Research Article

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.

 CaseAlgorithmIAEITAEMdEss

Three constant faultsCase 1EPFC [37]52.99554.3860.2650.203
PEO-FOPFC35.35843.0130.1770.185
Case 2EPFC [37]54.75958.2300.2740.217
PEO-FOPFC38.79548.1900.1940.204
Case 3EPFC [37]56.52361.2660.2830.228
PEO-FOPFC42.90352.3100.2150.217

Three time-varying faultsCase 4EPFC [37]56.18254.7150.2810.196
PEO-FOPFC42.43343.6660.2120.174
Case 5EPFC [37]61.11159.6240.3060.206
PEO-FOPFC50.23049.8320.2510.187
Case 6EPFC [37]63.89967.3140.3190.236
PEO-FOPFC55.61359.1160.2780.219