/*! 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

Methane enters a 3 -cm ID pipe at \(30^{\circ} \mathrm{C}\) and 10 bar with an average velocity of \(5.00 \mathrm{m} / \mathrm{s}\) and emerges at a point 200 m lower than the inlet at \(30^{\circ} \mathrm{C}\) and 9 bar. (a) Without doing any calculations, predict the signs ( \(+\) or \(-\) ) of \(\Delta \dot{E}_{\mathrm{k}}\) and \(\Delta \dot{E}_{\mathrm{p}},\) where \(\Delta\) signifies (outlet - inlet). Briefly explain your reasoning. (b) Calculate \(\Delta \dot{E}_{\mathrm{k}}\) and \(\Delta \dot{E}_{\mathrm{p}}(\mathrm{W}),\) assuming that the methane behaves as an ideal gas. (c) If you determine that \(\Delta \dot{E}_{\mathrm{k}} \neq-\Delta \dot{E}_{\mathrm{p}},\) explain how that result is possible.

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?

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.

One thousand liters of a 95 wt\% glycerol- \(5 \%\) water solution is to be diluted to \(60 \%\) glycerol by adding a \(35 \%\) solution pumped from a large storage tank through a \(5-\mathrm{cm}\) ID pipe at a steady rate. The pipe discharges at a point 23 m higher than the liquid surface in the storage tank. The operation is carried out isothermally and takes 13 min to complete. The friction loss ( \(\hat{F}\) of Equation \(7.7-2\) ) is \(50 \mathrm{J} / \mathrm{kg}\). Calculate the final solution volume and the shaft work in \(\mathrm{kW}\) that the pump must deliver, assuming that the surface of the stored solution and the pipe outlet are both at 1 atm. Data: \(\quad \rho_{\mathrm{H}_{2} \mathrm{O}}=1.00 \mathrm{kg} / \mathrm{L}, \rho_{\mathrm{gly}}=1.26 \mathrm{kg} / \mathrm{L} .\) (Use to estimate solution densities.)

The specific enthalpy of liquid \(n\) -hexane at 1 atm varies linearly with temperature and equals \(25.8 \mathrm{kJ} / \mathrm{kg}\) at \(30^{\circ} \mathrm{C}\) and \(129.8 \mathrm{kJ} / \mathrm{kg}\) at \(50^{\circ} \mathrm{C}\) (a) Determine the equation that relates \(\hat{H}(\mathrm{kJ} / \mathrm{kg})\) to \(T\left(^{\circ} \mathrm{C}\right)\) and calculate the reference temperature on which the given enthalpies are based. Then derive an equation for \(\hat{U}(T)(\mathrm{kJ} / \mathrm{kg})\) at 1 atm. (b) Calculate the heat transfer rate required to cool liquid \(n\) -hexane flowing at a rate of \(20 \mathrm{kg} / \mathrm{min}\) from \(60^{\circ} \mathrm{C}\) to \(25^{\circ} \mathrm{C}\) at a constant pressure of 1 atm. Estimate the change in specific internal energy \((\mathrm{kJ} / \mathrm{kg})\) as the n-hexane is cooled at the given conditions.

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