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Transcript
Chapter 20 - Thermodynamics A PowerPoint Presentation by Paul E. Tippens, Professor of Physics Southern Polytechnic State University © 2007 THERMODYNAMICS Thermodynamics is the study of energy relationships that involve heat, mechanical work, and other aspects of energy and heat transfer. Central Heating Objectives: After finishing this unit, you should be able to: • State and apply the first and second laws of thermodynamics. • Demonstrate your understanding of adiabatic, isochoric, isothermal, and isobaric processes. • Write and apply a relationship for determining the ideal efficiency of a heat engine. • Write and apply a relationship for determining coefficient of performance for a refrigeratior. A THERMODYNAMIC SYSTEM • A system is a closed environment in which heat transfer can take place. (For example, the gas, walls, and cylinder of an automobile engine.) Work done on gas or work done by gas INTERNAL ENERGY OF SYSTEM • The internal energy U of a system is the total of all kinds of energy possessed by the particles that make up the system. Usually the internal energy consists of the sum of the potential and kinetic energies of the working gas molecules. TWO WAYS TO INCREASE THE INTERNAL ENERGY, U. +U WORK DONE ON A GAS (Positive) HEAT PUT INTO A SYSTEM (Positive) TWO WAYS TO DECREASE THE INTERNAL ENERGY, U. Wout Qout -U Decrease hot WORK DONE BY EXPANDING GAS: W is positive hot HEAT LEAVES A SYSTEM Q is negative THERMODYNAMIC STATE The STATE of a thermodynamic system is determined by four factors: • Absolute Pressure P in Pascals • Temperature T in Kelvins • Volume V in cubic meters • Number of moles, n, of working gas THERMODYNAMIC PROCESS Increase in Internal Energy, U. Wout Qin Initial State: P1 V1 T1 n1 Heat input Final State: Work by gas P2 V2 T2 n2 The Reverse Process Decrease in Internal Energy, U. Win Qout Initial State: P1 V1 T1 n1 Work on gas Loss of heat Final State: P2 V2 T2 n2 THE FIRST LAW OF THERMODYAMICS: • The net heat put into a system is equal to the change in internal energy of the system plus the work done BY the system. Q = U + W final - initial) • Conversely, the work done ON a system is equal to the change in internal energy plus the heat lost in the process. SIGN CONVENTIONS FOR FIRST LAW • Heat Q input is positive +Wout +Qin U • Work BY a gas is positive -Win U • Work ON a gas is negative • Heat OUT is negative Q = U + W -Qout final - initial) APPLICATION OF FIRST LAW OF THERMODYNAMICS Example 1: In the figure, the Wout =120 J gas absorbs 400 J of heat and at the same time does 120 J of work on the piston. What is the change in internal energy of the system? Qin Apply First Law: Q = U + W 400 J Example 1 (Cont.): Apply First Law Q is positive: +400 J (Heat IN) Wout =120 J W is positive: +120 J (Work OUT) Q = U + W U = Q - W Qin 400 J U = Q - W = (+400 J) - (+120 J) = +280 J U = +280 J Example 1 (Cont.): Apply First Law Energy is conserved: The 400 J of input thermal energy is used to perform 120 J of external work, increasing the internal energy of the system by 280 J The increase in internal energy is: Wout =120 J Qin 400 J U = +280 J FOUR THERMODYNAMIC PROCESSES: • Isochoric Process: V = 0, W = 0 • Isobaric Process: P = 0 • Isothermal Process: T = 0, U = 0 • Adiabatic Process: Q = 0 Q = U + W ISOCHORIC PROCESS: CONSTANT VOLUME, V = 0, W = 0 0 Q = U + W so that Q = U QIN +U QOUT No Work Done -U HEAT IN = INCREASE IN INTERNAL ENERGY HEAT OUT = DECREASE IN INTERNAL ENERGY ISOCHORIC EXAMPLE: No Change in volume: P2 B P1 A PA TA = PB TB V1= V2 400 J Heat input