TY - CONF
T1 - Micro-explosion and burning characteristics of a single droplet of pyrolytic castor oil
AU - Chen, G. B.
AU - Li, Y. H.
AU - Lan, C. H.
AU - Li, J. W.
AU - Chao, Y. C.
N1 - Funding Information:
This research was supported by the National Science Council of the Republic of China under the grant number NSC 101-3113-P-468-001. References [1] Agblevor, F. A., Besler, S. and Wiselogel, A. E., Fast Pyrolysis of Stored Biomass Feedstocks, Energy and Fuels, 9 pp. 635-40, 1995. [2] Li, Feng Juan, Chang Lu Wang, Dong He, Ya Qiong Liu, Mian Hua Chen, Yu Rong Wang, Feng Juan Li, Zhao Hui Yang & Grace Chen, Evaluation of Genetic Diversity in Castor (Ricinus Communis L.) Using Rapd Markes, Advanced Materials Research, 343-344 pp. 981-87, 2011. [3] Lima, Rosiane L. S., Liv S. Severino, Ligia R. Sampaio, Valdinei Sofiatti, Jucélia A. Gomes & Napoleão E. M. Beltrão, Blends of Castor Meal and Castor Husks for Optimized Use as Organic Fertilizer, Industrial Crops and Products, 33 (2) pp. 364-68, 2011. [4] Guan-Lin Chen ,Guan-Bang Chen,Yueh-Heng Li and Wen-Ting Wu, “A Study of Thermal Pyrolysis for Castor Meal using Taguchi Method,” Energy Volume 71, 2014, Pages 62-70. [5] Cantrell, K., Ro, K., Mahajan, D., Anjom, M. and Hun, P. G., Role of Thermochemical Conversion in Live-stock Waste-to-Energy Treatments: Obstacles and Opportunities, Ind. Eng. Chem. Res., 46 pp. 8918-27, 2007. [6] Bridgwater, A. V., Review of Fast Pyrolysis of Biomass and Product Upgrading, Biomass and Bioenergy, 38 pp. 68-94, 2012. [7] Spalding, D. l., The Combustion of Liquid Fuels, Fuel, 32 pp. 169-185, 1953. [8] Law, C. K., Combustion Physics, New York: Cambridge University Press, 2006. [9] Wardana, I. N. G., Combustion Characteristics of Jatropha Oil Droplet at Various Oil Temperatures, Fuel, 89 pp. 659-664, 2010. [10] Scholza, V. and Silvab, J. N. D., Prospects and risks of the use of castor oil as a fuel, BIOMASS AND BI-OENERGY, 32 pp. 95-100, 2008.
Publisher Copyright:
© 2015 International Conference on Liquid Atomization and Spray Systems. All rights reserved.
PY - 2015
Y1 - 2015
N2 - In the study, castor oil is produced by thermal pyrolysis and its pyrolysis reaction and oxidation reactions are investigated using thermal gravimetric analysis. The results showed that the main pyrolysis and oxidation reactions occur in the temperature between 100 and 500 °C. The maximum weight loss occurs between 100 and 320 °C. Its non-volatile components may be ignited at about 500 °C and the residue is only about 0.18% of the original weight of the pyrolytic oil. The suspended droplet experimental system is also used to explore the micro-explosion phenomena and combustion modes of castor pyrolytic oil under different ambient temperatures (350 °C, 450 °C and 550 °C). The pyrolytic oil of castor seeds is a multi-component fuel and therefore has a wide boiling range. It results in a complex process during the heating process and the micro-explosion occurs, causing the droplet surface distortion. According to the timing and strength of the micro-explosion, there are three different stages: low intensity micro-explosion in the first stage, high intensity micro-explosion in the second stage and medium intensity micro-explosion in the last stage. After strong micro-explosion occurred in 550 °C ambient temperature, it will release more volatile vapor and the flammable mixture will form a non-premixed flame wrapping droplets after it is ignited in high temperature environments. During the combustion process of the droplet, the micro-explosion occurs continuously, but the droplet still maintains the appearance close to a sphere. The droplet rapidly evaporates and the flame wraps the droplet. In the latter period of the droplet combustion, volatile components have been completely evaporated, the residual solid particle will continue burning, and there is almost no residue after burning.
AB - In the study, castor oil is produced by thermal pyrolysis and its pyrolysis reaction and oxidation reactions are investigated using thermal gravimetric analysis. The results showed that the main pyrolysis and oxidation reactions occur in the temperature between 100 and 500 °C. The maximum weight loss occurs between 100 and 320 °C. Its non-volatile components may be ignited at about 500 °C and the residue is only about 0.18% of the original weight of the pyrolytic oil. The suspended droplet experimental system is also used to explore the micro-explosion phenomena and combustion modes of castor pyrolytic oil under different ambient temperatures (350 °C, 450 °C and 550 °C). The pyrolytic oil of castor seeds is a multi-component fuel and therefore has a wide boiling range. It results in a complex process during the heating process and the micro-explosion occurs, causing the droplet surface distortion. According to the timing and strength of the micro-explosion, there are three different stages: low intensity micro-explosion in the first stage, high intensity micro-explosion in the second stage and medium intensity micro-explosion in the last stage. After strong micro-explosion occurred in 550 °C ambient temperature, it will release more volatile vapor and the flammable mixture will form a non-premixed flame wrapping droplets after it is ignited in high temperature environments. During the combustion process of the droplet, the micro-explosion occurs continuously, but the droplet still maintains the appearance close to a sphere. The droplet rapidly evaporates and the flame wraps the droplet. In the latter period of the droplet combustion, volatile components have been completely evaporated, the residual solid particle will continue burning, and there is almost no residue after burning.
UR - http://www.scopus.com/inward/record.url?scp=85091998714&partnerID=8YFLogxK
UR - http://www.scopus.com/inward/citedby.url?scp=85091998714&partnerID=8YFLogxK
M3 - Paper
AN - SCOPUS:85091998714
T2 - 13th International Conference on Liquid Atomization and Spray Systems, ICLASS 2015
Y2 - 23 August 2015 through 27 August 2015
ER -