Method of calculation of static regime of rectification columns for optimization of constructive and technological parameters on MathCAD Prime 3.0.

Authors

D.P Muxitdinov, Doctor of Technical Sciences, Professor, Department of Automation of Production Processes, Tashkent State Technical University, Тel.: (+99894)604-23-80 (м.);
Yo.B Kadirov, Senior Lecturer, Department of Automation and Control, Navoi State Mining Institute, Тел.: (+99891)338-29-22 (м.),Follow

Abstract

The calculation of the statics of the rectification process is considered. The method of calculating the material and heat balances in the program MathCAD Prime 3.0 is presented. The proposed method involves calculating the pressure in a column based on the preliminary determination of the temperature of the total condensation of distillate vapors, the complexity of which is due to the nonlinear character of the dependence of the equilibrium constants on temperature. According to the Underwood equations, the minimum and working reflux ratio is calculated in the processes of multicomponent rectification. The theoretical number of plates of the column is calculated and the position of the food plate is determined.

First Page

95

Last Page

108

References

1. D.P.Muhitdinov, “Povy'shenie e`ffektivnosti processov rektifikacii mnogokomponentny'h smesey” [Improving the efficiency of rectification processes for multicomponent mixtures], Diss. dok. tehn. nauk, Tashkent, 2012. (in Russian)

2. N.R.YUsupbekov, D.P.Muhitdinov, SH.M.Gulyamov, “Osnovy' processov razdeleniya mnogokomponentny'h smesey” [Basics of separation processes for multicomponent mixtures], monografiya, Tashkent: «Universitet», 2017, 372 p. (in Russian)

3. V.V.Kafarov, M.B.Glebov, “Matematicheskoe modelirovanie osnovny'h processov himicheskih proizvodstv” [Mathematical modeling of the main processes of chemical production], Moskva: Vy'sshaya shkola, 1991, 400 p. (in Russian)

4. D.P.Muhitdinov, E'.B.Kadirov, D.YU.Abdunazarova, “Razrabotka lineyny'h modeley dinamicheskih ob`ektov upravleniya” [Development of linear models of dynamic control objects], Nauchno-tehnicheskiy jurnal «Razvitie nauki i tehnologiy», no. 1, pp. 135-140, 2018. (in Russian).

5. V.P.D'yakonov, “MathCAD 2000: Uchebny'y kurs” [MathCAD 2000: training course], Izdatel'stvo Piter, 2000, 596 p. (in Russian).

6. E'.B.Kadirov, D.P.Muhitdinov, “Vy'chisleniya skorostey potoka jidkosti i perepada davleniya” [Subtraction of fluid flow rates and differential pressure], Nauchno-prakticheskiy jurnal «Sovremenny'e materialy', tehnika i tehnologii». -YUZGU, no. 5(8), pp. 84-92, 2016.(in Russian).

7. Skogestad, S: "Dynamics and Control of Distillation Columns -A Critical Survey," 3rd IFAC Symp. on Dynamics and Control of Chemical Reactors, Distillation Columns, and Batch Processes, April 26-29, College Park, MD, USA, 1992.

8. Retzbach, B: "Mathematische Modelle von Destillationskolonnen zur Synthese von Regelungskonzepten," Fortschritt-BerichteVDI, Reihe 8: Mess-, Steuerungs- und Regelungstechnik, Nr. 126,VDI Verlag, 1986

9. A.G.Kasatkin “Osnovny'e processy' i apparaty' himicheskoy tehnologii. Uchebnik dlya vuzov. 10-e izd” [Basic processes and devices of chemical technology. Textbook for universities. 10th ed], Moskva: Al'yans, 2004, 753 p. (in Russian)

Recommended Citation

Muxitdinov, D.P and Kadirov, Yo.B (2018) "Method of calculation of static regime of rectification columns for optimization of constructive and technological parameters on MathCAD Prime 3.0.," Chemical Technology, Control and Management: Vol. 2018: Iss. 1, Article 17.
DOI: https://doi.org/10.34920/2018.1-2.95-108