โ Scribed by V. I. Ivanenko; O. A. Khokhel'; E. I. Shor
No coin nor oath required. For personal study only.
๐ SIMILAR VOLUMES
As confirmed by experimental results, a simple mathematical model of a complex oil refining column may be used to determine the controls whieh maximize the production of a specified petroleum product or a group of byproducts. Summary--A brief description of the engineering process of a primary oil
general synthesis problem is defined as that of determining an optimal system structure by extracting it from an enlarged system structure generated by splitting streams into alternative routes. When the optimized splitting ratio is close to 0 or 1, one of the alternative streams can be eliminated t
A simple robust adaptive control is presented for a class of non-linear systems with parameter uncertainty and under bounded disturbances. In the proposed scheme, assuming that a nominal control law, designed with the knowledge of the plant parameters ensures the uniform asymptotic stability of the