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Statistical Mechanics - Homework Assignment 5

Alejandro G´omez Espinosa∗

April 28, 2013

Pathria 8.2 For a Fermi-Dirac gas, we may define a temperature T0 at which the chemical potential of

the gas is zero (z = 1). Express T0 in terms of the Fermi temperature TF of the gas. (Hint: Use

equation (E.16).)

Let us start with Equation (8.1.4): N V = g λ3f3/2(z) = (2πmkT )3/2 h3 gf3/2

where T = T0 as defined in the problem. Then, solving for T0:

T0=

N2/3h2 2πmk(gV f3/2(z))2/3

(1) Then, the Fermi temperature is defined by TF = εkF where the Fermi energy εF is given by the

equation (8.1.24): εF =  3N 4πgV 2/3 h2 2m (2)

Hence, comparing (2) and (1): T0 = N2/3h2 2πmk(gV f3/2(z))2/3 =  4π 3f3/2(z) 2/3 3N 4πgV 2/3 h2 2mπk =  4π 3f3/2(z) 2/3 F πk =  4 3√πf3/2(z) 2/3 TF (3)

Now, let us calculate the factor f3/2(z). Since µ = 0, therefore z = eµβ = 1, thus

f3/2(z = 1) = 1 Γ 32 Z ∞ 0 x1/2 ex+ 1dx (4)

That is an integral easy to calculate using equation (E.16): 1 Γ (j + 1) Z ∞ 0 ηj eη+ 1dη =  1 − 1 2j  ζ(j + 1) ∗ [email protected]

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Hence, equation (4) become: f3/2(z = 1) = 1 Γ 32 Z ∞ 0 x1/2 ex+ 1dx =  1 −√1 2  ζ 3 2  ≈ 0.77 (5)

Plugging this result into (3), we got the final result:

T0=  1.73 √ π 2/3 TF = 0.98TF

Finally, using this result, we combined with knowledge of the low and high temperature limits, to sketch µ as a function of temperature in Figure1.

Figure 1: Sketch of µ/F as function of kT /F using the relation µ

F =

kT F ln e

N/gkT − 1 where, in this

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Pathria 8.13 Show that, quite generally, the low-temperatre behavior of the chemical potential, the spe-cific heat, and the entropy of an ideal Fermi gas is given by

µ ' εF " 1 −π 2 6  ∂ ln a(ε) ∂ ln ε  ε=εF  kT εF 2# (6) and Cv ' S ' π2 3 k 2T a(ε F) (7)

where a(ε) is the density of (the single-particle) states in the system. Examine these results for a gas with energy spectrum ε ≈ ps, confined to a space of n dimensions, and discuss the special cases: s=1 and 2, with n = 2 and 3. (Hint: Use equation E.18)

Let us start with equation (8.1.20):

N = Z F

0

a()d (8)

where the density of states a() is given by: a()d = g()f ()d where f () = (e(−µ)β+1)−1. Then,

N = Z F 0 g()d e(−µ)β+ 1 = 1 β Z F 0 g(βx)dx ex−µ/β+ 1 if x =  β (9)

This integral is similar to equation E.18 given in the book: Z ∞ 0 ψ(x)dx ex−ε+ 1 = Z ε 0 ψ(x)dx +π 2 6  dψ dx  x=ε + ... (10)

Using this relation into (9):

N = 1 β Z µ/β 0 g(βx) dx + π 2 6  dg(βx) dx  x=µ/β + ... ! = 1 β µ β − ε0+ π2 6  dg(βx) dx  x=µ/β + ... ! µ ' εF " 1 −π 2 6  ∂ ln a(ε) ∂ ln ε  ε=εF  kT εF 2#

Now, for the heat capacity at constant volume we need to calculate the internal energy first: U = Z εF 0 a()d = Z εF 0 g() e(−µ)β+ 1d

that is very similar of the result of the chemical potential. In a good approximation: U ' π 2 6  dg(ε) d(/β) (kT )2 F  (11) and for the chemical potential:

Cv =  ∂U ∂T  V = ∂ ∂T  π2 6 dg(ε) d(/β) (kT )2 F  ' π 2 3 k 2T a( F) (12)

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In the case that  ≈ ps, the density of states is given by: a() = gV h34p 2f ()dp = gV 2π2  2m ~ 3/2 1/2 e(−µ)β+ 1d = gV 2π2  2m ~ 3/2 ps/2 e(ps−µ)β + 1sp s−1dp = gV s 2π2  2m ~ 3/2 p3s/2−1 e(ps−µ)β + 1dp

