Araştırma Makalesi
BibTex RIS Kaynak Göster
Yıl 2022, Cilt: 6 Sayı: 1, 40 - 53, 30.01.2022
https://doi.org/10.31127/tuje.801441

Öz

Kaynakça

  • Ahn S M, Park M J & Rhee H K (1999). Extended Kalman filter–based nonlinear model predictive control for a continuous RIMA polymerization reactor. Ind. Eng. Chem. Res., 38 (10), 3942–3949.
  • Birla A, Singh B, Upadhyay S N & Sharma Y C (2012). Kinetics studies of synthesis of biodiesel from waste frying oil using a heterogeneous catalyst derived from snail shell. Bioresource Technol., 106, 95–100.
  • Chen W T & Xu C X (2001). Adaptive nonlinear control with partial overparameterization. Sys.Cont.Lett., 44, 13–24.
  • Clarke D W, Mohtadi C & Tuffs P S (1987). Generalized predictive control Part I, the basic algorithm. Automatica, 23(2), 137‒148.
  • Clarke D W & Mohtadi C (1989). Pro wrties of Generalized Predictive Control. Automatica, 25, 137–160.
  • Çağatay M T & Karacan S (2018). Simulation and optimization of reactive packed distillation column for biodiesel production using heterogeneous catalyst. International Journal of Energy Applications and Technologies, 5(4), 153–160.
  • DiSerio M, Tesser R, Pengmei L & Santacesaria E (2008). Heterogeneous catalysts for biodiesel production. Energy Fuels, 22, 201–217.
  • Donato A G, Gonçalves J A, Peres J S, Ramos A L S, Ribeiro de Melo Jr A L D C A, Antunes O A C, Furtado N C & Taft C A (2009). The use of acids, niobium oxide, and zeolite catalysts for esterification reactions. J.Phys.Org.Chem, 22, 709–716.
  • Hapoğlu H, Özkan G & Alpbaz M (2000). Optimal temperature control in a batch polymerization reactor using Nonlinear Generalized Predictive Control. Chem. Eng. Commun., 183(1), 155–185.
  • Hapoğlu H (2002). Nonlinear Long-range Predictive Control of an openloop unstable reactor. Computers and Chemical Engineering, 26, 1427–1436.
  • Harmsen G J (2007). Reactive distillation: the frontrunner of industrial process intensification a full review of commercial applications, research, scale–up, design and operation. Chem. Eng. Process, 46, 774–780.
  • Karacan S (2003). Application of a nonlinear long-range predictive control to a packed distillation column. Chem. Eng. and Processing, 42(5), 943–953.
  • Kouzu M, Kasuno T, Tajika M, Sugimoto Y, Yamanaka S & Hidaka J (2008). Calcium oxide as a solid base catalyst for transesterification of soybean oil and its application to biodiesel production. Fuel, 87, 2798–2806.
  • Kulkarni M G & Dalai A K (2006). Waste cooking oil – an economical source for biodiesel: a review. Ind. Eng. Chem. Res., 45, 2901–2913.
  • Martín M & Grossmann I E (2012). Simultaneous optimization and heat integration for biodiesel production from cooking oil and algae. Ind. Eng. Chem. Res, 51, 7998−8014.
  • Özkan G, Hapoğlu H & Alpbaz M (2006). Non–linear Generalised Predictive Control of a jacketed well mixed tank as applied to a batch process—A polymerisation reaction. Applied Thermal Engineering, 26, 720–726.
  • Sharma Y C, Singh B & Upadhyay S N (2008). Advancements in development and characterization of biodiesel. Fuel, 87, 2355–2373.
  • Srivastava A & Prasad R (2000). Triglycerides–based diesel fuels. Renew. Sustainable Energy Rev., 4, 111–133.
  • Vujicic D J, Comic D, Zarubica A, Micic R & Boskovi G (2010). Kinetics of biodiesel synthesis from sunflower oil over CaO heterogeneous catalyst. Fuel, 89, 2054–2061.
  • Zeybek Z, Çetinkaya S, Hapoğlu H & Alpbaz M (2006). Generalized delta rule (GDR) algorithm with generalized predictive control (GPC) for optimum temperature tracking of batch polymerization. Chemical Engineering Science, 61, 6691–6700.
  • Zhang Y, Dube M A, McLean D D & Kates M (2003). Biodiesel production from waste cooking oil: 1. Process design and technological assessment. Bioresource Technology, 89, 1–16.

