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Thermodynamics Lecture Series

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Presentation on theme: "Thermodynamics Lecture Series"— Presentation transcript:

1 Thermodynamics Lecture Series
Assoc. Prof. Dr. J.J. Second Law – Quality of Energy-Part1 Applied Sciences Education Research Group (ASERG) Faculty of Applied Sciences Universiti Teknologi MARA

2 Quotes It does not matter how slowly you go, so long as you do not stop. --Confucius To be wronged is nothing unless you continue to remember it. --Confucius

3

4 Symbols Q q W V E

5 Introduction - Objectives
Explain the need for the second law of thermodynamics on real processes. State the general and the specific statements of the second law of thermodynamics. State the meaning of reservoirs and working fluids. List down the characteristics of heat engines.

6 Introduction - Objectives
State the difference between thermodynamic heat engines and mechanical heat engines. Sketch an energy-flow diagram indicating the flow of energy and label all the energies and all the reservoirs for a steam power plant. Sketch a schematic diagram for a steam power plant and label all the energies, flow of energies and all the reservoirs.

7 Introduction - Objectives
State the desired output and required input for a steam power plant. State the meaning of engines’ performance and obtain the performance of a steam power plant in terms of the heat exchange. State the Kelvin-Planck statement on steam power plant.

8 Introduction - Objectives
Sketch an energy-flow diagram indicating the flow of energy and label all the energies and all the reservoirs for a refrigerator. Sketch a schematic diagram for a refrigerator and label all the energies, flow of energies and all the reservoirs. State the desired output and required input for a refrigerator.

9 Introduction - Objectives
Obtain the performance of a refrigerator in terms of the heat exchange. Sketch an energy-flow diagram indicating the flow of energy and label all the energies and all the reservoirs for a heat pump. Sketch a schematic diagram for a a heat pump and label all the energies, flow of energies and all the reservoirs.

10 Introduction - Objectives
State the desired output and required input for a a heat pump. Obtain the performance of a a heat pump in terms of the heat exchange. State the Clausius statement for refrigerators and heat pumps. Solve problems related to steam power plants, refrigerators and heat pumps.

11 Review - First Law Piston-cylinders, rigid tanks
All processes must obey energy conservation Processes which do not obey energy conservation cannot happen. Processes which do not obey mass conservation cannot happen Piston-cylinders, rigid tanks Turbines, compressors, Nozzles, heat exchangers

12 Review - First Law Properties will change indicating change of state
How to relate changes to the cause System E1, P1, T1, V1 To E2, P2, T2, V2 Win Wout Mass in Mass out Qin Qout Dynamic Energies as causes (agents) of change

13 Review - First Law Energy Balance
Energy Entering a system - Energy Leaving a system = Change of system’s energy Energy Balance Amount of energy causing change must be equal to amount of energy change of system

14 Review - First Law Energy Balance Ein – Eout = Esys, kJ or
Energy Entering a system - Energy Leaving a system = Change of system’s energy Energy Balance Ein – Eout = Esys, kJ or ein – eout = esys, kJ/kg or

15 Change of system’s mass
Review - First Law Mass Entering a system - Mass Leaving a system = Change of system’s mass Mass Balance min – mout = msys, kg or

16 Energy Balance – Control Volume Steady-Flow
Review - First Law Energy Balance – Control Volume Steady-Flow Steady-flow is a flow where all properties within boundary of the system remains constant with time DEsys= 0, kJ; Desys= 0 , kJ/kg, DVsys= 0, m3; Dmsys= 0 or min = mout , kg

17 Mass & Energy Balance–Steady-Flow CV
Review - First Law Mass & Energy Balance–Steady-Flow CV Mass balance Energy balance qin + win + qin = qout+ wout+ qout, kJ/kg

18 Mass & Energy Balance–Steady-Flow: Single Stream
Review - First Law Mass & Energy Balance–Steady-Flow: Single Stream Mass balance Energy balance qin – qout+ win – wout = qout – qin, kJ/kg = hout - hin + keout– kein + peout - pein, kJ/kg

