REAL TIME STEAM TEMPERATURE REGULATION USING SELF-TUNING FUZZY PID CONTROLLER ON HYDRO-DIFFUSION ESSENTIAL OIL EXTRACTION SYSTEM

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International Journal on Smart Sensing and Intelligent Systems

Professor Subhas Chandra Mukhopadhyay

Exeley Inc. (New York)

Subject: Computational Science & Engineering, Engineering, Electrical & Electronic

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VOLUME 6 , ISSUE 5 (December 2013) > List of articles

REAL TIME STEAM TEMPERATURE REGULATION USING SELF-TUNING FUZZY PID CONTROLLER ON HYDRO-DIFFUSION ESSENTIAL OIL EXTRACTION SYSTEM

Zakiah Mohd Yusoff * / Zuraida Muhammad / Mohd Hezri Fazalul Rahiman / Mohd Nasir Taib

Keywords : distillation, essential oil, hydro-diffusion system, self-tuning fuzzy PID

Citation Information : International Journal on Smart Sensing and Intelligent Systems. Volume 6, Issue 5, Pages 2,055-2,074, DOI: https://doi.org/10.21307/ijssis-2017-626

License : (CC BY-NC-ND 4.0)

Received Date : 11-August-2013 / Accepted: 16-November-2013 / Published Online: 16-December-2013

ARTICLE

ABSTRACT

The essential oil is mostly depends on the temperature. The temperature will influence the final product of the extraction process. The existing steam distillation processes are giving less intention on this issue. This work implemented the robust self-tuning fuzzy PID (STFPID) controller to monitor the steam temperature in the hydro-diffusion essential oil extraction system. The hydro-diffusion system is built to overcome some weakness of existing systems. The effectiveness of the STFPID using 25 rules and PID controller is measured by using performance indices of settling time, rise time, percentage overshoot (%OS) and root mean square error. The step responses analysis and robustness test show that STFPID and PID controller are able to drive the steam temperature to the desired set point However, the analysis shows that STFPID produces better performances based on set point tracking and adoption of load disturbance.

