Research Article
Nonlinear PI Control with Adaptive Interaction Algorithm for Multivariable Wastewater Treatment Process
Table 4
Comparative of controller performance for Case 1.
| | | Benchmark PI | Fixed | Adaptive | ā |
-% | ā | -% |
| Dry | Mean | 0.0840 | 0.0695 | 17.3052 | 0.0688 | 18.1381 | IAE | 0.5883 | 0.4814 | 18.1724 | 0.4813 | 18.1894 | ISE | 0.0840 | 0.0547 | 34.8616 | 0.0547 | 34.8616 | Max(dev) | 0.3963 | 0.3101 | 21.7532 | 0.3058 | 22.8382 | Std(dev) | 0.1095 | 0.0884 | 19.2915 | 0.0884 | 19.2915 |
| Rain | Mean | 0.0795 | 0.0688 | 13.4939 | 0.0666 | 16.2601 | IAE | 0.5567 | 0.4665 | 16.2056 | 0.4665 | 16.2056 | ISE | 0.0747 | 0.0513 | 31.3556 | 0.0512 | 31.4894 | Max(dev) | 0.3851 | 0.2992 | 22.2958 | 0.2868 | 25.5162 | Std(dev) | 0.1033 | 0.0856 | 17.1506 | 0.0855 | 17.2474 |
| Storm | Mean | 0.0809 | 0.0680 | 15.8978 | 0.0672 | 16.8872 | IAE | 0.5660 | 0.4702 | 16.9229 | 0.4701 | 16.9405 | ISE | 0.0789 | 0.0523 | 33.6934 | 0.0522 | 33.8202 | Max(dev) | 0.3792 | 0.3005 | 20.7626 | 0.2970 | 21.6855 | Std(dev) | 0.1062 | 0.0864 | 18.6057 | 0.0864 | 18.6057 |
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