19 First Law – Heat Exchanger
Boundary has 2 inlets and 2 exits

20 First Law – Heat Exchanger
Boundary has 1 inlet and 1 exit

21 First Law of Thermodynamics
Heat Exchanger no mixing 2 inlets and 2 exits In, 3 In, 1 Exit, 2 Exit, 4

22 First Law of Thermodynamics
Heat Exchanger no mixing 1 inlet and 1 exit In, 3 In, 1 Exit, 2 Exit, 4

23 First Law of Thermodynamics
Heat Exchanger Case 1 Energy balance Mass balance

24 First Law of Thermodynamics
Heat Exchanger Qout Case 2 Mass balance Energy balance

25 First Law of Thermodynamics
Heat Exchanger Energy balance: Case 1 Purpose: Remove or add heat Mass balance: where

26 First Law of Thermodynamics
Heat Exchanger Purpose: Remove or add heat Mass balance: Energy balance: Case 2 where Qout

27 First Law of Thermodynamics
Heat Exchanger Purpose: Remove or add heat Mass balance: Energy balance: Case 2 Qin where

28 Second Law 0 -qout+ 0 - 0 = -Du = u1 - u2, kJ/kg
First Law involves quantity or amount of energy to be conserved in processes Qout Tsys,initial=40C OK for this cup Tsurr=25C Tsys,final=25C This is a natural process!!! Q flows from high T to low T medium until thermal equilibrium is reached

29 Second Law qin – 0 + 0 - 0 = Du = u2 - u1, kJ/kg Tsys,initial=25C
Tsurr=25C Tsys,final=40C This is NOT a natural process!!! Q does not flow from low T to high T medium. Never will the coffee return to its initial state.

30 Second Law qin – 0 + 0 - 0 = Du = u2 - u1, kJ/kg Tsys,initial=25C
Tsurr=25C Tsys,final=40C This is NOT a natural process!!! Q does not flow from low T to high T medium. Never will the coffee return to its initial state.

31 Second Law qin – 0 + 0 - 0 = Du =u2-u1 kJ/kg
First Law involves quantity or amount of energy to be conserved in processes Qin Tsys,initial=25C Tsurr=25C Tsys,final=40C This is a NOT a natural process!!! Q does not flow from low T to high T medium. Never will equilibrium be reached But is the process in this cup possible??

32 Second Law First Law is not sufficient to determine if a process can or cannot proceed

33 Second Law First Law is not sufficient to determine if a process can or cannot proceed Introduce the second law of thermodynamics – processes occur in its natural direction. Heat (thermal energy) flows from high temperature medium to low temperature medium. Energy has quality & quality is higher with higher temperature. More work can be done.

34 Second Law Considerations:
Work can be converted to heat directly & totally. Heat cannot be converted to work directly & totally. Requires a special device – heat engine.

35 Second Law Heat Engine Characteristics:
Receive heat from a high T source. Convert part of the heat into work. Reject excess heat into a low T sink. Operates in a cycle.

36 Performance = Desired output / Required input
Second Law Heat Engines Thermodynamics heat engines – external combustion: steam power plants Combustion outside system Mechanical heat engines – internal combustion: jets, cars, motorcycles Combustion inside system Performance = Desired output / Required input

37 An Energy-Flow diagram for a SPP
Second Law Working fluid: Water High T Res., TH Furnace Purpose: Produce work, Wout, out qin = qH qin - qout = out - in qin = net,out + qout Steam Power Plant net,out net,out = qin - qout qout = qL Low T Res., TL Water from river An Energy-Flow diagram for a SPP

38 A Schematic diagram for a Steam Power Plant
Second Law Working fluid: Water High T Res., TH Furnace qin = qH Boiler Turbine Pump out in Condenser qout = qL qin - qout = out - in Low T Res., TL Water from river qin - qout = net,out A Schematic diagram for a Steam Power Plant

39 Second Law Thermal Efficiency for steam power plants

40 Second Law Thermal Efficiency for steam power plants

41 Second Law Kelvin Planck Statement for steam power plants
It is impossible for engines operating in a cycle to receive heat from a single reservoir and convert all of the heat into work. Heat engines cannot be 100% efficient.

