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Thermodynamics and Statistical Physics B Zheng 1 Zhejiang Institute of Modern Physics Zhejiang University Hangzhou 310027 P R China 1e mail zheng tel 0086 571 87952753 Fax 0086 571 87952754 Chapter 1 Thermodynamics The key point learn how to describe many body systems 1 1Thermal equilibrium and temperature 1 1 1Macroscopic thermodynamic state The system considered in thermodynamics is a macroscopic system which consists of many microscopic particles or ele ments e g gases liquids solids plasmas granular matter celestial matter human being companies Thermodynamics is an empirical theory for the macro scopic systems typically based on experiments or observa tions Important the system contains many particles e g 1 cm3gas consists of 1019molecules Why not mechanics et al Historically one didn t know what heat is also the microscopic structure of the macroscopic system It is too diffi cult to solve the equations of motion Complexity in many body systems compared with few body systems 1 Therefore one introduces some macroscopic parameters or observables to describe the macroscopic properties of the system Mechanical parameters pressure P volume V chemical parameters density n chemical potential Electromagnetic parameters electric fi eld E magnetic fi eld B Thermal parameters temperature T heat entropy S T and S are exclusively from thermodynamics A macroscopic state is described by a complete set of parameters We may construct a parameter space with the complete set of parameters x1 x2 xM then a state i can be represented by a point xi 1 xi2 xiM in the space When the system changes its states the point moves and forms a surface The number of parameters in the complete set is fi xed for a system This is important and should be always kept in mind E g for a dilute gas the number is two All other parameters can be expressed as functors of the complete set of parameters We should fi nd the laws governing these parameters 2 Classifi cation of the macroscopic states equilibrium state parameters do not depend on time t this is what we study in this course non equi state parameters evolves as t or more complicated e g one needs local parameters Classifi cation of the systems An isolated system nothing is exchanged with the environment A thermally isolated system no heat is exchange with the environment Classifi cation of the parameters Extensive parameters V Intensive parameters independent of V It is a good approximation that all physical parameters are either extensive or intensive Question why Why may such a classifi cation be useful e g for a system not too far from equilibrium we may divide it into many pieces then the extensive parameters can be just added up 1 1 2Thermal equilibrium and temperature We can easily understand pressure volume density et al which can be defi ned with the knowledge in other subjects So let us concentrate our attention on thermal observables e g the temperature fi rst 3 In the daily life we feel hot or cold what is it How to quantitatively describe it Observation Initially two systems are diff erently hot or cold then they thermally touch each other After a long time they become equally hot or cold Then we call that they are in thermal equilibrium The zero th law If systems A and B are each in thermal equilibrium with a third system C then A and B are in thermal equilibrium with each other Let us introduce a parameter T i e the temperature to describe how hot or cold the system is and assume the temperatures of two system in thermal equilibrium are the same The last assumption is very important Otherwise we can not compare the temperatures of diff erent systems and T is useless The zero th law is essential Otherwise T is not unique not well defi ned In other words the zeroth law defi nes the temperature Question why do we feel diff erently when touching wood and iron at a same temperature Furthermore T is a property of the macroscopic state This is clear from the defi nition which does not depend on any his tory how the system comes to thermal equilibrium this is somehow also an assumption i e we may have a com plete set of parameters already even without the temper ature As mentioned before we may introduce many param eters to describe the macroscopic properties of a system but not all are independent Assuming x1 x2 xM is a complete set T should be the function of x1 x2 xM i e 4 f T x1 x2 xM 0 This is called the equation of state E g 1 The Ideal gas PV NkT N number of