Abstract

It was investigated the technological process of changing the raw material for the production of technical carbon. The expediency of developing a new control system is analyzed. The mathematical model proce-su is developed.The volume of carbon black production in the world does not increase since 2010. Moreover, it will help to increase the quality of help and quality of money in the market.The optimal formulation should be as economically profitable as possible, that is, to choose the highest yield of technical carbon per unit of raw materials. This formulation is currently determined in the laboratory by conducting a series of studies on components. Automated recipe management system does not exist at this time. Since the production of TV raw materials is a combination of many hydrocarbons and all of them are combined with products of the petrochemical or coke industry, through which their composition can fluctuate on a single user, raises questions about the optimal formulation of raw materials for each supplier. To do this, you need to develop a mathematical model that will allow you to predict the review of the process and synthesize optimal control algorithms.In this paper, the actual scientific and practical problem of modeling the static and dynamic regime of the raw material process for the production of technical carbon is considered. The current development was introduced, as well as the possible use of the paths, namely, the synthesis of optimal management of raw recipe management, which can be used to optimize the recipes. This development will allow to optimize the types of use of available resources to increase the productivity of technical carbon production and reduce the number of production units. It improves economic efficiency and reduces the speed of costs, reducing financial costs and giving the opportunity to quasilifting human resources to solve other pressing problems. Transition processes have been built, aimed at the implementation of different models. They attest to the transient process of the first-order links.Because of the significant nonlinearity and dependence, each other influences one another from the proposed automatic system of optimal control of the linearization of the object. For the convenience of further practical use, it is proposed to attract optimal controls at different meanings of the initial rates for further approximation. This will allow the proposed algorithms to be used with fewer technical resources.

Highlights

  • Для цього необхідно розробити математичну модель що дозволить прогнозувати перебіг процесу і синтезувати алгоритми оптимального керування

  • Це дозволяє побудувати статичну характеристику по єдиному каналу «концентрації компонентів – індекс кореляції сировини» для цього випадку

  • You need to develop a mathematical model that will allow you to predict the review of the process and synthesize optimal control algorithms

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Summary

Introduction

Для цього необхідно розробити математичну модель що дозволить прогнозувати перебіг процесу і синтезувати алгоритми оптимального керування. Метою роботи є розробка математичної моделі процесу змішування сировини для виробництва технічного вуглецю. Це необхідно для синтезу алгоритмів оптимального керування рецептурою сировини, котрі дозволять збільшити ефективність підприємств з виготовлення технічного вуглецю і направити кваліфіковані людські ресурси на вирішення інших актуальних проблем [4]. Можна виразити масові витрати G1, G2, G3 через масові концентрації компонентів у сировині та G.

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