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REFERENCES

[1] F. Chemat, M. E. Lucchesi, J. Smadja, L. Favretto, G. Colnaghi, and F. Visinoni, "Microwave accelerated steam distillation of essential oil from lavender: A rapid, clean and environmentally friendly approach," Analytica Chimica Acta, vol. 555, pp. 157–160, 2006.
[2] J. M. Roldan-Gutierrez, J. Ruiz-Jimenez, and M. D. L. d. Castro, "Ultrasound-assisted dynamic extraction of valuable compounds from aromatic plants and flowers as compared with steam distillation and superheated liquid extraction," Talanta, vol. 75, pp. 1369–1375, 2008.
[3] A. Donelian, L. H. C. Carlsonb, T. J. Lopesa, and R. A. F. Machado, "Comparison of extraction of patchouli (Pogostemon cablin) essential oil with supercritical CO2 and by steam distillation," The Journal of Supercritical Fluids, vol. 48, pp. 15–20, 2009.
[4] M. Khajeh, Y. Yaminib, and S. Shariati, "Comparison of essential oils compositions of Nepeta persica obtained by supercritical carbon dioxide extraction and steam distillation methods," Food and Bioproducts Processing, vol. 88, pp. 227–232, 2010.
[5] M. E. Lucchesi, F. Chemat, and J. Smadja, "Solvent-free microwave extraction of essential oil from aromatic herbs: comparison with conventional hydro-distillation," Journal of Chromatography A, vol. 1043, pp. 323–327, 2004.
[6] E. L. Galvão, H. B. d. Sant’Ana, H. N. M. Oliveira, A.V.Souza, and E. M. B. D. Sousa, "Influence of Temperature in the Kinetics Extraction of the Cymbopogon Winterianus j. oil with Dense Carbon Dioxide," 2nd Mercosur Congress on Chemical Engineering, 4th Mercosur Congress on Process Systems Engineering.
[7] S. Sayyar, Z. Z. Abidin, R. Yunus, and A. Muhammad, "Extraction of Oil from Jatropha Seeds-Optimization and Kinetics," American Journal of Applied Sciences, vol. 6, pp. 1390-1395, 2009.
[8] N. Bousbia, M. A. Vian, M. A.Ferhat, E. Petitcolas, B. Y.Meklati, and F. Chemat, "Comparison of two isolation methods for essential oil from rosemary leaves:Hydrodistillation and microwave hydrodiffusion and gravity," Journal of Food Chemistry, vol. 114, pp. 355-362, 2009.
[9] E. S. Giray, S. Kirici, D. A. Kaya, M. Turk, O. Sonmez, and M. Inan, "Comparing the effect of sub-critical water extraction with conventional extractipn methods on the chemical composition of Lavandula stoechas," Talanta, vol. 74, pp. 930-935, 2008.
[10] A.Arce, A.Pobudkowska, O.Rodriguez, and A.Soto, "Citrus essential oil terpenless by extraction using 1-ethyl-3-methylimidazolium ethylsulfate ionic liquid: Effect of temperature," Chemical Engineering Journal, vol. 133, pp. 213-218, 2007.
[11] S. Chanthaphon, S. Chanthachum, and T. Hongpattarakere, "Antimicrobial activities of essential oils and crude extracts from tropical Citrus spp. against food-related microorganisms," Songklanakarin Journal of Science and Technology, vol. 30, pp. 125-131, 2008.
[12] G. Wenqiang, L. Shufen, Y. Ruixiang, T. Shaokun, and Q. Can, "Comparison of essential oils of clove buds extracted with supercritical carbon dioxide and other three traditional extraction methods," Food Chemistry, vol. 101, pp. 1558–1564, 2007.
[13] H. Ebrahimzadeh, Y. Yamini, F. Sefidkon, M. Chaloosi, and S. M. Pourmortazavi, "Chemical composition of the essential oil and supercritical CO2 extracts of Zataria multiflora Boiss," Food Chemistry, vol. 83, pp. 357–361, 2003.
[14] R. Adnan, M. Tajjudin, N. Ishak, H. Ismail, M. H. F. Rahiman, and N. M. Arshad, "Comparison between self-tuning Fuzzy-PID and Pole-Placement PID with application to saturated steam temperature regulation," International Conference on System Engineering and Technology (ICSET),, pp. 1-5, 11-12 Sept. 2012.
[15] M. Z. Ozel and H. Kaymaz, "Superheated water extraction, steam distillation and Soxhlet extraction of essential oils of Origanum onites," Analytical and bioanalytical chemistry vol. 379, pp. 1127-1133, 2004.
[16] C. Deng, X. Xu, N. Yao, N. Li, and X. Zhang, "Rapid determination of essential oil compounds in Artemisia Selengensis Turcz by gas chromatography-mass spectrometry with microwave distillation and simultaneous solid-phase microextraction," Analytica Chimica Acta, vol. 556, pp. 289-294, 2006.
[17] G. Song, C. Deng, D. Wu, and Y. Hu, "Comparison of Headspace Solid-Phase Microextraction with Solvent Extraction for the Analysis of the Volatile Constituents of Leaf Twigs of Chinese Arborvitae " Chromotographia vol. 59, pp. 769-774, 2003.
[18] N. A. Mohamed, "Study on Important Parameters Affecting the Hydrodistillation for Ginger Oil Production," 2005.
