Fractional-Order Predictive Functional Control of Industrial Processes with Partial Actuator Failures

Table 6

The results of control performance obtained by PEO-FOPFC and PFC on the process flow of coke furnace.

	Case	Algorithm	IAE	ITAE	Md	Ess
Three constant faults	Case 1	EPFC [37]	52.995	54.386	0.265	0.203
		PEO-FOPFC	35.358	43.013	0.177	0.185
	Case 2	EPFC [37]	54.759	58.230	0.274	0.217
		PEO-FOPFC	38.795	48.190	0.194	0.204
	Case 3	EPFC [37]	56.523	61.266	0.283	0.228
		PEO-FOPFC	42.903	52.310	0.215	0.217
Three time-varying faults	Case 4	EPFC [37]	56.182	54.715	0.281	0.196
		PEO-FOPFC	42.433	43.666	0.212	0.174
	Case 5	EPFC [37]	61.111	59.624	0.306	0.206
		PEO-FOPFC	50.230	49.832	0.251	0.187
	Case 6	EPFC [37]	63.899	67.314	0.319	0.236
		PEO-FOPFC	55.613	59.116	0.278	0.219