denotes the
  • temperature,
  • specific enthalpy,
  • and specific volume
for water boiling at a particular pressure.
Understanding saturated steam is vital in thermodynamic processes because it represents the conditions under which phase change occurs.
This is essential for accurately determining the operating conditions needed for different applications, like turbines and heat exchangers.
Mass Flow Rate Calculation
Mass flow rate is an essential component in thermodynamic and fluid mechanics calculations. It represents the amount of mass passing through a point per unit of time.
In thermal systems, mass flow rate is crucial for understanding how much energy is being transferred in the form of thermal energy or work.
It is calculated from the specific volume of steam and its flow rate as given by:
  • \( \dot{m} = \dfrac{V}{v} \)
where:
  • V is the volumetric flow rate
  • v is the specific volume of steam.
These calculations are crucial for designing and analyzing the efficiency and capacity of systems that utilize steam as a working fluid, such as power plants and steam engines.

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Most popular questions from this chapter

Superheated steam at 40 bar absolute and \(500^{\circ} \mathrm{C}\) flows at a rate of \(250 \mathrm{kg} / \mathrm{min}\) to an adiabatic turbine, where it expands to 5 bar. The turbine develops \(1500 \mathrm{kW}\). From the turbine the steam flows to a heater, where it is reheated isobarically to its initial temperature. Neglect kinetic energy changes. (a) Write an energy balance on the turbine and use it to determine the outlet stream temperature. (b) Write an energy balance on the heater and use it to determine the required input (kW) to the steam. (c) Verify that an overall energy balance on the two-unit process is satisfied. (d) Suppose the turbine inlet and outlet pipes both have diameters of 0.5 meter. Show that it is reasonable to neglect the change in kinetic energy for this unit.

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?

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.

A turbine discharges \(200 \mathrm{kg} / \mathrm{h}\) of saturated steam at \(10.0 \mathrm{bar}\) absolute. It is desired to generate steam at \(250^{\circ} \mathrm{C}\) and 10.0 bar by mixing the turbine discharge with a second stream of superheated steam of \(300^{\circ} \mathrm{C}\) and \(10.0 \mathrm{bar}\) (a) If \(300 \mathrm{kg} / \mathrm{h}\) of the product steam is to be generated, how much heat must be added to the mixer? (b) If instead the mixing is carried out adiabatically, at what rate is the product steam generated?

A 200.0 -liter water tank can withstand pressures up to 20.0 bar absolute before rupturing. At a particular time the tank contains \(165.0 \mathrm{kg}\) of liquid water, the fill and exit valves are closed, and the absolute pressure in the vapor head space above the liquid (which may be assumed to contain only water vapor) is 3.0 bar. A plant technician turns on the tank heater, intending to raise the water temperature to \(155^{\circ} \mathrm{C},\) but is called away and forgets to return and shut off the heater. Let \(t_{1}\) be the instant the heater is turned on and \(t_{2}\) the moment before the tank ruptures. Use the steam tables for the following calculations. (a) Determine the water temperature, the liquid and head-space volumes (L), and the mass of water vapor in the head space (kg) at time \(t_{1}\) (b) Determine the water temperature, the liquid and head-space volumes (L), and the mass of water vapor (g) that evaporates between \(t_{1}\) and \(t_{2}\). (Hint: Make use of the fact that the total mass of water in the tank and the total tank volume both remain constant between \(t_{1}\) and \(t_{2}\).) (c) Calculate the amount of heat (kJ) transferred to the tank contents between \(t_{1}\) and \(t_{2}\). Give two reasons why the actual heat input to the tank must have been greater than the calculated value.

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