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Not allowing
heat to enter
or leave the
gas




∆Q = 0          ∆Q = ∆U + W   Thermodynamic
                              first law
                0 = ∆U + W

                 ∆U = –W
∆U = –W




Work done by the gas
    W = +ve



     ∆U = –W
∆U = –W




Work done by the gas
                          Work done on the gas
    W = +ve
                              W = –ve


     ∆U = –W
                          ∆U = –(–W) = +W
back



                     γ–1            γ–1
 back
              T1V1         = T2V2

                1–γ        γ    1–γ        γ
back
              p1      T1 = p2         T2
∆U              ∆U = CV,m∆T

          ∆T

          ∆Q = 0
          W = p∆V


       ∆Q = ∆U + W         Thermodynamic
                           first law
       0 = CV,m∆T + p∆V

back   p∆V = –CV,m∆T ---------(1)
For one mole of an ideal gas
                           Initially:         substitute
                           pV = RT
                           After compression:
                           (p + ∆p)(V + ∆V) = R(T + ∆T)
                           pV + p∆V + V∆p + ∆p∆V = RT + R∆T)

                                               Assumed zero
                           RT + p∆V + V∆p + ∆p∆V = RT + R∆T)
                                      p∆V + V∆p = R∆T
Substitute (1) into here             V∆p = R∆T – p∆V
                                     ∆pV = R∆T + CV,m∆T
        Cp,m – CV,m = R              ∆pV = (R + CV,m )∆T
                                           = Cp,m ∆T ---------(2)
∆pV = Cp,m ∆T ---------(2)



(2) :
(1)
                  Cp,m ∆V
        ∆p
              = – C     V
        p          V,m

                                           Cp,m
         ∆p   =   –γ
                       ∆V          γ   =
         p              V                  CV,m

                            ---------(3)
As ∆p  0 and
                 –γ
dp                         dV
         =                          ∆V  0
 p                          V

                     –γ
                            dV
∫   dp
     p
             =   ∫           V

∫
     1 dp = – γ 1 dV
     p               V      ∫                             To adiabatic
      ln p = – γ ln V + m                                   equation

                                       Use log rule
     ln p = ln V–γ + m
         p = e ln V–γ + m              Use log rule
         p = e ln V–γ e m                              p1V1γ = p2V2γ
         p = e ln V–γ (constant)
                      –γ
                                        Use log rule
         p = V (constant)
         pVγ = constant ----------(4)
pVγ = constant
RT γ
V V = constant                  p = RT
                                    V

      γ–1       constant
RTV         =
                constant
TV   γ–1
            =      R
                       Because       R is also a constant

TVγ – 1 =       constant ----------(5)


  T1V1γ – 1 = T2V2γ – 1
                                          To adiabatic
                                            equation
pVγ = constant

  RT γ                             V = RT
p p    = constant                      p

    1–γ   γ    γ
p       R T  = constant
       1–γ γ    constant
     p    T  =      γ
                  R                    Because R γ is also a
       1–γ γ                           constant
     p    T  = constant
                γ                  γ
      1– γ              1–γ
     p1       T1 = p2         T2
                                             To adiabatic
                                               equation
Vf
                     γ
              From pV = constant               W=∫          p dV
                      = k                              Vi
                                                       Vf
                         p = kV–γ                =∫          kV–γ dV
                                                       Vi
                                                              Vf
P
                    Adiabatic                        = k∫          V–γ dV
                                                              Vi
pi                  expansion                                                 Vf
                                                 = k                V–γ+1
                                                                   –γ+1        Vi
                                 T1                      k                    Vf
                                                 =
 pf                  T2                               –γ+1           V–γ+1
                                                                              Vi
                                           k
     0                                =
         Vi         Vf       V
                                          –γ+1       Vf–γ+1        – V –γ+1
                                                                      i
----(1)

     1
=                 –γ+1   – kV –γ+1                pVγ = constant = k
    1–γ     kV   f
                                                  piViγ = pfVfγ = k
                             i

     1
=            pfVfγ ) V –γ+1 – p V γ
    1–γ    (          f      ( i i ) Vi–γ+1
     1
=              pfVf      –    piVi
    1–γ
     1
=              piVi      –    pfVf      ----(2)
    γ –1
     1
=              nRT1 –         nRT2
    γ –1                                             pV = nRT
     nR
=            T1 –                ----------(3)
    γ –1                 T2
nR
W =             T1 –                ∆T = T2 – T1
       γ –1            T2

         nR
 =
                ( –∆T)              γ   = f+2
       f+2                                 f
              –1
          f
            nR                                     Work done on
                   (–∆T)
 =     f+2 – f                                     the gas , W = –ve
          f     f                                   W = +∆U
                                   W = –∆U
       nR
 =      2 (–∆T)                                    Means a rise in
        f                   Work done              its internal
                            by the gas             energy
 =    – nfR ∆T
            2                W = –∆U               T
                            Means a
 = –∆U                      reduction in its T
                            internal energy
Is a process which can be made to retrace its path from
one equillibrium state to another equillibrium state
through small changes at every step.