molecules k Boltzmann s constant 1 38 10 16erg deg T temperature 2 Real gases Assuming P is not too high PV A BP CP 2 A B0 V C0 V 2 A B B0 C C0 all are functions of T 1 1 3Temperature scales To defi ne the temperature scale we may proceed as follow 1 choose a specifi c system 2 choose a specifi c property which depends on temper ature 3 fi x the relation between this property and T 4 set the unit of T E g 1 water 2 volume 3 liner relation between V and T 4 the transition point from liquid to solid is T 0 the transition point from gas to liquid is T 100 Mathematically T aV b 0 aVi b 100 aVf b 5 then a 100 Vf Vi b 100Vi Vf Vi To defi ne temperature in this way however theoreti cally is not so elegant for it depends on the system and the property we choose It is not universal and it is diffi cult to accurately measure it A somewhat better choice is to choose the ideal gas as the specifi c system Experimentally it is set up that at a certain fi xed temperature PV const depending on temperature Fix V following the above procedure TV 100 P Pi Pf Pi Fix P TP 100 V Vi Vf Vi ExerciseProveTV TP Hint assume PV aVTV bVand PV aPTP bP and prove aV aPand bV bP Proof Since PVi aV100 P Pi Pf Pi bV therefore aV Pf Pi 100 Vi bV aV 100Pi Pf Pi PiVi Similarly PiV aP100 V Vi Vf Vi bP 6 therefore aP Vf Vi 100 Pi bP ap 100Vi Vf Vi PiVi Since PfVi VfPi fi xed by the boiling point of water aP aVbP bV The ideal gas temperature scale PV NkT 1 2 The fi rst law 1 2 1Thermodynamic transformation A change of state is a thermodynamic transformation The transformation can be realized only by the external con dition Note that here we only consider the equilibrium state If the external condition changes so slowly that at any moment the system is approximately in equilibrium the transformation is called quasi static For example for the ideal gas every point on the P V space represents an equilibrium state and a quasi static transformation is a continuous path on the P V diagram If not specifi ed we concern only quasi static transfor mation The concept of work is taken over from mechanics For a system described by P V the work done by the system in an infi nitesimal transformation is dW PdV Question why 7 e g in Fig 1 1 dW P S dx For a fi nite process W Z dW Z PdV Important Work is not fi xed by the initial and fi nal states but depends on the specifi c process between the initial and fi nal states Now it comes another thermal concept heat Heat is what is absorbed by a system if its temperature in creases while no work is done e g as shown in Fig 1 2 for T2 T1 Obviously the temperature of system 1 will increase therefore something should fl ow from system 2 to system 1 otherwise the temperature of system 1 will not increase Apparently dQ CdT C is called the heat capacity it depends on the detailed nature of the system e g CVand CP Experimentally we may fi x the unit of Q with a spe cifi c system e g increase the temperature of water by one degree Q R dQ is also process dependent 1 2 2 The fi rst law For an arbitrary transformation given the initial and fi nal states let Qdenote the heat absorbed by the system Wdenote the work done by the system Minus sign of Q and W represents the opposite di rection The fi rst law states that the quantity U defi ned by U Q W 8 Figure 1 1 Figure 1 2 9 is the same for all possible transformations i e it only depends on the initial and fi nal states This immediately defi nes a state function U called the internal energy Of course it is defi ned only up to a con stant Experimentally it is found that U is extensive U being a state function means for an infi nitesimal transfor mation dU dQ dW is exact That is dU is a diff erential e g if U U P V dU U P V dP U V P dV dU being exact leads to V U P V P P U V P V Question how to prove that dU being exact is equivalent to U being a state function Actually it is also equivalent to that any loop integrals are zero or any integrals between two states are path in dependent If the number of independent parameters is one U U P U P Z P2 P1 dU P U P2 U P1 If the number of independent parameters is two as shown in Fig 1 3 U U P V 10 U Z P2 V2 P1 V1 dU P V Z P2 V2 P1 V1 dU P VC P U P2 V2 U P1 V1 What is the physical meaning of the fi rst law It states that heat is also a kind of energy and it is feasible to con vert mechanical work into heat or vice verse When talking about energy conservation heat should be included Then what is heat Heat is the energy transferred through microscopic ir regular motion of molecules or