Mass and Energy Analysis of Control Volumes

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1 MAE 320-Chapter 5 Mass and Energy Analysis of Control Volumes Objectives Develop the conservation of mass principle. Apply the conservation of mass principle to various systems including steady- and unsteady-flow control volumes. Apply the first law of thermodynamics as the statement of the conservation of energy principle to control volumes. Identify the energy carried by a fluid stream crossing a control surface as the sum of internal energy, flow work, kinetic energy, and potential energy of the fluid and to relate the combination of the internal energy and the flow work to the property enthalpy. Solve energy balance problems for steady-flow devices such as nozzles, compressors, turbines, throttling valves, mixers, heaters, and heat exchangers. Apply the energy balance to general unsteady-flow processes with particular emphasis on the uniform-flow process as the model for commonly encountered charging and discharging processes. The content and the pictures are from the text book: Çengel, Y. A. and Boles, M. A., Thermodynamics: An Engineering Approach, McGraw-Hill, New York, 6th Ed., 2008 Conservation of Mass Conservation of mass: Mass, like energy, is a conserved property, and it cannot be created or destroyed during a process. Closed systems: The mass of the system remain constant during a process. Control volumes: Mass can cross the boundaries, and so we must keep track of the amount of mass entering and leaving the control volume. Mass and Volume Flow Rates The differential mass flow rate of a fluid across a a small area element da c : Mass flow rate average velocity: Mass flow rate: Volume flow rate: Mass is conserved even during chemical reactions. The average velocity V avg is defined as the average speed through a cross section. The conservation of mass principle for a control volume (CV): The net mass transfer to or from a control volume during a time interval Δt is equal to the net change in the total mass within the control volume during Δt. General conservation of mass: The mass balance of a control volume: General conservation of mass in rate form: Total mass in a control volume: m CV = CV ρdv or Conservation of mass principle for an ordinary bathtub. 1

2 Mass Balance for Steady-Flow Processes During a steady-flow process, the total amount of mass contained within a control volume does not change with time (m CV = constant). Then the conservation of mass principle requires that the total amount of mass entering a control volume equal to the total amount of mass leaving it. For steady-flow processes, the mass flow rate for multiple inlets and exits: For single stream: Many engineering devices such as nozzles, diffusers, turbines, compressors, and pumps involve a single stream (only one inlet and one outlet). Conservation of mass principle for a twoinlet one-outlet steady-flow system. Special Case: Incompressible Flow The conservation of mass relations can be simplified even further when the fluid is incompressible, which is usually the case for liquids. There is no such thing as a conservation of volume principle. However, for steady flow of liquids, the volume flow rates, as well as the mass flow rates, remain constant since liquids are essentially incompressible substances. During a steady-flow process, volume flow rates are not necessarily conserved although mass flow rates are. Steady, incompressible Steady, incompressible flow (single stream) Example ft = 0.5 in 3 ft V = 2gh Example 5-2 Example Dtan k dt = 2 D jet dh 2gh 2

4 Mass and Energy balances for a steady-flow process Energy balance relations with sign conventions (i.e., heat input and work output are positive) Energy Transport by Mass when kinetic and potential energy changes are negligible: Under steady operation, shaft work and electrical work are the only forms of work a simple compressible system may involve. steam water Energy Transport by Mass Example 5-3 Energy Transport by Mass Example 5-3 Some Steady-flow Engineering Devices Many engineering devices operate essentially under the same conditions for long periods of time. The components of a steam power plant (turbines, compressors, heat exchangers, and pumps), for example, operate nonstop for months before the system is shut down for maintenance. Therefore, these devices can be conveniently analyzed as steady-flow devices. Nozzles and Diffusers Nozzles and diffusers are commonly utilized in jet engines, rockets, spacecraft, and even garden hoses. A nozzle is a device that increases the velocity of a fluid at the expense of pressure. A diffuser is a device that increases the pressure of a fluid by slowing it down. A modern land-based gas turbine used for electric power production. This is a General Electric LM5000 turbine. It has a length of 6.2 m, it weighs 12.5 tons, and produces 55.2 MW at 3600 rpm with steam injection. At very high velocities, even small changes in velocities can cause significant changes in the kinetic energy of the fluid. Nozzles and diffusers are shaped so that they cause large changes in fluid velocities and thus kinetic energies. Energy balance for a nozzle or diffuser: 4

5 Nozzles and Diffusers Nozzles and Diffusers Example 5-4 Nozzles and Diffusers Example 5-4 Nozzles and Diffusers Example 5-4 Energy balance for the compressor and turbine Turbine drives the electric generator In steam, gas, or hydroelectric power plants. As the fluid passes through the turbine, the shaft rotates, and the turbine produces work. Compressors, as well as pumps and fans, are devices used to increase the pressure of a fluid. Work is supplied to these devices from an external source through a rotating shaft. Compressor 5

6 Example 5-7 Example 5-7 Example 5-7 Example 5-7 Throttling valves Throttling valves are any kind of flow-restricting devices that cause a significant pressure drop in the fluid. The pressure drop in the fluid is often accompanied by a large drop in temperature, and for that reason throttling devices are commonly used in refrigeration and air-conditioning. Throttling valves Energy balance Since w=0,, The temperature of an ideal gas does not change during a throttling (h = constant) process since h = h(t). 6

7 Throttling valves Example 5-8 Throttling valves Example 5-8 Mixing chambers In engineering applications, the section where the mixing process takes place is commonly referred to as a mixing chamber. 60 C Mixing chambers 140 kpa 10 C 43 C Energy balance for the adiabatic mixing chamber in the figure is: The T-elbow of an ordinary shower serves as the mixing chamber for the hot- and the cold-water streams. Mixing chambers Example 5-9 Mixing chambers Example 5-9 7

8 Mixing chambers Example 5-9 are devices where two moving fluid streams exchange heat without mixing. Heat exchangers are widely used in various industries, and they come in various designs. A heat exchanger can be as simple as two concentric pipes. The heat transfer associated with a heat exchanger may be zero or nonzero depending on how the control volume is selected. Example 5-10 Example 5-10 Example

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