Warning: foreach() argument must be of type array|object, bool given in /var/www/html/web/app/themes/studypress-core-theme/template-parts/header/mobile-offcanvas.php on line 20

Steam at 80 psia and \(400^{\circ} \mathrm{F}\) is mixed with water at \(60^{\circ} \mathrm{F}\) and 80 psia steadily in an adiabatic device. Steam enters the device at a rate of \(0.05 \mathrm{lbm} / \mathrm{s}\), while the water enters at \(1 \mathrm{lbm} / \mathrm{s}\). Determine the temperature of the mixture leaving this device when the outlet pressure is 80 psia.

Short Answer

Expert verified
Answer: The final temperature of the mixture leaving the adiabatic mixing device is approximately \(106.77^{\circ} \mathrm{F}\).

Step by step solution

01

Given information

Steam enters the device at 80 psia, 400°F and 0.05 lbm/s Water enters the device at 80 psia, 60°F, and 1 lbm/s Outlet pressure: 80 psia Our goal is to find the temperature of the mixture leaving this device.
02

Define the enthalpy of each stream

Define the enthalpy of the incoming steam as \(h_{steam}\), the enthalpy of the incoming water as \(h_{water}\), and the enthalpy of the mixture as \(h_{mixture}\). We need to find these values to use conservation of energy.
03

Find the properties of steam and water

Use steam tables to find the properties of the incoming steam and water at the given pressures and temperatures. For the steam, at 80 psia and 400°F, we can find: \(h_{steam} = 1203.1 \frac{Btu}{lbm}\) For the water, at 80 psia and 60°F, we can find: \(h_{water} = 28.08 \frac{Btu}{lbm}\)
04

Apply the conservation of energy

The equation for conservation of energy in this adiabatic mixing process is: $$m_{steam}h_{steam} + m_{water}h_{water} = (m_{steam} + m_{water}) h_{mixture}$$ where, \(m_{steam}\) is the mass flow rate of steam = 0.05 lbm/s \(m_{water}\) is the mass flow rate of water = 1 lbm/s
05

Solve the conservation of energy equation for \(h_{mixture}\)

Plug the values into the equation above: $$(0.05)(1203.1) + (1)(28.08) = (0.05 + 1) h_{mixture}$$ Solve for \(h_{mixture}\): $$h_{mixture} = \frac{0.05(1203.1) + 1(28.08)}{0.05 + 1} = 62.312 \frac{Btu}{lbm}$$
06

Find the exit temperature of the mixture

Now, we need to find the temperature corresponding to the calculated \(h_{mixture}\) value. Since the outlet pressure is 80 psia, we will use the steam table at that pressure: 80 psia and enthalpy \(h_{mixture} = 62.312 \frac{Btu}{lbm}\) correspond to a temperature of: \(T_{mixture} = 106.77^{\circ} \mathrm{F}\) (approximately) The temperature of the mixture leaving the device is approximately \(106.77^{\circ} \mathrm{F}\).

Unlock Step-by-Step Solutions & Ace Your Exams!

  • Full Textbook Solutions

    Get detailed explanations and key concepts

  • Unlimited Al creation

    Al flashcards, explanations, exams and more...

  • Ads-free access

    To over 500 millions flashcards

  • Money-back guarantee

    We refund you if you fail your exam.

Over 30 million students worldwide already upgrade their learning with Vaia!

Key Concepts

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

Conservation of Energy in Adiabatic Processes
The principle of the conservation of energy states that energy cannot be created or destroyed, only transformed from one form to another. In thermodynamics, this principle is applied to systems to determine the energy exchange between them and their surroundings. In adiabatic processes, such as the one described in the exercise, there is no heat exchange with the environment - the system is thermally insulated. Hence, the total enthalpy of the incoming steam and water must equal the enthalpy of the mixture leaving the device.

This principle allows us to set up an energy balance equation that accounts for the mass and enthalpy of each stream. By calculating the enthalpy of each component and then applying the conservation of energy, we determine the properties of the mixture at the exit of the adiabatic device. The adiabatic mixing of steam and water without external heat exchange is a practical demonstration of energy conservation in a thermal system.
Enthalpy and Its Role in Thermodynamics
Enthalpy is a measure of the total energy of a thermodynamic system, encompassing both internal energy and the energy required to make room for it by displacing the system's environment. It is a crucial concept in the study of energy transfer during the mixing and heating or cooling of substances.