particles or elements Ir regular here means looking at macroscopically Of course the microscopic motion is still governed by the Newton s laws et al U excludes the global mechanical energy U includes the energy of irregular motion interacting energy between molecules energy inside a molecule and energy in a fi eld The temperature measures how irregular the microscopic motion is This will be understood in statistical physics 1 2 3Some applications 1 Exercises 1 5 1 6 1 7 in the textbook It can be deduced that CV Q T V U T V from 1 7 CP Q T P H T P from 1 6 H U PV called enthalpy 2 Free expansion of an ideal gas 11 Experimental fi nding T1 T2in Fig 1 3 in the textbook Since W 0 T 0 Therefore Q 0 since T 0 U 0 from the 1st law We may take T and V as independent variables U U T V Therefore U U T since V is non zero 3 4 b c in the textbook page 9 1 3The second law 1 3 1Reversible and irreversible transformations Observation All naturally occuring processes proceed in one direc tion only They never of their own accord proceed in the opposite direction E g A stone resting on the ground never leaps up into the air A cup of hot coff ee never gets hotter The molecules of a drop of ink in a glass of water spread uniformly throughout the volume of the water They never regroup into a drop shaped clump The second law concerns the direction of the processes A reversible transformation is a transformation that the system retraces its history in time when the external con dition retraces its history in time Important If only the system retraces its history the environment not the transformation is not reversible 12 Examples of irreversible transformations All naturally occuring processes are irreversible These are the processes that the systems relax from their non equilibrium states to equilibrium states they never go in the opposite direction A process contains a relaxation from a non equilibrium state to an equilibrium state For example as it is shown in Fig 1 4 Examples of reversible transformations A and B systems are in thermal equilibrium As shown in Fig 1 5 We increase the temperature of B by dT then a certain amount of heat dQ will be transferred to A Then we cool down B by dT the same dQ will be transferred from A back to B Question if dT is fi nite is it still reversible Fig 1 8 in the textbook A heat reservoir is a system so large that the gain or loss of any fi nite amount of heat does not change its temperature The system absorbs the heat from the reservoir and transfers the energy to the spring This process can be reversed diff erent from free expansion Reversible transformations have to be quasi static but reverse is not necessarily true But such examples are rare we may usually think that quasi static and reversible are equivalent Discussions why irreversible E g as shown in Fig 1 6 Newton s equations are re versible in time Therefore the mechanical motion of the 13 Figure 1 3 Figure 1 4 14 Figure 1 5 Figure 1 6 15 microscopic particles is reversible Why is the macroscopic process irreversible Indeed microscopically if we start from a microscopic confi guration in the fi nal macroscopic state with V2 and reverse the motion of all particles the particles will come back to the microscopic state in the initial state with V2 But this probability is very small The probability for a particle to stay in V1is V1 V2 N Since the number N of the particles is a big number V1 V2 N is infi nitesimal small In simple words the initial condition violates the reversibility of the Newton s law in time 1 3 2The second law Kelvin statement There exists no thermodynamic trans formation whose sole eff ect is to extract a quantity of heat from a given heat reservoir and to convert it entirely into work Otherwise we would not have any energy crisis Clausius statement There exists no thermodynamic trans formation whose sole eff ect is to transfer a quantity of heat from a colder reservoir to a hotter reservoir That is why we need refrigerators E g when an ideal gas is expanded reversibly and isother mally a quantity of heat absorbed from the reservoir is entirely converted to work However this process is al lowed by the second law because the volume of the gas is changed i e the word sole is violated Adiabatic expansions don t violate the second law since the work is not converted from heat rather from the change of state 16 From the view of a relaxation from a non equilibrium state to an equilibrium state Clausius statement is obvi ous Kelvin and Clausius statements