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OCTOBER 19-20, 2012 - YMCA University of Science & Technology

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Proceedings <strong>of</strong> the National Conference on<br />

Trends and Advances in Mechanical Engineering,<br />

<strong>YMCA</strong> <strong>University</strong> <strong>of</strong> <strong>Science</strong> & <strong>Technology</strong>, Faridabad, Haryana, Oct <strong>19</strong>-<strong>20</strong>, <strong>20</strong>12<br />

The objective function given in Eq. (32) can be plotted with respect to the coefficient <strong>of</strong> performance <strong>of</strong> the heat<br />

pump given in Eq. (27) for various k values, as shown in Fig-2. It is apparent from the Fig 2 that there exists a<br />

certain value <strong>of</strong> COP hp at which the objective function bF hp is maximum for a given k value. Thus Eq. (32) can<br />

be maximized with respect to y and x.<br />

Therefore, ∂bF hp / ∂y = 0 and ∂bF hp / ∂x = 0 gives:<br />

y * = √(kk L T L1 ) and (34)<br />

x * = T H1 / [√{(T L1 – y) / (kk H )(1-((kk L )/y))} - 1] (35)<br />

The optimal values <strong>of</strong> x * and y * can be submitted in Eq. (32) to obtain the value <strong>of</strong> bF max<br />

bF hp = 1 / [k{(k H / x * ) + (k L (T L1 – y * ) / y * (T H1 + x * ))}+ b {1 – ((T L1 – y * ) / (T L1 + x * ))}]<br />

(36)<br />

and the optimum coefficient <strong>of</strong> performance is<br />

COP * hp = Q H / W = (T H1 + x * ) / [(T H1 + x * ) - (T L1 – y * )] (37)<br />

2.2 Optimization for Endoreversible Refrigerator system<br />

The model and T-S diagram as given in Fig 1 for an endoreversible heat pump hold schematically for<br />

endoreversible refrigerator also. However, in this case (T H2 – T H1 ) is the ambient temperature and (T L1 – T L2 ) is<br />

the temperature <strong>of</strong> the cooled space. Therefore, Eqs. (1) – (26) can be used for endoreversible refrigerator. The<br />

coefficient <strong>of</strong> performance (COP) for endoreversible refrigerator is:<br />

COP ref = Q L / W = (T L1 - y) / [(T H1 + x) - (T L1 - y)] (38)<br />

The objective function <strong>of</strong> thermoeconomic optimization as proposed by earlier researchers [9, 12-13] is given by<br />

F ref = Q L / (C i + C e + C m ) (39)<br />

C i = a(A H + A L ) + b 1 W<br />

C e = b 2 W = b 2 (Q H - Q L )<br />

And C m = b p (Q H - Q L )<br />

Here b p is equal to equivalent annual operation hours per unit power input.<br />

Substituting the value <strong>of</strong> C i , C e and C m into Eq. (39), gives<br />

F ref = Q L / {a (A H + A L ) + b (Q H - Q L )} (40)<br />

Where b = b 1 + b 2 + b p<br />

Using Eqs. (<strong>20</strong>), (24), and (26) gives<br />

F ref = Q L / Q L [a{(k H / x)((T H1 + x) / (T L1 - y)) + (k L / y) }+ b {((T H1 + x) / (T L1 - y)) - 1}]<br />

Or b F ref = 1 / [k{(k H / x)((T H1 + x) / (T L1 - y)) + (k L / y) }+ {((T H1 + x) / (T L1 - y)) - 1}]<br />

(41)<br />

Where k = a/b; Economical parameter<br />

The objective function given in Eq. (41) can be plotted with respect to the coefficient <strong>of</strong> performance <strong>of</strong> the heat<br />

pump given in Eq. (38) for various k values, as shown in Fig-3. It is apparent from the Fig 3 that there exists a<br />

certain value <strong>of</strong> COP hp at which the objective function bF hp is maximum for a given k value. Thus Eq. (41) can<br />

be maximized with respect to y and x.<br />

Therefore, ∂bF hp / ∂y = 0 and ∂bF hp / ∂x = 0 gives:<br />

x * = √(kk H T H1 ) and` (42)<br />

y * = T L1 / [√{(T H1 + x) / (kk L )(1+ ((kk H )/x))} + 1] (43)<br />

The optimal values <strong>of</strong> x * and y * can be submitted in Eq. (32) to obtain the value <strong>of</strong> bF max<br />

b F ref = 1 / [k{(k H / x * )((T H1 + x * ) / (T L1 – y * )) + (k L / y * ) }+ {((T H1 + x * ) / (T L1 – y * )) - 1}]<br />

(44)<br />

and the optimum coefficient <strong>of</strong> performance is<br />

COP ref = Q L / W = (T L1 – y * ) / [(T H1 + x * ) - (T L1 – y * )] (45)<br />

3.PERFORMANCE ANALYSIS<br />

The variation <strong>of</strong> objective function for refrigerators and heat pumps with respect to the coefficient <strong>of</strong><br />

performance (COP) for various values <strong>of</strong> economic parameter (k), corresponding to both fixed and variable<br />

temperature heat reservoir are shown in Fig 2 and Fig 3, respectively. In each figure, the dotted line represents<br />

curves for a system with fixed temperature heat reservoir, while the curves with solid line show the variation, for<br />

the same system but with variable temperature heat reservoir. In both the cases, for each system, a similar pattern<br />

<strong>of</strong> variation is observed; however, the value <strong>of</strong> COP that maximizes the objective function for the given value <strong>of</strong><br />

31

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