/*! 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 52 Horatio Meshuggeneh has his own ... [FREE SOLUTION] | 91Ó°ÊÓ

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Horatio Meshuggeneh has his own ideas of how to do things. For instance, when given the task of determining an oven temperature, most people would use a thermometer. Being allergic to doing anything most people would do, however, Meshuggeneh instead performs the following experiment. He puts acopper bar with a mass of 5.0 kg in the oven and puts an identical bar in a well- insulated 20.0-liter vessel containing 5.00L of liquid water and the remainder saturated steam at \(760 \mathrm{mm}\) Hg absolute. He waits long enough for both bars to reachthermal equilibrium with their surroundings, then quickly takes the first bar out of the oven, removes the second bar from the vessel, drops the first bar in its place, covers the vessel tightly, waits for the contents to come to equilibrium, and notes the reading on a pressure gauge built into the vessel. The value he reads is 50.1 mm Hg. He then uses the facts that copper has a specific gravity of 8.92 and a specific internal energy given by the expression \(\hat{U}(\mathrm{kJ} / \mathrm{kg})=0.36 T\left(^{\circ} \mathrm{C}\right)\) to calculate the oven temperature. (a) The Meshuggeneh assumption is that the bar can be transferred from the oven to the vessel without any heat being lost. If he makes this assumption, what oven temperature does Meshuggeneh calculate? How many grams of water evaporate in the process? (Neglect the heat transferred to the vessel wall- -i.e., assume that the heat lost by the bar is transferred entirely to the water in the vessel. Also, remember that you are dealing with a closed system once the hot bar goes into the vessel.) (b) In fact, the bar lost 8.3 kJ of heat between the oven and the vessel. What is the true oven temperature? (c) The experiment just described was actually Meshuggeneh's second attempt. The first time he tried it, the final gauge pressure in the vessel was negative. What had he forgotten to do?

Short Answer

Expert verified
Under the assumption of no heat loss during the transfer, the oven temperature calculated by Meshuggeneh is roughly 1974.17 °C. To determine the true oven temperature, one must account for the heat loss by the bar between the oven and the vessel, which adjusts the temperature upwards. In the first attempt, a negative final gauge pressure suggests that the copper bar was not sufficiently hot when placed in the vessel.

Step by step solution

01

Calculate the Oven Temperature under the Meshuggeneh Assumption

Under the assumption that there is no heat loss during the bar transfer, the oven temperature is given by the equation: \[ T = \frac{{760-50.1}}{{0.36}} \] Answer: \( T \approx 1974.17 °C \]
02

Calculate the Amount of Water Evaporating

Each gram of water that changes to vapor absorbs a latent heat of vaporization (about 2260 joules/g at normal pressure and temperature). The mass of water that evaporates is then given by the heat lost by the copper bar divided by the latent heat of vaporization: \[ m_{water} = \frac{{\Delta U_{copper}}}{{L_{vap}}} \] where \(\Delta U_{copper}\) is the change in internal energy of the copper bar and \(L_{vap}\) is the latent heat of vaporization.
03

Calculate the True Oven Temperature

If the bar lost heat during the transfer, the actual oven temperature is higher. The heat lost by the bar between the oven and the vessel (\(q = 8.3 kJ\)) must be subtracted from the previous temperature calculation: \[ T_{actual} = T + \frac{{q}}{{0.36 \times m_{copper}}} \] where \(m_{copper}\) is the mass of the copper bar.
04

Determine what went wrong in the First Attempt

If the final gauge pressure was negative in the first attempt, it means the pressure inside the vessel was less than the atmospheric pressure. This could only occur if too little heat was provided to the system, meaning that the copper bar was not hot enough when placed in the vessel. Meshuggeneh might have forgotten to heat the copper bar to the necessary temperature before placing it into the vessel.

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Key Concepts

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

Thermal Equilibrium
Thermal equilibrium is a fundamental concept in thermodynamics referring to a state in which two objects in physical contact with each other cease to exchange energy by heat. At this point, both objects reach the same temperature and no further changes take place without external influence.

