Question 2.13.1: Ten liters of a monatomic ideal gas at 25° C and 10 atm pres...

Ten liters of a monatomic ideal gas at 25° C and 10 atm pressure are expanded to a final pressure of 1 atm. The molar heat capacity of the gas at constant volume, cv c_v , is 3/2 R and is independent of temperature. Calculate the work done, the heat absorbed, and the change in U and in H for the gas if the process is carried out

• Isothermally and reversibly
• Adiabatically and reversibly

Having determined the final state of the gas after the reversible adiabatic expansion, verify that the change in U for the process is independent of the path taken between the initial and final states by considering the process to be carried out as

• An isothermal process followed by a constant-volume process
• A constant-volume process followed by an isothermal process
• An isothermal process followed by a constant-pressure process
• A constant-volume process followed by a constant-pressure process
• A constant-pressure process followed by a constant-volume process

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The size of the system must first be calculated. From consideration of the initial state of the system (the point a in Figure 2.6),

n = the number of moles =PaVaRTa=10×100.08206×298=4.09\frac{P_{a}V_{a}}{RT_{a}} =\frac{10\times 10}{0.08206\times 298} = 4.09

a. The isothermal reversible expansion . The state of the gas moves from a to b along the 298-degree isotherm. Along any isotherm, the product PV is constant:

Vb=PaVaPb=10×101=100V_b =\frac{P_aV_a}{P_b} =\frac{10\times 10}{1} = 100 liters

For an ideal gas undergoing an isothermal process, ΔU = 0, and hence, from the First Law,

q=w=abPdV=nRT=abdVV=4.09×8.3144×298×ln10010J=23.3 kJq=w=\int_{a}^{b}{PdV} =nRT=\int_{a}^{b}{\frac{dV}{V}= 4.09\times 8.3144\times 298\times \ln \frac{100}{10}}J =23.3  kJ

 

Thus, in passing from the state a to the state b along the 298-degree isotherm, the system performs 23.3 kJ of work and absorbs 23.3 kJ of heat from the constant-temperature surroundings.

Since for an ideal gas, H is a function only of temperature , ΔH(ab)=0\Delta H^{\prime }_{(a\rightarrow b)} =0 ; that is,

ΔH(ab)=ΔU(ab)+(PbVbPaVa)=(PbVbPaVa)\Delta H_{(a\rightarrow b)} = \Delta U_{(a\rightarrow b)}+(P_bV_b-P_aV_a) =(P_bV_b-P_aV_a)

 

=nRTb – nRTa=nR(TbTa)=0=nRT_b  –  nRT_a = nR(T_b-T_a)=0

 

b. The reversible adiabatic expansion . If the adiabatic expansion is carried out reversibly, then during the process the state of the system is, at all times, given by PVγ PV^\gamma = constant, and the final state is the point c in the diagram. The volumeVc V_c is obtained from PaVaγ=PcVcγP_aV^{\gamma }_{a} = P_cV^{\gamma }_{c} as

Vc=10×105/313/5=39.8V_c =\left\lgroup\frac{10\times 10^{5/3} }{1} \right\rgroup ^{3/5} = 39.8 liters

and

Tc=PcVcnR=1×39.84.09×0.08206=119T_c =\frac{P_cV_c}{nR} =\frac{1\times 39.8}{4.09\times 0.08206} =119 degrees

The point c thus lies on the 119-degree isotherm. As the process is adiabatic, q = 0, and hence,

ΔU(a)=w=acncvdT=ncv(TCTa)\Delta U_{(a\rightarrow )}= -w =\int_{a}^{c}{nc_vdT} = nc_v(T_C -T_a)

 

=4.09×1.5×8.3144×(119298)J=9.13 kJ= 4.09\times 1.5\times 8.3144\times (119-298)J = -9.13  kJ

 

The work done by the system as a result of the process equals the decrease in the internal energy of the system = 9.13  kJ.

i.  An isothermal process followed by a constant-volume process (the path a → e → c ; that is, an isothermal change from a to e , followed by a constant volume change from e to c ).

