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. 2024 Nov 4;14:26593. doi: 10.1038/s41598-024-77275-z

Table 1.

Optimal control variables of BCS were obtained in all cases.

MODE NSCBO
Control variables Case 1 Case 2 Case 3 Case 1 Case 2 Case 3
Pg1 (MW) 117.6738 122.79 104.248 117.917 122.92 105.10
Pg2 (MW) 58.3414 52.121 54.7094 56.6998 52.494 58.886
Pg5 (MW) 27.1461 30.961 30.9903 25.9895 30.998 31.289
Pg8 (MW) 35.0000 35.000 35.0000 35.0000 35.000 35.000
Pg11 (MW) 25.7737 26.430 30.0000 27.3524 26.528 29.382
Pg13 (MW) 25.0592 21.313 33.1979 25.8268 20.681 28.458
Vg1 (p.u.) 1.0719 1.1000 1.0970 1.1000 1.0999 1.1000
Vg2 (p.u.) 1.0593 1.0912 1.0777 1.0871 1.0907 1.0847
Vg5 (p.u.) 1.0323 1.0685 1.0542 1.0555 1.0687 1.0644
Vg8 (p.u.) 1.0417 1.0781 1.0703 1.0692 1.0775 1.0832
Vg11 (p.u.) 1.0788 1.0974 1.0941 1.0999 1.0993 1.0895
Vg13 (p.u.) 1.0501 1.1000 1.0735 1.1000 1.1000 1.0918
t6−9 (p.u.) 1.0334 1.0399 1.0050 0.9583 1.0440 0.9722
t6−10 (p.u.) 0.9385 0.9243 1.0048 1.0031 0.9000 1.0446
t4−12 (p.u.) 0.9796 1.001 0.9844 1.0549 0.9784 1.0151
t28−27 (p.u.) 0.9753 0.9774 0.9866 0.9765 0.9652 0.9872
bsh10 (p.u.) 0.0126 0.0500 0.0150 0.0388 0.0500 0.0381
bsh12 (p.u.) 0.0190 0.0436 0.2379 0.0341 0.0498 0.0124
bsh15 (p.u.) 0.0393 0.0461 0.2235 0.0500 0.0471 0.0000
bsh17 (p.u.) 0.0488 0.0500 0.4190 0.0001 0.0491 0.0246
bsh20 (p.u.) 0.0385 0.0463 0.0366 0.0500 0.0385 0.0376
bsh21 (p.u.) 0.0500 0.0500 0.0094 0.0306 0.0500 0.0500
bsh23 (p.u.) 0.0257 0.0459 0.0423 0.0000 0.0245 0.0376
bsh24 (p.u.) 0.0498 0.0497 0.0325 0.0404 0.0500 0.0376
bsh29 (p.u.) 0.0247 0.0217 0.0500 0.0359 0.0233 0.0297
TFC ($/h) 830.9120 827.791 851.9996 830.551 827.54 847.17
EP (ton/h) 0.2486 0.2603 0.2300 0.2481 0.2540 0.2326
APL (MW) 5.5944 5.2312 4.7459 5.3860 5.2293 4.7238

Bold Values indicated that the results obtained by the proposed algorithm.