increases P with const. V 400 J heat input increases internal energy by 400 J and zero work is done. ISOBARIC PROCESS: CONSTANT PRESSURE, P = 0 Q = U + W But W = P V QIN QOUT Work Out +U -U Work In HEAT IN = Wout + INCREASE IN INTERNAL ENERGY HEAT OUT = Wout + DECREASE IN INTERNAL ENERGY ISOBARIC EXAMPLE (Constant Pressure): P A B VA TA 400 J Heat input increases V with const. P V1 = VB TB V2 400 J heat does 120 J of work, increasing the internal energy by 280 J. ISOBARIC WORK P A B VA TA 400 J V1 V2 = TB PA = PB Work = Area under PV curve W orkPV VB ISOTHERMAL PROCESS: CONST. TEMPERATURE, T = 0, U = 0 Q = U + W AND QIN U = 0 Q = W QOUT Work Out U = 0 Work In NET HEAT INPUT = WORK OUTPUT WORK INPUT = NET HEAT OUT ISOTHERMAL EXAMPLE (Constant T): PA A B PB U = T = 0 PAVA = PBVB V2 V1 Slow compression at constant temperature: ----- No change in U. ISOTHERMAL EXPANSION (Constant T): PA A B PB U = T = 0 VA VB 400 J of energy is absorbed by gas as 400 J of work is done on gas. T = U = 0 PAVA = PBVB TA = TB Isothermal Work VB W nRT ln VA ADIABATIC PROCESS: NO HEAT EXCHANGE, Q = 0 Q = U + W ; W = -U or U = -W U = -W W = -U U Work Out Q = 0 +U Work In Work done at EXPENSE of internal energy INPUT Work INCREASES internal energy ADIABATIC EXAMPLE: PA A B PB V1 Insulated Walls: Q = 0 V2 Expanding gas does work with zero heat loss. Work = -U ADIABATIC EXPANSION: PA A B PB Q = 0 PAVA TA VA 400 J of WORK is done, DECREASING the internal energy by 400 J: Net heat exchange is ZERO. Q = 0 = PBVB TB VB P AV A P BV B MOLAR HEAT CAPACITY OPTIONAL TREATMENT The molar heat capacity C is defined as the heat per unit mole per Celsius degree. Check with your instructor to see if this more thorough treatment of thermodynamic processes is required. SPECIFIC HEAT CAPACITY Remember the definition of specific heat capacity as the heat per unit mass required to change the temperature? Q c m t For example, copper: c = 390 J/kgK MOLAR SPECIFIC HEAT CAPACITY The “mole” is a better reference for gases than is the “kilogram.” Thus the molar specific heat capacity is defined by: C= Q n T For example, a constant volume of oxygen requires 21.1 J to raise the temperature of one mole by one kelvin degree. SPECIFIC HEAT CAPACITY CONSTANT VOLUME How much heat is required to raise the temperature of 2 moles of O2 from 0oC to 100oC? Q = nCv T Q = (2 mol)(21.1 J/mol K)(373 K - 273 K) Q = +4220 J SPECIFIC HEAT CAPACITY CONSTANT VOLUME (Cont.) Since the volume has not changed, no work is done. The entire 4220 J goes to increase the internal energy, U. Q = U = nCv T = 4220 J U = nCv T Thus, U is determined by the change of temperature and the specific heat at constant volume. SPECIFIC HEAT CAPACITY CONSTANT PRESSURE We have just seen that 4220 J of heat were needed at constant volume. Suppose we want to also do 1000 J of work at constant pressure? Q = U + W Same Q = 4220 J + J Q = 5220 J Cp > Cv HEAT CAPACITY (Cont.) Heat to raise temperature of an ideal gas, U, is the same for any process. U = nCvT For constant pressure Q = U + W nCpT = nCvT + P V Cp > Cv Cp Cv REMEMBER, FOR ANY PROCESS INVOLVING AN IDEAL GAS: PV = nRT Q = U + W PAVA TA = PBVB TB U = nCv T Example Problem: A 2-L sample of Oxygen gas has an initial temperature and pressure of 200 K and 1 atm. The gas undergoes four processes: • AB: Heated at constant V to 400 K. • BC: Heated at constant P to 800 K. • CD: Cooled at constant V back to 1 atm. • DA: Cooled at constant P back to 200 K. PV-DIAGRAM FOR PROBLEM How many moles of O2 are present? Consider point A: PV = nRT PB 1 atm B A 400 K 800 K 200 K 2L PV (101, 300Pa)(0.002m3 ) n 0.122 mol RT (8.314J/mol K)(200K) PROCESS AB: ISOCHORIC What is the pressure at point B? PA TA = 1 atm 200 K B PB A 1 atm PB 200 K 2L TB = 400 K PB 400 K P B = 2 atm or 203 kPa 800 K PROCESS AB: Q = U + W Analyze first law for ISOCHORIC process AB. W = 0 PB 1 atm B A Q = U = nCv T 400 K 800 K 200 K 2L U = (0.122 mol)(21.1 J/mol K)(400 K - 200 K) Q = +514 J U = +514 J W = 0 PROCESS BC: ISOBARIC What is the volume at point C (& D)? VB TB = 2L 400 K VC 1 atm TC = PB B 400 K 800 K C 200 K 2L VC 800 K D 4L VC = VD = 4 L FINDING U FOR PROCESS BC. Process BC is ISOBARIC. P = 0 2 atm B 1 atm U = nCv T 400 K 800 K C 200 K 2L 4L U = (0.122 mol)(21.1 J/mol K)(800 K - 400 K) U = +1028 J FINDING W FOR PROCESS BC. Work depends on change in V. P = 0 Work = P V 2 atm B 400 K 800 K C 200 K 1 atm 2L 4L W = (2 atm)(4 L - 2 L) = 4 atm L = 405 J W = +405 J FINDING Q FOR PROCESS BC. Analyze first law for BC. 2 atm Q = U + W 1 atm Q = +1028 J + 405 J B 400 K 800 K C 200 K 2L 4L Q = +1433 J Q = 1433 J U = 1028 J W = +405 J PROCESS CD: ISOCHORIC What is temperature at point D? PC TC = 2 atm 800 K 1 atm PD A 400 K 200 K 2L TD = PB B 1 atm TD T D = 400 K 800 K C D PROCESS CD: Q = U + W Analyze first law for ISOCHORIC process CD. PB W = 0 400 K 800 K 200 K 1 atm Q = U = nCv T C D 400 K 2L U = (0.122 mol)(21.1 J/mol K)(400 K - 800 K) Q = -1028 J U = -1028 J W = 0 FINDING U FOR PROCESS DA. Process DA is ISOBARIC. P = 0 U = nCv T 400 K 2 atm 1 atm 800 K 200 K A 2L 400 K D 4L U = (0.122 mol)(21.1 J/mol K)(400 K - 200 K) U = -514 J FINDING W FOR PROCESS DA. Work depends on change in V. P = 0 400 K 2 atm 1 atm A Work = P V 200 K 2L 800 K 400 K D 4L W = (1 atm)(2 L - 4 L) = -2 atm L = -203 J W = -203 J FINDING Q FOR PROCESS DA. Analyze first law for DA. 400 K 2 atm Q = U + W 1 atm Q = -514 J - 203 J A 800 K 200 K 2L D 400 K 4L Q = -717 J Q = -717 J U = -514 J W = -203 J PROBLEM SUMMARY For all Q = U + W processes: Process Q U W AB 514 J 514 J 0 BC 1433 J 1028 J 405 J CD -1028 J -1028 J DA -717 J -514 J -203 J Totals 202 J 0 202 J 0 NET WORK FOR COMPLETE CYCLE IS ENCLOSED AREA 2 atm B +404 J C 1 atm Neg 1 atm 2L 2 atm 2 atm B -202 J C B 4L C 1 atm 2L 4L Area = (1 atm)(2 L) Net Work = 2 atm L = 202 J 2L 4L ADIABATIC EXAMPLE: Example 2: A diatomic gas at 300 K and 1 atm is compressed adiabatically, decreasing its volume by 1/12. (VA = 12VB). What is the new pressure and temperature? ( = 1.4) PB B Q = 0 VB PAVA PBVB PAVA = PBVB A PA VA TA = TB ADIABATIC (Cont.): FIND PB B PB PAVA = PBVB 300 K 1 atm A Q = 0 VB 12VB Solve for PB: VA PB PA V B 1.4 12VB PB PA VB P ( 1a tm )(1 2 ) B 1 .4 PB = 32.4 atm or 3284 kPa ADIABATIC (Cont.): FIND TB 32.4 atm 1 atm Q = 0 B TB=? 300 K A VB 12VB (1 atm)(12VB) (300 K) = PAVA PBVB TA TB Solve for TB (32.4 atm)(1 VB) TB = 810 K TB ADIABATIC (Cont.): If VA= 96 cm3 and VA= 8 cm3, FIND W 32.4 atm B 810 K 300 K 1 atm Q = 0 A 8 cm3 W = - U = - nCV T Find n from point A Since Q = 0, W = - U 96 cm3 & PV = nRT CV= 21.1 j/mol K n= PV RT ADIABATIC (Cont.): If VA= 96 cm3 and VA= 8 cm3, FIND W n= PV RT = (101,300 Pa)(8 x10-6 m3) (8.314 J/mol K)(300 K) n = 0.000325 mol & T = 810 - 300 = 510 K W = - U = - nCV T W = - 3.50 J CV= 21.1 j/mol K 32.4 atm B 810 K 300 K 1 atm A 8 cm3 96 cm3 HEAT ENGINES Hot Res. TH Qhot Engine Qcold Cold Res. TC Wout A heat engine is any device which through a cyclic process: • Absorbs heat Qhot • Performs work Wout • Rejects heat Qcold THE SECOND LAW OF THERMODYNAMICS Hot Res. TH Qhot Engine Wout Qcold Cold Res. TC It is impossible to construct an engine that, operating in a cycle, produces no effect other than the extraction of heat from a reservoir and the performance