ΔU(ae)=0\Delta U^{\prime }_{(a\rightarrow e)} =0, as this is an isothermal change of state

 

ΔU(ec)=qv(ΔV=0\Delta U^{\prime }_{(e\rightarrow c)} =q_v(\Delta V =0, and hence, w=0)

 

=ecncvdT=\int_{e}^{c}{nc_vdT}

 

and as the state e lies on the 298-degree isotherm, then

ΔU(ec)=4.09×1.5×8.3144×(119  298)J=9.13 KJ\Delta U^{\prime }_{(e\rightarrow c)} =4.09\times 1.5\times 8.3144\times (119   298)J= 9.13  KJ

 

Thus,

ΔU(ac)=ΔU(ae)+ΔU(ec)=9.13 KJ\Delta U^{\prime }_{(a\rightarrow c)} =\Delta U^{\prime }_{(a\rightarrow e)}+\Delta U^{\prime }_{(e\rightarrow c)} =-9.13  KJ

 

ii.  A constant-volume process followed by an isothermal process (the path a → d → c ; that is, a constant-volume change from a to d , followed by an isothermal change from d to c ).

ΔU(ad)=qv(ΔV=0\Delta U^{\prime }_{(a\rightarrow d)} =q_v(\Delta V =0, and hence, w=0)

 

=adncvdT=\int_{a}^{d}{nc_vdT } , and as the state d lies in the 119-degree isotherm, then

ΔU(ad)=4.09×1.5×8.3144×(119298)J=9.13 KJ\Delta U^{\prime }_{(a\rightarrow d)}=4.09\times 1.5\times 8.3144\times (119-298)J=-9.13  KJ

 

ΔU(dc)=0\Delta U^{\prime }_{(d\rightarrow c)}=0, as this is an isothermal process, and hence,

ΔU(ac)=ΔU(ad)+ΔU(dc)=9.13 KJ\Delta U^{\prime }_{(a\rightarrow c)}=\Delta U^{\prime }_{(a\rightarrow d)}+\Delta U^{\prime }_{(d\rightarrow c)}=-9.13  KJ

 

iii.  An isothermal process followed by a constant-pressure process (the path a → b → c; that is, an isothermal change from a to b, followed by a constant-pressure change from b to c ).

ΔU(ad)=0\Delta U^{\prime }_{(a\rightarrow d)}=0, as this process is isothermal

ΔU(bc)=qpw\Delta U^{\prime }_{(b\rightarrow c)}=q_p-w, and as Pb=PcP_b=P_c, thenw=Pb(VcVb) w=P_b(V_c-V_b)

=bcncpdT=Pb(VcVb)=\int_{b}^{c}{nc_pdT=P_b(V_c-V_b)}

 

Since cv=1.5 Rc_v=1.5  R and cpcv=Rc_p-c_v=R, then cpcv=Rc_p-c_v=R; and as 1 liter atm equals 101.3 J,

ΔUbc=[4.09×2.5×8.3144×(119298)]\Delta U^{\prime }_{b\rightarrow c} =\left[4.09\times 2.5\times 8.3144\times (119-298)\right]

 

[1×(39.8100)×101.3]J-\left[1\times (39.8-100)\times 101.3\right] J

 

=15.2+6.1=9.1 KJ=-15.2+6.1=-9.1  KJ

 

Thus,

ΔU(ac)=U(ab)+U(bc)=9.1 KJ\Delta U^{\prime }_{(a\rightarrow c)} = U^{\prime }_{(a\rightarrow b)}+ U^{\prime }_{(b\rightarrow c)}=-9.1  KJ

 

iv.  A constant-volume process followed by a constant-pressure process (the path a → f → c ; that is, a constant-volume change from a to f , followed by a constant-pressure change from f to c ).

ΔU(af)=qv(Va=Vf\Delta U^{\prime }_{(a\rightarrow f)} = q_v(V_a=V_f, and hence,w=0) w=0)

 

=afncvdT=\int_{a}^{f}{nc_vdT}

 

From the ideal gas law,

Tf=PfVfnR=1×104.09×0.08206=30 degreesT_f=\frac{P_fV_f}{nR} =\frac{1\times 10}{4.09\times0.08206} =30  degrees

 

That is, the state f lies on the 30-degree isotherm. Thus,

ΔU(af)=4.09×1.5×8.3144×(30298)joules=13.67 KJ\Delta U^{\prime }_{(a\rightarrow f)}=4.09\times 1.5\times 8.3144\times (30-298)joules=-13.67  KJ

 

ΔU(fc)=qpw=fcncpdTPf(VCVf)\Delta U^{\prime }_{(f\rightarrow c)}= q_p-w=\int_{f}^{c}{nc_pdT-P_f(V_C-V_f)}

