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Energy Transfer by Heat and Work
Chapter 4 Energy Transfer by Heat and Work
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Types of Energy: Heat Work Kinetic energy Potential energy Internal energy
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The Three Types of Heat Transfer
Conduction: is the transfer of energy from the more energetic particles of a substance to the adjacent less energetic ones as a result of interactions between the particles. Convection: is the mode of energy transfer between a solid surface (or liquid) and the adjacent liquid or gas that is in motion, and it involves the combined effects of conduction and fluid motion. Radiation: is the energy emitted by matter in the form of electromagnetic waves (or photons) as a result of the changes in the electronic configurations of the atoms or molecules.
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Types of Work: Electrical Work Mechanical Work 1. Moving Boundary Work 2. Shaft Work 3. Spring Work
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Mechanical Work: 1. Moving Boundary Work 2. Shaft Work 3. Spring Work
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Example 1
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Example 2
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Example 3
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Example 4
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Example 5
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Kinetic Energy Kinetic energy (KE) is the energy associated with velocity and mass flow of material. KE=½mv2 KE is a state variable.
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Example KE
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Example Determine the kinetic energy in Btu/h for 100 gallon/min flow of water through a 3-inch schedule 40 pipe (inside diameter equal to in.)
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Potential Energy Potential energy is the energy associated with elevation changes of material compared to a reference level. PE is a state variable. PE=mgh m- mass g- gravitational acceleration h- elevation change
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Example for Potential Energy
pe
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Potential Energy with Slope
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Conservation of Mass “Mass cannot be created or destroyed BUT it can be changed from one form to another”
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Or: Min-Mout=ΔMsystem
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Example 6
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Example 8 R-134a compressor 2 0.8 MPa 50C 1 0.14 MPa
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Refrigerant-134a enters a compressor as a saturated vapor at a specified pressure, and leaves as superheated vapor at a specified rate. The rates of energy transfer by mass into and out of the compressor are to be determined. Assumptions 1 The flow of the refrigerant through the compressor is steady. 2 The kinetic and potential energies are negligible, and thus they are not considered. Properties The enthalpy of refrigerant-134a at the inlet and the exit are (Tables A-12 and A-13)
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Analysis Noting that the total energy of a flowing fluid is equal to its enthalpy when the kinetic and potential energies are negligible
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