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Energy Transfer by Heat and Work

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Presentation on theme: "Energy Transfer by Heat and Work"— Presentation transcript:

1 Energy Transfer by Heat and Work
Chapter 4 Energy Transfer by Heat and Work

2 Types of Energy: Heat Work Kinetic energy Potential energy Internal energy

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5 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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9 Types of Work: Electrical Work Mechanical Work 1. Moving Boundary Work 2. Shaft Work 3. Spring Work

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11 Mechanical Work: 1. Moving Boundary Work 2. Shaft Work 3. Spring Work
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15 Example 1

16 Example 2

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18 Example 3

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23 Example 4

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25 Example 5

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28 Kinetic Energy Kinetic energy (KE) is the energy associated with velocity and mass flow of material. KE=½mv2 KE is a state variable.

29 Example KE

30 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.)

31 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

32 Example for Potential Energy
pe

33 Potential Energy with Slope
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34 Conservation of Mass “Mass cannot be created or destroyed BUT it can be changed from one form to another”

35 Or: Min-Mout=ΔMsystem

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39 Example 6

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43 Example 8 R-134a compressor 2 0.8 MPa 50C 1 0.14 MPa

44 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)

45 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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