Then, we only need to calculate the term inside the parentesis for each case. For s = 1: a() = gV 2π2  2m ~ 3/2 p3/2−1 e(p−µ)β+ 1dp  dg(βx dx  = gV 2π2  2m ~ 3/2 d dβp 1/2 = gV 2π2  2m ~ 3/2 d dp  βp1/2 = gV 4π2  2m ~ 3/2 βp−1/2

and the thermodinamic variables are: µ ' εF " 1 −π 2 6 gV 4π2  2m ~ 3/2 βp−1/2 kT εF 2# Cv ' S ' π2 3 k 2TgV 4π2  2m ~ 3/2 βp−1/2 For s = 2: a() = gV 2π2  2m ~ 3/2 p6/2−1 e(p2−µ)β + 1dp  dg(βx dx  = gV 2π2  2m ~ 3/2 d dβp 2 = gV 2π2  2m ~ 3/2 d dp β p1/2 2p ! = −gV 8π2  2m ~ 3/2 βp−3/2

and the thermodinamic variables are: µ ' εF " 1 +π 2 6 gV 4π2  2m ~ 3/2 βp−3/2 kT εF 2# Cv ' S ' π2 3 k 2TgV 4π2  2m ~ 3/2 βp−3/2

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Pathria 10.5 Show that the first-order Joule-Thomson coefficient of a gas is given by the formula  ∂T ∂P  H = N Cp  T∂(a2λ 3) ∂T − a2λ 3  (13) where a2(T ) is the second virial coefficient of the gas and H its enthalpy; see equation (10.2.1).

Derive an explicit expression for the Joule-Thomson coefficient in the case of a gas with interparticle interaction u(r) =    +∞ for 0 < r < D, −u0 for D < r < r1, 0 for r1 < r < ∞, (14) and discuss the temperature dependence of this coefficient.

Let us calculate the JT coefficient:  ∂T ∂P  H = − ∂T ∂H  P ∂P ∂H  T = − ∂H ∂P  T ∂H ∂T  P = − 1 Cp  ∂H ∂P  (15) Then, we know that:

dH = CpdT + V  1 − T V  ∂V ∂T  P  dP (16) therefore:  ∂H ∂P  T = V  1 − T V  ∂V ∂T  P  (17) Plugging (17) into (15):  ∂T ∂P  H = − 1 Cp V  1 − T V  ∂V ∂T  P  = 1 Cp  T ∂V ∂T  P − V  (18) Now, let us calculate the partial derivative in the RHS using equation (10.2.1):

P v kT = ∞ X l=1 al(T )  λ3 v l−1 P = kT v ∞ X l=1 al(T )  λ3 v l−1 P = N kT V + N kT V2 a2(T )λ 3+ .... dP = 0 = N k V dT − N kT V2 dV + N k V2  a2λ3− T ∂(a2λ3) ∂T  dT − 2N kTa2λ 3 V3 dV + ... N k V  1 + 1 V  a2λ3− T ∂(a2λ3) ∂T  dT = N kT V2  1 + 2a2λ 3 V  dV  ∂V ∂T  P = V T  1 + 1 V  a2λ3− T ∂(a2λ3) ∂T   1 + 2a2λ 3 V −1 ≈ V T  1 + 1 V  a2λ3− T ∂(a2λ3) ∂T   1 − 2a2λ 3 V + ...  ≈ V T  1 + 1 V  a2λ3− T ∂(a2λ3) ∂T  − 2a2λ 3 V  = V T  1 −a2λ 3 V + T V ∂(a2λ3) ∂T 

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Plugging this result into (18), we found:  ∂T ∂P  H = 1 Cp  T ∂V ∂T  P − V  = 1 Cp  T V T  1 −a2λ 3 V + T V ∂(a2λ3) ∂T  − V  = 1 Cp  V − a2λ3+ T ∂(a2λ3) ∂T − V  = 1 Cp  T∂(a2λ 3) ∂T − a2λ 3 

Now, let us discuss this expression for a gas with interparticle interaction. The term a2 is given by

equation (10.3.1): a2= 2π λ3 Z ∞ 0  1 − e−u(r)β  r2 dr (19)

For the case when 0 < r < D:

a2 = 2π λ3 Z D 0  1 − e−∞β  r2 dr = 2π λ3 Z D 0 r2 dr = 2π λ3 r3 3 D 0 = 2πD 3 3λ3

and the JT coefficient:  ∂T ∂P  H = N Cp T∂ 2πD 3/3 ∂T − 2πD3 3 ! = −2πD 3N 3Cp

For the case when D < r < r1:

a2 = 2π λ3 Z r1 D  1 − eu0βr2 dr = 2π λ3  1 − eu0β Z r1 D r2 dr = 2π λ3  1 − eu0β  r3 3 r1 D = 2π 3λ3  1 − eu0β(r3 1− D3)

and the JT coefficient:  ∂T ∂P  H = N Cp T∂ 2π 3 1 − e u0β (r3 1− D3)  ∂T − 2π 3  1 − eu0β(r3 1 − D3) ! = N Cp −2πT 3 (r 3 1− D3) ∂ eu0/kT ∂T − 2π 3  1 − eu0β  (r13− D3) ! = 2πN 3Cp (r31− D3)u0 kTe u0β1 − eu0β

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For the case when r1 < r < ∞: a2 = 2π λ3 Z ∞ r1 1 − e0 r2 dr = 0

and the JT coefficient:

 ∂T ∂P



H

= 0

From the expressions above, the only temperature dependence of the JT coefficient is when D < r < r1. Since temperature appears in the exponential and the denominator, when T → 0 this term

tends to 2πN3C

p(r

3

References

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