Isothermal expansion              Isothermal compression
p            Small               p            Small
             step at                          step at
             every                            every
             instant                          instant

0                      V         0                        V
The wall of the container must be as thin as possible
                to allow heat transfer.
     The piston must be light and frictionless.
   carried out very slowly through small steps
                  For a reversible
                  process to occur
                     in practicce

Isothermal expansion              Isothermal compression
p           Small               p             Small
            step at                           step at
            every                             every
            instant                           instant

0                      V        0                        V
Thick insulator so that
                          heat transfer cannot occur
                         Piston must be light
                            and frictionless
                       Must be carried out very
                        quickly through small steps
    For a reversible
    process to occur
       in practicce




    
        
            
              
             
            
            
            
Example 1 :
Example 2 :
Example 3 :
Thermodynamics of gases2
Thermodynamics of gases2

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Thermodynamics of gases2

  • 1.
  • 2. Not allowing heat to enter or leave the gas ∆Q = 0 ∆Q = ∆U + W Thermodynamic first law 0 = ∆U + W ∆U = –W
  • 3. ∆U = –W Work done by the gas W = +ve ∆U = –W
  • 4. ∆U = –W Work done by the gas Work done on the gas W = +ve W = –ve ∆U = –W ∆U = –(–W) = +W
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  • 7. back γ–1 γ–1 back T1V1 = T2V2 1–γ γ 1–γ γ back p1 T1 = p2 T2
  • 8. ∆U ∆U = CV,m∆T ∆T ∆Q = 0 W = p∆V ∆Q = ∆U + W Thermodynamic first law 0 = CV,m∆T + p∆V back p∆V = –CV,m∆T ---------(1)
  • 9. For one mole of an ideal gas Initially: substitute pV = RT After compression: (p + ∆p)(V + ∆V) = R(T + ∆T) pV + p∆V + V∆p + ∆p∆V = RT + R∆T) Assumed zero RT + p∆V + V∆p + ∆p∆V = RT + R∆T) p∆V + V∆p = R∆T Substitute (1) into here V∆p = R∆T – p∆V ∆pV = R∆T + CV,m∆T Cp,m – CV,m = R ∆pV = (R + CV,m )∆T = Cp,m ∆T ---------(2)
  • 10. ∆pV = Cp,m ∆T ---------(2) (2) : (1) Cp,m ∆V ∆p = – C V p V,m Cp,m ∆p = –γ ∆V γ = p V CV,m ---------(3)
  • 11. As ∆p  0 and –γ dp dV = ∆V  0 p V –γ dV ∫ dp p = ∫ V ∫ 1 dp = – γ 1 dV p V ∫ To adiabatic ln p = – γ ln V + m equation Use log rule ln p = ln V–γ + m p = e ln V–γ + m Use log rule p = e ln V–γ e m p1V1γ = p2V2γ p = e ln V–γ (constant) –γ Use log rule p = V (constant) pVγ = constant ----------(4)
  • 12. pVγ = constant RT γ V V = constant p = RT V γ–1 constant RTV = constant TV γ–1 = R Because R is also a constant TVγ – 1 = constant ----------(5) T1V1γ – 1 = T2V2γ – 1 To adiabatic equation
  • 13. pVγ = constant RT γ V = RT p p = constant p 1–γ γ γ p R T = constant 1–γ γ constant p T = γ R Because R γ is also a 1–γ γ constant p T = constant γ γ 1– γ 1–γ p1 T1 = p2 T2 To adiabatic equation
  • 14. Vf γ From pV = constant W=∫ p dV = k Vi Vf p = kV–γ =∫ kV–γ dV Vi Vf P Adiabatic = k∫ V–γ dV Vi pi expansion Vf = k V–γ+1 –γ+1 Vi T1 k Vf = pf T2 –γ+1 V–γ+1 Vi k 0 = Vi Vf V –γ+1 Vf–γ+1 – V –γ+1 i
  • 15. ----(1) 1 = –γ+1 – kV –γ+1 pVγ = constant = k 1–γ kV f piViγ = pfVfγ = k i 1 = pfVfγ ) V –γ+1 – p V γ 1–γ ( f ( i i ) Vi–γ+1 1 = pfVf – piVi 1–γ 1 = piVi – pfVf ----(2) γ –1 1 = nRT1 – nRT2 γ –1 pV = nRT nR = T1 – ----------(3) γ –1 T2
  • 16. nR W = T1 – ∆T = T2 – T1 γ –1 T2 nR = ( –∆T) γ = f+2 f+2 f –1 f nR Work done on (–∆T) = f+2 – f the gas , W = –ve f f  W = +∆U W = –∆U nR = 2 (–∆T) Means a rise in f Work done its internal by the gas energy = – nfR ∆T 2  W = –∆U T Means a = –∆U reduction in its T internal energy
  • 17. Is a process which can be made to retrace its path from one equillibrium state to another equillibrium state through small changes at every step. Isothermal expansion Isothermal compression p Small p Small step at step at every every instant instant 0 V 0 V
  • 18. The wall of the container must be as thin as possible to allow heat transfer. The piston must be light and frictionless. carried out very slowly through small steps For a reversible process to occur in practicce Isothermal expansion Isothermal compression p Small p Small step at step at every every instant instant 0 V 0 V
  • 19. Thick insulator so that heat transfer cannot occur Piston must be light and frictionless Must be carried out very quickly through small steps For a reversible process to occur in practicce         
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