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

In a heating system, cold outdoor air at \(7^{\circ} \mathrm{C}\) flowing at a rate of \(4 \mathrm{kg} / \mathrm{min}\) is mixed adiabatically with heated air at \(70^{\circ} \mathrm{C}\) flowing at a rate of \(3 \mathrm{kg} / \mathrm{min} .\) The exit temperature of the mixture is \((a) 34^{\circ} \mathrm{C}\) (b) \(39^{\circ} \mathrm{C}\) \((c) 45^{\circ} \mathrm{C}\) \((d) 63^{\circ} \mathrm{C}\) \((e) 77^{\circ} \mathrm{C}\)

Short Answer

Expert verified
Answer: (a) 34°C

Step by step solution

01

Conservation of Energy

For an adiabatic process, the total energy of the incoming streams should be equal to the total energy of the outgoing stream. Therefore, the energy equation for this process can be expressed as: \(m_1 c_p(T_1) + m_2 c_p(T_2) = (m_1 + m_2) c_p(T_x)\) where - \(m_1\) and \(m_2\) are the mass flow rates of the two streams (in kg/min), - \(c_p\) is the specific heat capacity of air (in J/kg K), - \(T_1\) and \(T_2\) are the temperatures of the two incoming streams (in °C), - \(T_x\) is the exit temperature we want to find (in °C).
02

Solve for the exit temperature \(T_x\)

Now we can plug in the known values and solve the equation for \(T_x\): \(4 \, kg/min \cdot c_p \cdot (7 ^{\circ} C) + 3 \, kg/min \cdot c_p \cdot (70^{\circ} C) = (4 \, kg/min + 3 \, kg/min) \cdot c_p \cdot (T_x)\). Since \(c_p\) is the same for both flow rates and temperatures, we can cancel it out from the equation: \((4)(7^{\circ} C) + (3)(70^{\circ} C) = (4 + 3)(T_x)\).
03

Calculate the exit temperature

Solve the equation for \(T_x\): \(28^{\circ} C + 210^{\circ} C = 7(T_x)\). \(238^{\circ} C = 7(T_x)\). Now, divide both sides of the equation by 7 to find the exit temperature: \(T_x = 34^{\circ} C\). So, the exit temperature of the mixture is \((a) \, 34^{\circ} C\).

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!

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

Design a scalding unit for slaughtered chickens to loosen their feathers before they are routed to feather-picking machines with a capacity of 1200 chickens per hour under the following conditions: The unit will be of an immersion type filled with hot water at an average temperature of \(53^{\circ} \mathrm{C}\) at all times. Chicken with an average mass of \(2.2 \mathrm{kg}\) and an average temperature of \(36^{\circ} \mathrm{C}\) will be dipped into the tank, held in the water for \(1.5 \mathrm{min}\), and taken out by a slow-moving conveyor. The chicken is expected to leave the tank 15 percent heavier as a result of the water that sticks to its surface. The center-to-center distance between chickens in any direction will be at least \(30 \mathrm{cm} .\) The tank can be as wide as \(3 \mathrm{m}\) and as high as \(60 \mathrm{cm} .\) The water is to be circulated through and heated by a natural gas furnace, but the temperature rise of water will not exceed \(5^{\circ} \mathrm{C}\) as it passes through the furnace. The water loss is to be made up by the city water at an average temperature of \(16^{\circ} \mathrm{C}\). The walls and the floor of the tank are well-insulated. The unit operates \(24 \mathrm{h}\) a day and 6 days a week. Assuming reasonable values for the average properties, recommend reasonable values for \((a)\) the mass flow rate of the makeup water that must be supplied to the tank, (b) the rate of heat transfer from the water to the chicken, in \(\mathrm{kW},(c)\) the size of the heating system in \(\mathrm{kJ} / \mathrm{h},\) and \((d)\) the operating cost of the scalding unit per month for a unit cost of \(\$ 1.12 /\) therm of natural gas.

Air at \(27^{\circ} \mathrm{C}\) and 5 atm is throttled by a valve to 1 atm. If the valve is adiabatic and the change in kinetic energy is negligible, the exit temperature of air will be \((a) 10^{\circ} \mathrm{C}\) \((b) 15^{\circ} \mathrm{C}\) \((c) 20^{\circ} \mathrm{C}\) \((d) 23^{\circ} \mathrm{C}\) \((e) 27^{\circ} \mathrm{C}\)

A scuba diver's \(2-\mathrm{ft}^{3}\) air tank is to be filled with air from a compressed air line at 120 psia and \(85^{\circ} \mathrm{F}\). Initially, the air in this tank is at 20 psia and \(60^{\circ} \mathrm{F}\). Presuming that the tank is well insulated, determine the temperature and mass in the tank when it is filled to 120 psia.

Steam enters a diffuser steadily at \(0.5 \mathrm{MPa}, 300^{\circ} \mathrm{C}\) and \(122 \mathrm{m} / \mathrm{s}\) at a rate of \(3.5 \mathrm{kg} / \mathrm{s}\). The inlet area of the diffuser is \((a) 15 \mathrm{cm}^{2}\) \((b) 50 \mathrm{cm}^{2}\) \((c) 105 \mathrm{cm}^{2}\) \((d) 150 \mathrm{cm}^{2}\) \((e) 190 \mathrm{cm}^{2}\)

Refrigerant-134a expands in an adiabatic turbine from \(1.2 \mathrm{MPa}\) and \(100^{\circ} \mathrm{C}\) to \(0.18 \mathrm{MPa}\) and \(50^{\circ} \mathrm{C}\) at a rate of \(1.25 \mathrm{kg} / \mathrm{s} .\) The power output of the turbine is \((a) 44.7 \mathrm{kW}\) \((b) 66.4 \mathrm{kW}\) \((c) 72.7 \mathrm{kW}\) \((d) 89.2 \mathrm{kW}\) \((e) 112.0 \mathrm{kW}\)

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