[19] E. Cassel, R. M. F. Vargas, N. Martinez, D. Lorenzo, and E. Dellacassa, "Steam distillation modeling for essential oil extraction process," Industrial Crops and Products, vol. 29, pp. 171–176, 2009.
[20] N. C. Nikolic, S. M. Cakic, S. M. Novakovi, M. D. Cvetkovic, and M. Z. Stankovic, "Effect of Extraction Techniques on Yield and Composition of Soybean Oil," Macedonian Journal of Chemistry and Chemical Engineering vol. 28, pp. 173-179, 2009.
[21] C. C. Lee, "Fuzzy Logic in Control Systems: Fuzzy Logic Controller-Part I," IEEE Transactions On Systems, vol. 20, pp. 404-418, 1990.
[22] S. G. Cao, N. W. Rees, and G. Feng, "Analysis and Design for a Class of Complex Control Systems Part II: Fuzzy Controller Design," Automatica, vol. 33, pp. 1029-1039, 1997.
[23] Z. Xiaodong, X. Senlin, and Z. Hongbo, "A New Strategy for Batch Reactor's Temperature Control," WRI World Congress on Computer Science and Information Engineering, vol. 5, pp. 56-61, 2009.
[24] N. N. Mohammad, N. Kasuan, M. H. F. Rahiman, and M. N. Taib, "Steam Temperature Control Using Fuzzy Logic for Steam Distillation Essential Oil Extraction Process," IEEE Control and System Graduate Research Colloquium, pp. 53-58, 2011.
[25] Zulfatman and M. F. Rahmat, "Application of self-tuning fuzzy PID controller on industrial hydraulic actuator using system identification approach," International Journal on Smart Sensing and Intelligent Systems, vol. 2, pp. 246-261, 2009.
[26] N. B. Kha and A. Kyoung-Kwan, "Position Control of Shape Memory Alloy Actuators by Using Self Tuning Fuzzy PID Controller," 1ST IEEE Conference on Industrial Electronics and Applications, , pp. 1-5, 2006.
[27] G. Zhiqiang, T. A. Trautzsch, and J. G. Dawson, "A stable self-tuning fuzzy logic control system for industrial temperature regulation," IEEE Transactions on Industry Applications, vol. 38, pp. 414-424, 2002.
[28] P. Isomursu and T. Rauma, "A self-tuning fuzzy logic controller for temperature control of superheated steam," IEEE World Congress on Computational Intelligence., Proceedings of the Third IEEE Conference on Fuzzy Systems, vol. 3, pp. 1560-1563 1994.
[29] K. Sinthipsomboon, I. Hunsacharoonroj, J. Khedari, W. Pongaen, and P. Pratumsuwan, "A hybrid of fuzzy and fuzzy self-tuning PID controller for servo electro-hydraulic system," Industrial Electronics and Applications (ICIEA), 2011 6th IEEE Conference on, pp. 220-225, 21-23 June 2011.
[30] W. H. Bare, R. J. Mulholland, and S. S. Sofer, "Design of a self-tuning rule based controller for a gasoline refinery catalytic reformer," IEEE Transactions on Automatic Control, vol. 35, pp. 156-164, 1990.
[31] T. Ching-Chih and L. Chi-Huang, "Multivariable self-tuning temperature control for plastic injection molding process," IEEE Transactions on Industry Applications, vol. 34, pp. 310-318, 1998.
[32] W. C. Daugherity, B. Rathakrishnan, and J. Yen, "Performance evaluation of a self-tuning fuzzy controller," IEEE International Conference on Fuzzy Systems, pp. 389-397, 1992.
[33] F. Peng, L. Sheng, B. Liu, H. Tong, and S. Liu, "Comparison of different extraction methods: steam distillation, simultaneous distillation and extraction and headspace co-distillation, used for the analysis of the volatile components in aged flue-cured tobacco leaves," Journal of Chromatography A, vol. 1040, pp. 1–17, 2004.
[34] P. Masango, "Cleaner production of essential oils by steam distillation," Journal of Cleaner Production, vol. 13, pp. 833-839, 2005.
[35] T. Hagglund, "An industrial dead-time compensating PI controller," Control Engineering Practice, vol. 4, pp. 749-756, 1996.
[36] K. K. Ahn and D. Q. Truong, "Online tuning fuzzy PID controller using robust extended Kalman filter," Jounal of Process Control, vol. 19, pp. 1011-1023, 2009.
[37] N. Kasuan, M. N. Taib, and M. H. F. Rahiman, "Model Reference Adaptive Controller to Regulate Steam Temperature in Distillation Process for Essential Oil Extraction," 7th International Colloquium on Signal Processing and its Applications, pp. 298-303, 2011.
[38] R. K. Mudi and N. R. Pal, "A Robust Self-Tuning Scheme for PI- and PD-Type Fuzzy Controllers," IEEE Transactions On Fuzzy Systems, vol. 7, pp. 2-16, 1999.
[39] T. Ching-Chih and H. Chih-Hung, "Model reference adaptive predictive control for a variable-frequency oil-cooling machine," IEEE Transactions On Industrial Electronics, vol. 51, pp. 330-339, 2004.
[40] J. Flores-Cerrillo and J. F. MacGregor, "Latent variable MPC for trajectory tracking in batch processes," Jounal of Process Control, vol. 15, pp. 651-663, 2005.
 

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