| Abstract: | Conclusions An approach to the construction of an optimum control system for multistage schemes for cleaning-up spinning solutions under conditions of appreciably nonsteadiness of the filtration process has been examined.The control problem has been formulated and the basic stages in its solution have been set forth, based on the results of mathematical modeling of the process and formalizing the decisive links.A standard functional structure of the system of operative control of the filtration division as a subsystem of the ACS TP for man-made fibre plants is given.Program and mathematical assurance for realizing the control system examined have been developed, using computer control technique.Translated from Khimicheskie Volokna, No. 5, pp. 29–32, September–October, 1986. |