are equivalent Proof standard way Kvalid Cvalid Cvalid Kvalid alternative way Kfalse Cfalse Cfalse Kfalse because it cannot happen KvalidCfalse orKfalseCvalid therefore it can only be KvalidCvalid orKfalseCfalse The key point what are known and what are unknown Kfalse Cfalse If K is false we may extract heat from a reservoir at temperature T1 and convert it to work with no other ef fect Experimentally it is found that it is possible to convert work entirely into heat e g simply press an ideal gas That is why we formulate K Therefore we can convert this work into heat and deliver it to a reservoir at T2 T1 Then the net result of the two step process is the transfer of an amount of heat from a colder reservoir to a hotter reservoir C is false 17 Cfalse Kfalse Experimentally it is found that it is possible to extract a quantity of heat from a reservoir at temperature T2 and convert a part of it to work and deliver another part to a reservoir at T1 T2 That is also why we formulate K Suppose C false we may transfer heat Q2from a reser voir at temperature T1to a reservoir at T2 T1 Then we extract Q2from the reservoir at T2 and convert it partially to work and reject certain heat to the reservoir at T1 The net result is that an amount of heat is extracted from the reservoir at T1and converted entirely into work with no other eff ect Hence K is false 1 4Carnot s theorem 1 4 1The Carnot engine An engine is a machine which convert heat into work An engine which does everything in a reversible way is called a Carnot engine e g as shown in Fig 1 7 a bis isothermal heat Q2is absorbed by the system b cadiabatic c disothermal heat Q1is rejected by the system d aadiabatic Work is done by the system in every step positively from a b and b c and negatively from c d and d a In one cycle U 0 the work done by the system according to the fi rst law W Q2 Q1 18 The effi ciency of the engine is W Q2 1 Q1 Q2 We may prove that if W 0 then Q1 0 Q2 O Proof reading materials If Q1 0 it violates the Kelvin statement Suppose Q1 0 FromW Q2 Q1 0 it follwsQ2 0 Exercise If W 0 and Q1 0 then Q2 0 This is a refrigerator but it is trivial betterIf Q1 0 then W 0 Q2 Q1 0Q0 2 Q0 1 0 Let Q2 Q02 N0 N where N N0are integers This equality will be valid by making N N0 suffi ciently large It is important to keep in mind that the Carnot engine can be operated in reverse i e change the sing of W Q1 and Q2 Now operate the C engine N cycles in reverse and the X engine N0cycles Wtotal N0W 0 NW Q2 total N0Q0 2 NQ2 0 Q1 total N0Q0 1 NQ1 On the other hand from the fi rst law and U total 0 Wtotal Q2 total Q1 total Q1 total IfWtotal 0 it violates the Kelvin statement Therefor Wtotal 0 i e Q1 total 0 In other words N0Q0 1 NQ1 0 from Q1 Q2 Q0 1 Q02 21 Figure 1 7 Figure 1 8 22 i e 1 Q1 Q2 1 Q0 1 Q02 Since X can be a Carnot engine Thus we have Corollary All Carnot engines have the same effi ciency In the proof of the Carnot theorem the key point is to choose one of the Wtotal Q2 totaland Q1 totalto be zero then apply the fi rst and second laws to prove the theorem An alternative way to prove the Carnot theorem Operate the C engine N cycles in reverse and the X engine N0 and let Wtotal N0W 0 NW 0 Q2 total N0Q0 2 NQ2 Q1 total N0Q0 NQ1 From the second laws Q2 total 0 Hence N0Q0 2 NQ2 therefore W Q2 W 0 Q02 Note that assuming Wtotal W 0 W 0 one may also prove the Carnot theorem However this is not general since the effi ciency may depend on the work W 1 4 3Absolute scale of temperature The Carnot s theorem tells something absolute it may be used for defi ning a better temperature scale 23 If the effi ciency of a Carnot engine is we defi ne the absolute scale of temperature by T1 T2 1 Since 0 0 T2 0 If 1 it violates the second law Note that does not fi x the unit since 1 T1 T2 T1 T2 To defi ne the unit we note that T1 T2 Q1 Q2 hence T1 Q1 T2 Q2 Similarly we fi x W Qn 1 Qnindependent of n and have Tn Qn Tn 1 Qn 1 i e both W and the ratio Tn Qnare independent of n Choosing W such that Tn 1 Tn Tn Qn Qn 1 Qn Tn Qn W 1K That is the unit of the absolute scale of temperature Here we assume that 1K is known empirically If it is not we may defi ne the unit Tn 1 Tn by fi xing W to be a certain amount The absolute scale of temperature is independent of the specifi c properties of any substance 24 T 0 is the greatest low bound and is called the ab solute zero No Carnot engine exists with a reservoir of T 0 But this has not yet meant that T can not be zero The absolute
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