In our exercise, we refer to the enthalpy values of steam (\(h_{steam}\)) and water (\(h_{water}\)), obtained from steam tables, which are comprehensive references of water and steam properties at various temperatures and pressures. By knowing these values and the mass flow rates of the inputs, we can determine the enthalpy of the resulting mixture (\(h_{mixture}\)). It is important to understand that the enthalpy values are not just abstract numbers but represent the actual energy content within the steam and water, which governs how the two will interact when mixed.
Steam Properties - Understanding Steam Tables
Steam properties are the physical characteristics of steam, such as temperature, pressure, enthalpy, entropy, and specific volume. These properties are essential for the engineering analysis of power plants, heating systems, and any application involving steam.

In the case of an adiabatic mixing process, we use steam tables to find specific properties, such as the enthalpy of steam at a given pressure and temperature (\(400^{\textnormal{o}} \textnormal{F}\) and 80 psia in this problem). Steam tables are indispensable tools that provide these properties in a straightforward manner, removing the need for complex calculations. Material properties like these are the foundational data used to perform the energy balance calculations required to solve our problem.
Mass Flow Rate in Thermal Systems
The mass flow rate is a measure of the amount of mass moving through a cross-section per unit time. This rate is crucial in the analysis of fluid flow systems and is typically measured in units of lbm/s (pounds mass per second) or kg/s (kilograms per second).

In the adiabatic mixing process described in the exercise, we have two different mass flow rates: steam (\(0.05 \textnormal{ lbm/s}\)) and water (\(1 \textnormal{ lbm/s}\)). Accurate measurement and control of these rates are essential for making precise energy balance calculations. The mass flow rates are part of the conservation of energy equation, which allows us to solve for the final temperature of the mixture. Understanding the flow rates helps in predicting system performance and is fundamental in scaling these principles to industrial applications.

One App. One Place for Learning.

All the tools & learning materials you need for study success - in one app.

Get started for free

Most popular questions from this chapter

Air enters the duct of an air-conditioning system at 15 psia and \(50^{\circ} \mathrm{F}\) at a volume flow rate of \(450 \mathrm{ft}^{3} / \mathrm{min}\). The diameter of the duct is 10 in, and heat is transferred to the air in the duct from the surroundings at a rate of \(2 \mathrm{Btu} / \mathrm{s}\). Determine \((a)\) the velocity of the air at the duct inlet and \((b)\) the temperature of the air at the exit.

In a steam heating system, air is heated by being passed over some tubes through which steam flows steadily. Steam enters the heat exchanger at 30 psia and \(400^{\circ} \mathrm{F}\) at a rate of 15 lbm/min and leaves at 25 psia and \(212^{\circ} \mathrm{F}\). Air enters at 14.7 psia and \(80^{\circ} \mathrm{F}\) and leaves at \(130^{\circ} \mathrm{F}\). Determine the volume flow rate of air at the inlet.

The air in a \(6-m \times 5-m \times 4-m\) hospital room is to be completely replaced by conditioned air every 15 min. If the average air velocity in the circular air duct leading to the room is not to exceed \(5 \mathrm{m} / \mathrm{s}\), determine the minimum diameter of the duct.

Hot combustion gases (assumed to have the properties of air at room temperature) enter a gas turbine at \(1 \mathrm{MPa}\) and \(1500 \mathrm{K}\) at a rate of \(0.1 \mathrm{kg} / \mathrm{s}\), and exit at \(0.2 \mathrm{MPa}\) and \(900 \mathrm{K} .\) If heat is lost from the turbine to the surroundings at a rate of \(15 \mathrm{kJ} / \mathrm{s}\), the power output of the gas turbine is \((a) 15 \mathrm{kW}\) (b) \(30 \mathrm{kW}\) \((c) 45 \mathrm{kW}\) \((d) 60 \mathrm{kW}\) \((e) 75 \mathrm{kW}\)

Refrigerant-134a is compressed by a compressor from the saturated vapor state at \(0.14 \mathrm{MPa}\) to \(0.9 \mathrm{MPa}\) and \(60^{\circ} \mathrm{C}\) at a rate of \(0.108 \mathrm{kg} / \mathrm{s} .\) The refrigerant is cooled at a rate of \(1.10 \mathrm{kJ} / \mathrm{s}\) during compression. The power input to the compressor is \((a) 4.94 \mathrm{kW}\) \((b) 6.04 \mathrm{kW}\) \((c) 7.14 \mathrm{kW}\) \((d) 7.50 \mathrm{kW}\) \((e) 8.13 \mathrm{kW}\)

See all solutions

Recommended explanations on Physics Textbooks

View all explanations

What do you think about this solution?

We value your feedback to improve our textbook solutions.

Study anywhere. Anytime. Across all devices.

Sign-up for free