Table 5.

Output result of the energy rate, different exergies, exergoeconomic and exergy efficiency of the components of combined cycle.

Component	$\dot{Q}or\dot{W}\left(kW\right)$	${\dot{Ex}}_f\left(kW\right)$	${\dot{Ex}}_p\left(kW\right)$	${\dot{Ex}}_D\left(kW\right)$	${\eta }_{ex}$	$c_F=\left(\raisebox{1ex}{$\$$}\!\left/ \!\raisebox{-1ex}{$Gj$}\right.\right)$	$c_P=\left(\raisebox{1ex}{$\$$}\!\left/ \!\raisebox{-1ex}{$Gj$}\right.\right)$	${\dot{C}}_D=\left(\raisebox{1ex}{$\$$}\!\left/ \!\raisebox{-1ex}{$h$}\right.\right)$	$\dot{Z}=\left(\raisebox{1ex}{$\$$}\!\left/ \!\raisebox{-1ex}{$h$}\right.\right)$	$f(\%)$
Air compressor	54.05	54.05	46.37	7.679	0.857	29.665	34.693	0.82	0.018	2.147
Fuel compressor	0.717	0.717	0.614	0.103	0.856	29.665	34.693	0.011	0.00013	1.199
Water pump	0.0014	0.0014	0.0012	0.0002	0.817	29.665	107.135	0.000028	0.0003	91.43
Air HX	2206	1316	1108	208.2	0.841	29.665	36.248	22.1	4.958	18.33
Fuel HX	52.2	43.4	27.49	15.91	0.633	29.664	46.665	1.689	0.038	2.219
Water HX	242.57	203.2	75.87	127.3	0.373	29.664	79.247	13.51	0.087	0.6417
Fuel cell	473.3	598.6	487.9	110.6	0.815	21.254	27.702	8.446	2.858	25.24
Afterburner	–	1808	1701	107.8	0.94	27.702	29.664	10.75	0.111	1.029
Hot water HX	246.1	76.49	13.52	62.97	0.176	29.664	174.134	6.682	0.359	–
Generator	25.86	10.92	3.18	7.744	0.291	29.644	118.217	0.821	0.183	18.26
Absorber	23.74	0.998	0.401	0.597	0.401	187.6	594.15	0.403	0.183	31.26
Condenser	17.35	0.429	0.293	0.136	0.683	141.079	380.544	0.069	0.183	72.65
Evaporator	15.15	1.257	0.823	0.434	0.654	141.134	277.492	0.22	0.183	45.41
Solution HX	10.3	1.08	0.677	0.402	0.627	141.134	300.269	0.204	0.183	47.28
Solution pump	0.077	0.077	0.061	0.015	0.795	10	23.571	0.0005	0.0024	81.06
Solution pressure relief valve	–	516.4	516.3	0.045	0.999	141.134	141.218	0.022	–	–
Refrigerant pressure relief valve	–	271.1	271	0.108	0.999	141.079	141.107	0.055	–	–