of an equivalent amount of work. Not only can you not win (1st law); you can’t even break even (2nd law)! THE SECOND LAW OF THERMODYNAMICS Hot Res. TH 400 J 100 J Engine Hot Res. TH 400 J Engine 400 J 300 J Cold Res. TC • A possible engine. Cold Res. TC • An IMPOSSIBLE engine. EFFICIENCY OF AN ENGINE Hot Res. TH QH W Engine QC The efficiency of a heat engine is the ratio of the net work done W to the heat input QH. e= W QH = Cold Res. TC e=1- QH- QC QH QC QH EFFICIENCY EXAMPLE Hot Res. TH 800 J Engine 600 J Cold Res. TC W An engine absorbs 800 J and wastes 600 J every cycle. What is the efficiency? QC e=1QH e=1- 600 J 800 J e = 25% Question: How many joules of work is done? EFFICIENCY OF AN IDEAL ENGINE (Carnot Engine) Hot Res. TH QH Engine QC W For a perfect engine, the quantities Q of heat gained and lost are proportional to the absolute temperatures T. e= TH- TC Cold Res. TC e=1- TH TC TH Example 3: A steam engine absorbs 600 J of heat at 500 K and the exhaust temperature is 300 K. If the actual efficiency is only half of the ideal efficiency, how much work is done during each cycle? e=1e=1- TC Actual e = 0.5ei = 20% TH W 300 K 500 K e = 40% e= QH W = eQH = 0.20 (600 J) Work = 120 J REFRIGERATORS Hot Res. TH Qhot Win Engine Qcold Cold Res. TC A refrigerator is an engine operating in reverse: Work is done on gas extracting heat from cold reservoir and depositing heat into hot reservoir. Win + Qcold = Qhot WIN = Qhot - Qcold THE SECOND LAW FOR REFRIGERATORS Hot Res. TH Qhot Engine Qcold Cold Res. TC It is impossible to construct a refrigerator that absorbs heat from a cold reservoir and deposits equal heat to a hot reservoir with W = 0. If this were possible, we could establish perpetual motion! COEFFICIENT OF PERFORMANCE Hot Res. TH QH W Engine QC The COP (K) of a heat engine is the ratio of the HEAT Qc extracted to the net WORK done W. K= Cold Res. TC For an IDEAL refrigerator: QC W K= = QH QH- QC TH TH- TC COP EXAMPLE 500 K Hot Res. TH QH W Eng ine 800 J A Carnot refrigerator operates between 500 K and 400 K. It extracts 800 J from a cold reservoir during each cycle. What is C.O.P., W and QH ? K= TC TH- TC = 400 K 500 K - 400 K Cold Res. TC 400 K C.O.P. (K) = 4.0 COP EXAMPLE (Cont.) 500 K Hot Res. TH QH W Eng ine Next we will find QH by assuming same K for actual refrigerator (Carnot). K= 800 J Cold Res. TC 400 K 4.0 = QC QH- QC 800 J QH - 800 J QH = 1000 J COP EXAMPLE (Cont.) 500 K Hot Res. TH 1000 J W Engine 800 J Cold Res. TC 400 K Now, can you say how much work is done in each cycle? Work = 1000 J - 800 J Work = 200 J Summary The First Law of Thermodynamics: The net heat taken in by a system is equal to the sum of the change in internal energy and the work done by the system. Q = U + W final - initial) • Isochoric Process: V = 0, W = 0 • Isobaric Process: P = 0 • Isothermal Process: T = 0, U = 0 • Adiabatic Process: Q = 0 Summary (Cont.) The Molar Specific Heat capacity, C: Units are:Joules per mole per Kelvin degree Q c = n T The following are true for ANY process: Q = U + W PAVA PBVB TA TB U = nCv T PV = nRT Summary (Cont.) Hot Res. TH Qhot Wout Engine Qcold Cold Res. TC The Second Law of Thermo: It is impossible to construct an engine that, operating in a cycle, produces no effect other than the extraction of heat from a reservoir and the performance of an equivalent amount of work. Not only can you not win (1st law); you can’t even break even (2nd law)! Summary (Cont.) The efficiency of a heat engine: QC e=1- Q H e=1- TC TH The coefficient of performance of a refrigerator: QC QC K Win QH QC TC K TH TC CONCLUSION: Chapter 20 Thermodynamics