 

=[4.09×2.5×8.3144×(11930)][1×(39.810)×101.3]J=\left[4.09\times 2.5\times 8.3144\times (119-30)\right]-\left[1\times (39.8-10)\times 101.3\right] J

 

=+7.573.02 KJ=+7.57-3.02  KJ

 

Thus,

ΔU(ac)=ΔU(af)+ΔU(fc)=13.67+7.573.02=9.12 KJ\Delta U^{\prime }_{({a\rightarrow c})}= \Delta U^{\prime }_{({a\rightarrow f})}+\Delta U^{\prime }_{({f\rightarrow c})}=13.67+7.57-3.02 = -9.12  KJ

 

v.  A constant-pressure process followed by a constant-volume process (the path a → g → c ; that is, a constant-pressure step from a to g , followed by a constant-volume step from g to c ).

ΔU(ag)=qpw\Delta U^{\prime }_{({a\rightarrow g})}=q_p-w

 

From the ideal gas law,

TgPgVgnR=10×39.84.09×0.08206=1186T_g\frac{P_gV_g}{nR}=\frac{10\times 39.8}{4.09\times 0.08206}=1186 degrees

and hence, the state g lies on the 1186-degree isotherm. Thus,

ΔU(ag)=[4.09×2.5×8.3144×(1186298)]J\Delta U^{\prime }_{({a\rightarrow g})}=\left[4.09\times 2.5\times 8.3144\times (1186-298)\right]J [10×(39.810)×101.3]J-\left[10\times (39.8-10)\times 101.3\right] J

 

=75.530.2 KJ=75.5-30.2  KJ

 

ΔU(gc)=qv=4.09×1.5×8.3144×(1191186)J=54.4 KJ\Delta U^{\prime }_{({g\rightarrow c})}=q_v=4.09\times 1.5\times 8.3144\times (119-1186)J =-54.4  KJ

 

Thus,

ΔU(ac)=ΔU(ag)+ΔU(gc)=75.530.254.4=9.1 KJ\Delta U^{\prime }_{({a\rightarrow c})}=\Delta U^{\prime }_{({a\rightarrow g})}+\Delta U^{\prime }_{({g\rightarrow c})}=75.5-30.2-54.4 = -9.1  KJ

 

The value of ΔU(ac)\Delta U^{\prime }_{({a\rightarrow c})} is thus seen to be independent of the path taken by the process between the states a and c .

The change in enthalpy from a to c (Figure 2.6). The enthalpy change is most simply calculated from the consideration of a path which involves an isothermal portion, over which ΔH=0\Delta H^\prime =0, and an isobaric portion, over which ΔH=qp=ncpdT\Delta H^\prime =q_p=\int{nc_pdT} . For example, consider the path a → b → c .

ΔH(ab)=0\Delta H^{\prime }_{(a\rightarrow b)} =0

 

ΔH(bc)=qp=ncp(TcTb)\Delta H^{\prime }_{(b\rightarrow c)} = q_p=nc_p(T_c-T_b)

 

=4.09×2.5×8.3144×(119298)J   =15.2 KJ=4.09\times 2.5\times 8.3144\times (119-298)J    =-15.2  KJ

 

and hence,

ΔH(ac)=15.2 KJ\Delta H^{\prime }_{(a\rightarrow c)}=-15.2  KJ

 

or alternatively

ΔH(ac)=ΔH(ac)+(PcVcPaVa)\Delta H^{\prime }_{(a\rightarrow c)}=\Delta H^{\prime }_{(a\rightarrow c)}+(P_cV_c-P_aV_a)

 

=9.12KJ+[(1×39.810×10)×101.3]J=-9.12 KJ+\left[(1\times 39.8-10\times 10)\times 101.3\right]J

 

=9.126.10=15.2 KJ= -9.12 – 6.10= -15.2  KJ

 

in each of the paths (i) to (v), the heat and work effects differ, although in each case the difference q – w equals – 9.12 kJ. In the case of the reversible adiabatic path, q = 0, and hence, w = +9.12 kJ. If the processes (i) to (v) are carried out reversibly, then

•  For path (i), q = – 9.12 + the area aeih
•  For path (ii), q = – 9.12 + the area dcih
•  For path (iii), q = – 9.12 + the area abjh – the area cbji
•  For path (iv), q = – 9.12 + the area fcih
•  For path (v), q = – 9.12 + the area agih

2.6

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