42 Second Law Refrigerator/ Air Cond
Working fluid: Ref-134a High T Res., TH, Kitchen room / Outside house qout – qin = in - out qout = qH Refrigerator/ Air Cond net,in qin = qL net,in = qout - qin Purpose: Maintain space at low T by Removing qL Low Temperature Res., TL, Inside fridge or house net,in = qH - qL An Energy-Flow diagram for a Refrigerator/Air Cond.

43 A Schematic diagram for a Refrigerator/Air Cond.
Second Law Working fluid: Refrigerant-134a High T Res., TH Kitchen/Outside house qout = qH pressor Com Condenser in Throttle Valve Evaporator qin = qL Low T Res., TL Ref. Space/Room A Schematic diagram for a Refrigerator/Air Cond.

44 Second Law Coefficient of Performance for a Refrigerator
Divide top and bottom by qin

45 Second Law Coefficient of Performance for a Refrigerator

46 An Energy-Flow diagram for a Heat Pump
Second Law Working fluid: Ref-134a High Temperature Res., TH, Inside house Purpose: Maintain space at high T by supplying qH qout = net,in + qin qout = qH Heat Pump net,in net,in = qout - qin qin = qL net,in = qH - qL Low Temperature Res., TL, Outside house An Energy-Flow diagram for a Heat Pump

47 A Schematic diagram for a Heat Pump
Second Law Working fluid: Refrigerant-134a High T Res., TH Inside house qout = qH pressor Com Condenser in Throttle Valve Evaporator qin = qL Low T Res., TL Outside the house A Schematic diagram for a Heat Pump

48 Second Law Coefficient of Performance for a Heat Pump

49 Second Law Clausius Statement on Refrigerators/Heat Pump
It is impossible to construct a device operating in a cycle and produces no effect other than the transfer of heat from a low T to a high T medium. Must do external work to the device to make it function. Hence more energy removed to the surrounding.

50 Second Law – Energy Degrade
What is the maximum performance of real engines if it can never achieve 100%?? Factors of irreversibilities less heat can be converted to work Friction between 2 moving surfaces Processes happen too fast Non-isothermal heat transfer

51 Second Law – Dream Engine
Carnot Cycle Isothermal expansion Slow adding of Q resulting in work done by system (system expand) Qin – Wout = U = 0. So, Qin = Wout . Pressure drops. Adiabatic expansion 0 – Wout = U. Final U smaller than initial U. T & P drops.

52 Second Law – Dream Engine
Carnot Cycle Isothermal compression Work done on the system Slow rejection of Q - Qout + Win = U = 0. So, Qout = Win . Pressure increases. Adiabatic compression 0 + Win = U. Final U higher than initial U. T & P increases.

53 Second Law – Dream Engine
Carnot Cycle P -  diagram for a Carnot (ideal) power plant P, kPa , m3/kg qout qin 2 3 4 1

54 Second Law – Dream Engine
Reverse Carnot Cycle P, kPa qout qin 3 4 2 1 , m3/kg P -  diagram for a Carnot (ideal) refrigerator

55 Second Law – Dream Engine
Carnot Principles For heat engines in contact with the same hot and cold reservoir All reversible engines have the same performance. Real engines will have lower performance than the ideal engines.

56 An Energy-Flow diagram for a Carnot SPPs
Second Law Working fluid: Not a factor High T Res., TH Furnace qin = qH P1: 1 = 2 = 3 Steam Power Plants net,out P2: real < rev qout = qL Low T Res., TL Water from river An Energy-Flow diagram for a Carnot SPPs

57 Second Law Rev. Fridge/ Heat Pump
Working fluid: Not a factor High T Res., TH, Kitchen room / Outside house qout = qH Rev. Fridge/ Heat Pump net,in qin = qL Low Temperature Res., TL, Inside fridge or house An Energy-Flow diagram for Carnot Fridge/Heat Pump


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