Multivariable generalized predictive control of reactive distillation column process for biodiesel production

Yıl 2022, Cilt: 6 Sayı: 1, 40 - 53, 30.01.2022
https://doi.org/10.31127/tuje.801441

Öz

Most industrial control systems consist of a significant number of control loops. Generally, large processes are divided into many interconnected subsystems affecting each other, thus creating multivariable systems known as multiple–input multiple–output (MIMO) process. Generalized Predictive Control (GPC) based control algorithm is most suitable for MIMO systems. In this study, multivariate nonlinear (NL) GPC and discrete–time PID control of calcium oxide catalyst–packed reactive distillation (RD) column used for biodiesel production from waste cooking oil were investigated. Temperatures of reaction and reboiler sections were controlled by using non–decoupled and decoupled MIMO NLGPC and discrete–time MIMO PID algorithms. Feed flow rate with constant molar ratio and reboiler heat duty parameters were selected as manipulating variables. All recommended control methods, except for non-decoupled MIMO NLGPC, have been found to perform satisfactorily reference tracking and disturbance rejection in RD column. Consequently, the best control results were obtained in the decoupled MIMO NLGPC.

Kaynakça

  • Ahn S M, Park M J & Rhee H K (1999). Extended Kalman filter–based nonlinear model predictive control for a continuous RIMA polymerization reactor. Ind. Eng. Chem. Res., 38 (10), 3942–3949.
  • Birla A, Singh B, Upadhyay S N & Sharma Y C (2012). Kinetics studies of synthesis of biodiesel from waste frying oil using a heterogeneous catalyst derived from snail shell. Bioresource Technol., 106, 95–100.
  • Chen W T & Xu C X (2001). Adaptive nonlinear control with partial overparameterization. Sys.Cont.Lett., 44, 13–24.
  • Clarke D W, Mohtadi C & Tuffs P S (1987). Generalized predictive control Part I, the basic algorithm. Automatica, 23(2), 137‒148.
  • Clarke D W & Mohtadi C (1989). Pro wrties of Generalized Predictive Control. Automatica, 25, 137–160.
  • Çağatay M T & Karacan S (2018). Simulation and optimization of reactive packed distillation column for biodiesel production using heterogeneous catalyst. International Journal of Energy Applications and Technologies, 5(4), 153–160.
  • DiSerio M, Tesser R, Pengmei L & Santacesaria E (2008). Heterogeneous catalysts for biodiesel production. Energy Fuels, 22, 201–217.
  • Donato A G, Gonçalves J A, Peres J S, Ramos A L S, Ribeiro de Melo Jr A L D C A, Antunes O A C, Furtado N C & Taft C A (2009). The use of acids, niobium oxide, and zeolite catalysts for esterification reactions. J.Phys.Org.Chem, 22, 709–716.
  • Hapoğlu H, Özkan G & Alpbaz M (2000). Optimal temperature control in a batch polymerization reactor using Nonlinear Generalized Predictive Control. Chem. Eng. Commun., 183(1), 155–185.
  • Hapoğlu H (2002). Nonlinear Long-range Predictive Control of an openloop unstable reactor. Computers and Chemical Engineering, 26, 1427–1436.
  • Harmsen G J (2007). Reactive distillation: the frontrunner of industrial process intensification a full review of commercial applications, research, scale–up, design and operation. Chem. Eng. Process, 46, 774–780.
  • Karacan S (2003). Application of a nonlinear long-range predictive control to a packed distillation column. Chem. Eng. and Processing, 42(5), 943–953.
  • Kouzu M, Kasuno T, Tajika M, Sugimoto Y, Yamanaka S & Hidaka J (2008). Calcium oxide as a solid base catalyst for transesterification of soybean oil and its application to biodiesel production. Fuel, 87, 2798–2806.
  • Kulkarni M G & Dalai A K (2006). Waste cooking oil – an economical source for biodiesel: a review. Ind. Eng. Chem. Res., 45, 2901–2913.
  • Martín M & Grossmann I E (2012). Simultaneous optimization and heat integration for biodiesel production from cooking oil and algae. Ind. Eng. Chem. Res, 51, 7998−8014.
  • Özkan G, Hapoğlu H & Alpbaz M (2006). Non–linear Generalised Predictive Control of a jacketed well mixed tank as applied to a batch process—A polymerisation reaction. Applied Thermal Engineering, 26, 720–726.
  • Sharma Y C, Singh B & Upadhyay S N (2008). Advancements in development and characterization of biodiesel. Fuel, 87, 2355–2373.
  • Srivastava A & Prasad R (2000). Triglycerides–based diesel fuels. Renew. Sustainable Energy Rev., 4, 111–133.
  • Vujicic D J, Comic D, Zarubica A, Micic R & Boskovi G (2010). Kinetics of biodiesel synthesis from sunflower oil over CaO heterogeneous catalyst. Fuel, 89, 2054–2061.
  • Zeybek Z, Çetinkaya S, Hapoğlu H & Alpbaz M (2006). Generalized delta rule (GDR) algorithm with generalized predictive control (GPC) for optimum temperature tracking of batch polymerization. Chemical Engineering Science, 61, 6691–6700.
  • Zhang Y, Dube M A, McLean D D & Kates M (2003). Biodiesel production from waste cooking oil: 1. Process design and technological assessment. Bioresource Technology, 89, 1–16.
Toplam 21 adet kaynakça vardır.

