/*! 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 38 A steam trap is a device to purg... [FREE SOLUTION] | 91Ó°ÊÓ

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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.

Short Answer

Expert verified
The steam trap discharges approximately 4.3 times per minute. The total cost due to the leaks for a year is approximately $4,397,800.

Step by step solution

01

Heat Transferred

Calculate the heat transferred by using the given rate \[1.00 \times 10^{4} \mathrm{kJ} / \mathrm{min}\]. The total heat transferred per minute will be \(Q = 1.00 \times 10^{4} \mathrm{kJ}\)
02

Heat Capacity

Now calculate the heat capacity per kg or the heat content represented by the mass of the condensate. From a standard steam table, at 25 bar, the heat of condensation or heat content of steam is 1940 kJ/kg. Thus, for 1200 g or 1.2 kg of steam, the heat content becomes \(GC = 1.2 \times 1940\) = 2328 kJ.
03

Frequency of Discharge

Use the heat transferred and heat capacity to find the frequency of discharge. To heat the oil at the given rate, the number of times condensate collected and discharged per minute can be found as \(n = Q/GC = 1.00 \times 10^{4}/2328 = 4.29\) discharges per min.
04

Additional Steam

Calculate the additional steam needed due to leaks. As given, 10% more steam is required to compensate for the steam lost through leaks. So the additional steam required per trap per minute is \(AS = 0.10 \times 1.2 = 0.12 kg/min\}
05

Total Leaked Steam

Calculate the total steam leaked per year. The total steam leaked per year for 1000 traps is \(TS = 1000 \times 0.12 \times 60 \times 24 \times 360 = 311040000 kg\).
06

Yearly Cost

Determine the yearly cost of the leaks. The extra cost due to the leaked steam can be calculated by \(EC = TS \times 1940 \times 0.0000075 = $4397800\)

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Key Concepts

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

Heat Transfer
Heat transfer is a key concept when discussing steam traps, as these devices play a crucial role in removing condensate without losing steam in a heating process. In our exercise, steam is used to heat oil from 135°C to 185°C at a heat transfer rate of \(1.00 \times 10^{4} \text{kJ/min}\). This means that the steam provides the necessary energy through condensation to elevate the oil’s temperature efficiently.
  • Heat transfer occurs when there is a difference in temperature, allowing energy to move from the steam (hotter) to the oil (cooler) via conduction through the tube walls.
  • The calculation of heat transferred, \(Q\), focuses on the amount of energy needed to change the temperature of a given mass of oil.
  • This process ensures that the system operates effectively, only allowing condensate to leave via the steam trap, thus maintaining steam within the system effectively.
Understanding this flow of energy is crucial for efficient system design and operation, especially in industrial processes where energy efficiency leads to cost savings.
Condensation Process
The condensation process is where steam transforms back into the liquid phase as it transfers its latent heat to the oil. In a sealed heat exchanger, the steam is exposed to the oil-cooled tube bundle, causing the steam to condense.
  • This phase change releases a significant amount of heat—known as the heat of condensation—which is used to heat the oil.
  • As steam condenses, it loses energy and collects as liquid condensate at the bottom of the exchanger.
  • The heat content per kilogram of the condensate is crucial in calculating system efficiency and discharge frequency of the steam trap. For steam at 25 bar, this value is 1940 kJ/kg.
Efficient condensation is vital to ensure the thermal energy is adequately transferred, preventing energy loss and making the process more economical.
Discharge Frequency Calculation
Calculating the discharge frequency of the steam trap is fundamental to ensuring that only condensate is removed, avoiding the loss of steam. This frequency dictates how often the float 'pulls the plug' to release the collected condensate.
  • The formula \(n = \frac{Q}{GC}\) helps determine this frequency, where \(Q\) is the heat transfer rate (\(1.00 \times 10^{4} \text{kJ/min}\)) and \(GC\) is the heat content of the condensate collected per cycle (2328 kJ for 1.2 kg).
  • So, the trap must discharge approximately 4.29 times per minute to balance the energy transfer and remove the excess condensate efficiently.
  • These calculations help in designing the system for optimal performance by ensuring that steam is neither wasted nor trapped, impacting overall plant efficiency.
This aspect is critical in the long-term maintenance and operational planning of systems employing steam traps.

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Most popular questions from this chapter

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.

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?

Prove that for an ideal gas, \(\hat{U}\) and \(\hat{H}\) are related as \(\hat{H}=\hat{U}+R T\), where \(R\) is the gas constant. Then: (a) Taking as given that the specific internal energy of an ideal gas is independent of the gas pressure, justify the claim that \(\Delta \hat{H}\) for a process in which an ideal gas goes from \(\left(T_{1}, P_{1}\right)\) to \(\left(T_{2}, P_{2}\right)\) equals \(\Delta \hat{H}\) for the same gas going from \(T_{1}\) to \(T_{2}\) at a constant pressure of \(P_{1}\) (b) Calculate \(\Delta H(\text { cal })\) for a process in which the temperature of 2.5 mol of an ideal gas is raised by \(50^{\circ} \mathrm{C},\) resulting in a specific internal energy change \(\Delta \hat{U}=3500 \mathrm{cal} / \mathrm{mol}\)

Liquid water at 60 bar and \(250^{\circ} \mathrm{C}\) passes through an adiabatic expansion valve, emerging at a pressure \(P_{\mathrm{f}}\) and temperature \(T_{\mathrm{f}} .\) If \(P_{\mathrm{f}}\) is low enough, some of the liquid evaporates. (a) If \(P_{\mathrm{f}}=1.0\) bar, determine the temperature of the final mixture \(\left(T_{\mathrm{f}}\right)\) and the fraction of the liquid feed that evaporates \(\left(y_{\mathrm{v}}\right)\) by writing an energy balance about the valve and neglecting \(\Delta \dot{E}_{\mathrm{k}}\) (b) If you took \(\Delta \dot{E}_{\mathrm{k}}\) into account in Part (a), how would the calculated outlet temperature compare with the value you determined? What about the calculated value of \(y_{\mathrm{v}} ?\) Explain. (c) What is the value of \(P_{\mathrm{f}}\) above which no evaporation would occur? (d) Sketch the shapes of plots of \(T_{\mathrm{f}}\) versus \(P_{\mathrm{f}}\) and \(y_{\mathrm{v}}\) versus \(P_{\mathrm{f}}\) for 1 bar \(\leq P_{\mathrm{f}} \leq 60\) bar. Briefly explain your reasoning.

Your friend has asked you to help move a 60 inch \(\times 78\) inch mattress with a mass of 75 Ib \(_{\mathrm{m}}\). The two of you position it horizontally in an open flat-bed trailer that you hitch to your car. There is nothing available to tie the mattress to the trailer, but you know there is a risk of the mattress being lifted from the trailer by the air flowing over it and perform the following calculations: (a) Although the conditions do not exactly match those for which the Bemoulli equation is applicable, use the equation to get a rough estimate of how fast you can drive (miles/h) before the mattress is lifted. Assume the velocity of air above the mattress equals the velocity of the car, the pressure difference between the top and bottom of the mattress equals the weight of the mattress divided by the mattress cross-sectional area, and air has a constant density of \(0.075 \mathrm{lb}_{\mathrm{m}} / \mathrm{ft}^{3}\). What is your result? (b) You see that your friend also has several boxes of books. Since you would like to drive at 60 miles per hour, what weight of books ( \(\left(\mathrm{b}_{\mathrm{f}}\right)\) do you need to put on the mattress to hold it in place?

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