Van der Waal expansion and delivered work

AI Thread Summary
The discussion centers on the isothermal expansion of one mole of an ideal van der Waals fluid, focusing on calculating the work delivered to a reversible work source (RWS) using the equation dW_{RWS}. The integration of the work equation leads to a formula that incorporates both the heat and work terms, with a specific emphasis on the correction needed for the temperature ratio T_c/T_h. Energy and entropy conservation principles are applied, resulting in equations that relate changes in internal energy, work, and heat. The participant identifies a confusion regarding the two heat terms involved in the calculations. Clarifying the distinction between the subsystem heat and the heat from the RWS is essential for resolving the issue.
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Homework Statement


Assume that one mole of an ideal van der Waals fluid is expanded isothermally, at temperature T_h from an initial volume V_i to a final volume V_f. A thermal reselvoir at temperature T_c is available. Apply <br /> dW_{RWS} = \left ( 1 - \frac{T_{RHS}}{T} \right ) (-dQ) +(-dW)
to a differential process and integrate to calculate the work delivered to a reversible work source (RWS). RHS is reversible heat source. Corroborate by overall energy and entropy conservation.

Hint: remember to add the direct work transfer pdV to obtain the total work delivered to the reversible work source.

Homework Equations


Van der Waal equations:
<br /> u + a/v = cRT<br />
where u, a, v, c, R, T are, respectively, energy per mole, constant, volume per mole, another constant, temperature.
<br /> p = \frac{RT}{v-b} - \frac{a}{v^2}<br />

The entropy is
<br /> S = NR\log [ (v-b)(cRT)^c] + Ns_0<br />
where N is the number of moles and b is another constant.

The Attempt at a Solution


[/B]
Using the first equation with T=T_h, T_{RHS} = T_c and -dW = pdV and integrating we get
<br /> W_{RHS} = - \left ( 1- \frac{T_c}{T_h} \right) Q + RT_h \log \left ( \frac{v_f-b}{v_i - b} \right) + \frac{a}{v_f} - \frac{a}{v_i}<br />
Also energy conservation gives
<br /> \Delta u + W + Q =0<br />
and entropy conservation
R \log \left ( \frac{v_f-b}{v_i - b} \right) + \frac{Q}{T_c} = 0<br />
Finally the energy change is
<br /> \Delta u = \frac{a}{v_i} - \frac{a}{v_f}<br />
Everything seems to work out except that fraction T_c/T_h is the wrong way round and I see no way of dealing with this. Help would be appreciated.
 
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I see my problem: there are two Qs. The first equation was the heat from the subsystem and the energy and entropy the heat RHS.
 
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