Ayrıntılar

Birincil Dil İngilizce
Konular Mühendislik
Bölüm Articles
Yazarlar

Mehmet Çağatay 0000-0002-8625-8058

Suleyman Karacan 0000-0001-8113-7874

Yayımlanma Tarihi 30 Ocak 2022
Yayımlandığı Sayı Yıl 2022 Cilt: 6 Sayı: 1

Kaynak Göster

APA Çağatay, M., & Karacan, S. (2022). Multivariable generalized predictive control of reactive distillation column process for biodiesel production. Turkish Journal of Engineering, 6(1), 40-53. https://doi.org/10.31127/tuje.801441
AMA Çağatay M, Karacan S. Multivariable generalized predictive control of reactive distillation column process for biodiesel production. TUJE. Ocak 2022;6(1):40-53. doi:10.31127/tuje.801441
Chicago Çağatay, Mehmet, ve Suleyman Karacan. “Multivariable Generalized Predictive Control of Reactive Distillation Column Process for Biodiesel Production”. Turkish Journal of Engineering 6, sy. 1 (Ocak 2022): 40-53. https://doi.org/10.31127/tuje.801441.
EndNote Çağatay M, Karacan S (01 Ocak 2022) Multivariable generalized predictive control of reactive distillation column process for biodiesel production. Turkish Journal of Engineering 6 1 40–53.
IEEE M. Çağatay ve S. Karacan, “Multivariable generalized predictive control of reactive distillation column process for biodiesel production”, TUJE, c. 6, sy. 1, ss. 40–53, 2022, doi: 10.31127/tuje.801441.
ISNAD Çağatay, Mehmet - Karacan, Suleyman. “Multivariable Generalized Predictive Control of Reactive Distillation Column Process for Biodiesel Production”. Turkish Journal of Engineering 6/1 (Ocak 2022), 40-53. https://doi.org/10.31127/tuje.801441.
JAMA Çağatay M, Karacan S. Multivariable generalized predictive control of reactive distillation column process for biodiesel production. TUJE. 2022;6:40–53.
MLA Çağatay, Mehmet ve Suleyman Karacan. “Multivariable Generalized Predictive Control of Reactive Distillation Column Process for Biodiesel Production”. Turkish Journal of Engineering, c. 6, sy. 1, 2022, ss. 40-53, doi:10.31127/tuje.801441.
Vancouver Çağatay M, Karacan S. Multivariable generalized predictive control of reactive distillation column process for biodiesel production. TUJE. 2022;6(1):40-53.
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