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Modern Engineering Thermodynamics

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8.2 Systems Undergoing Reversible Processes 253<br />

Solution<br />

First, draw a sketch of the system.<br />

Here, the unknown is _W electrical , and the system is the entire power plant as shown in Figure 8.2. You must now realize<br />

max<br />

that a system like this produces maximum work output when the internal losses (friction etc.) are a minimum, and the<br />

absolute maximum occurs when the system is reversible. Therefore, what we wish to find here is _W electrical<br />

rev :<br />

200.°F<br />

System boundary<br />

Q solar<br />

100. × 10 ³ Btu/h<br />

W elect = ?<br />

Heat<br />

engine<br />

Electrical<br />

generator<br />

Solar collector<br />

River<br />

Condenser<br />

40.0°F<br />

Q condenser<br />

FIGURE 8.2<br />

Example 8.2.<br />

Since no clearly defined system states are given in the problem statement and all the given values are rate values, we recognize<br />

that this problem requires a rate analysis. The energy rate balance (ERB) equation for this system is<br />

_Q net − _W net = _U<br />

+ _ KE + _ PE<br />

0<br />

ðsteady<br />

stateÞ<br />

0<br />

ðassume the system<br />

is stationaryÞ<br />

or<br />

<br />

_W electrical rev = _W net = _Q net<br />

<br />

= _Q solar − j _Q j condenser<br />

Note that there are two heat transfer surfaces in this system (the solar collector and the condenser), each at a different isothermal<br />

temperature, and one work mode (electrical). The entropy rate balance (SRB) equation for this system is<br />

_S =<br />

_ms<br />

0<br />

ðsteady<br />

stateÞ<br />

Z <br />

=<br />

Σ<br />

<br />

_q<br />

T b<br />

dA + _S P<br />

rev<br />

0<br />

ðreversible<br />

systemÞ<br />

The system surface area Σ system is the sum of the surface areas of the collector, condenser, and the remaining surfaces where<br />

no heat transfer occurs<br />

Since the heat transfer surfaces are all isothermal, we can set<br />

Z <br />

_q<br />

Σ<br />

T b<br />

∑ system = ∑ collector +∑ condenser +∑ no heat transfer sufaces<br />

Z<br />

dA =<br />

Σcollector<br />

Z<br />

_q<br />

dA +<br />

T b<br />

Σcondenser<br />

<br />

_q Q<br />

dA =<br />

_ solar<br />

−<br />

T collector <br />

T b<br />

_Q condenser<br />

T river<br />

<br />

(Continued )

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