In the context of the given exercise, Horatio Meshuggeneh waits for the copper bars to reach thermal equilibrium with their respective environments. This means that the first bar in the oven and the second bar in the well-insulated vessel reach the same temperature as their surroundings. When Meshuggeneh transfers the first bar to the vessel quickly, he minimizes heat exchange with the external environment, assuming no heat loss in the process.

This assumption of no heat loss is quite abstract, as in real-life applications, some heat transfer to the surroundings is inevitable. Understanding thermal equilibrium helps students realize the importance of isolating systems to accurately measure temperature changes, critical for experiments and engineering applications.
Latent Heat of Vaporization
The latent heat of vaporization is the amount of heat required to convert a unit mass of a substance from the liquid phase to the vapor phase without changing its temperature. It is a characteristic property of every substance. For water, it's approximately 2260 joules/gram. This concept explains the significant amount of energy involved in phase transitions.

In the exercise, the latent heat of vaporization comes into play when the hot copper bar is placed in the vessel with water and steam, causing some of the water to evaporate. The amount of heat provided by the copper bar directly corresponds to the mass of water that can be converted into steam, which can be calculated using the heat lost by the copper and the latent heat of vaporization.

Students should note that the latent heat is also indicative of the strong molecular forces present in the liquid phase; considerable energy is needed to overcome these forces during vaporization. Moreover, it's crucial for students to understand that latent heat is a form of energy transfer that occurs at constant temperature during a phase change.
Specific Internal Energy
Specific internal energy is an intensive property of a substance, representing the internal energy per unit mass. It includes the kinetic and potential energies of the molecules of a substance. For example, the specific internal energy for copper is given by the expression \( \hat{U}(\text{kJ} / \text{kg})=0.36 T(\text{°C}) \) in the provided exercise.

This expression allows us to calculate the amount of internal energy within the copper bar based on its temperature. Specific internal energy is a crucial concept in thermal physics and chemical engineering education because it helps students understand energy changes within a system without considering the mass of the substance.

The calculation of oven temperature and the amount of water vaporized in the exercise hinge on this concept. Understanding specific internal energy enables students to track energy flows, which is essential for solving thermal system problems and designing processes involving heat transfer.

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Most popular questions from this chapter

Superheated steam at \(T_{1}\left(^{\circ} \mathrm{C}\right)\) and 20.0 bar is blended with saturated steam at \(T_{2}\left(^{\circ} \mathrm{C}\right)\) and 10.0 bar in a ratio (1.96 kg of steam at 20 bar)/(1.0 kg of steam at 10 bar). The product stream is at 250^'C and 10.0 bar. The process operates at steady state. (a) Calculate \(T_{1}\) and \(T_{2},\) assuming that the blender operates adiabatically. (b) If in fact heat is being lost from the blender to the surroundings, is your estimate of \(T_{1}\) too high or too low? Briefly explain.

Write and simplify the closed-system energy balance (Equation \(7.3-4\) ) for each of the following processes, and state whether nonzero heat and work terms are positive or negative. Begin by defining the system. The solution of Part (a) is given as an illustration. (a) The contents of a closed flask are heated from \(25^{\circ} \mathrm{C}\) to \(80^{\circ} \mathrm{C}\). (b) A tray filled with water at \(20^{\circ} \mathrm{C}\) is put into a freezer. The water tums into ice at \(-5^{\circ} \mathrm{C}\). (Note: When a substance expandsit does work on its surroundings and when it contracts the surroundings do work on it.) (c) A chemical reaction takes place in a closed adiabatic (perfectly insulated) rigid container. (d) Repeat Part (c), only suppose that the reactor is isothermal rather than adiabatic and that when the reaction was carried out adiabatically, the temperature in the reactor increased.

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.

Steam at \(260^{\circ} \mathrm{C}\) and 7.00 bar absolute is expanded through a nozzle to \(200^{\circ} \mathrm{C}\) and 4.00 bar. Negligible heat is transferred from the nozzle to its surroundings. The approach velocity of the steam is negligible. The specific enthalpy of steam is \(2974 \mathrm{kJ} / \mathrm{kg}\) at \(260^{\circ} \mathrm{C}\) and 7 bar and \(2860 \mathrm{kJ} / \mathrm{kg}\) at \(200^{\circ} \mathrm{C}\) and 4 bar. Use the open-system energy balance to calculate the exit steam velocity.

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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