ISSN: 0256-1115 (print version) ISSN: 1975-7220 (electronic version)
Copyright © 2024 KICHE. All rights reserved

Articles & Issues

Language
English
Conflict of Interest
In relation to this article, we declare that there is no conflict of interest.
Publication history
Received December 27, 2004
Accepted April 1, 2005
articles This is an Open-Access article distributed under the terms of the Creative Commons Attribution Non-Commercial License (http://creativecommons.org/licenses/bync/3.0) which permits unrestricted non-commercial use, distribution, and reproduction in any medium, provided the original work is properly cited.
Copyright © KIChE. All rights reserved.

All issues

Pyrolysis Kinetics and Characteristics of the Mixtures of Waste Ship Lubricating Oil and Waste Fishing Rope

Department of Environmental Engineering, Samcheok National University, Gangwon-do 245-711, Korea 1Department of Environmental Engineering, School of Engineering, Dong Hae University, 119 Jiheung-dong, DongHae, Gangwon-do 240-713, Korea 2Enviart Co., Ltd, 129 Songhyun-dong, Dong-gu, Incheon 401-040, Korea 3Department of Chemical Engineering, Kongju National University, Kongju, Chungnam 314-701, Korea
ks7070@dreamwiz.com
Korean Journal of Chemical Engineering, July 2005, 22(4), 573-578(6), 10.1007/BF02706646
downloadDownload PDF

Abstract

Kinetic investigations on the pyrolysis of a mixture of waste ship lubricating oil (WSLO) and waste fishing rope (WFR) were carried out using a thermogravimetric analyzer (TGA) at a heating rate of 0.5 ℃/min, 1.0 ℃/min and 2.0 ℃/min. WSLO and WFR were mainly decomposed at the temperature of range of 400 ℃ to 455 ℃ and 370 ℃ to 410 ℃, respectively. The WSLO/WFR mixture was mainly decomposed at the temperature range of 300 ℃ and 450 ℃, which is a lower temperature than that for the WSLO or the WFR alone at each heating rate. The ranges of apparent activation energies of the WALO/WFR mixture were between 137 kJ mol.1 and 197 kJ mol.1 at conversions in the range of 10-95%. The mixture of WSLO and WFR was pyrolyzed in a micro-scale tubing reactor at 440 ℃ for 60 min and 80 min. The yield of pyrolyzed gases increased from 2.13 wt% to 2.29 wt% with reaction time. The selectivity to C7 hydrocarbons was shown in the pyrolyzed oil of the mixture.

References

Ballice L, Fuel, 81, 1233 (2002) 
Bockhom H, Homugn A, Homung U, J. Anal. Appl. Pyrolysis, 46, 1 (1998) 
Bockhom H, Homung A, Homung U, Schalwaller D, J. Anal. Appl. Pyrolysis, 48, 93 (1999) 
Ceamanos J, Mastral JF, Millera A, Aldea ME, J. Anal. Appl. Pyrolysis, 65, 93 (2002) 
Choi DH, " A Study on the Practical Effect for the Acting of Protection Policy of Marine Environmental", Korea Maritime Institute, 5-56 (2001)
Friedman HL, J. Polym. Sci. : Part C., 6, 183 (1963)
Holland BJ, Hay JN, Polym. Int., 49, 943 (2000) 
Jha A, Bhowmick AK, Polym. Degrad. Stabil., 62, 575 (1998) 
Kim S, Chun HD, Korean J. Chem. Eng., 12(4), 448 (1995)
Kim SD, Park SY, J. Korean Solid Wastes Engineering, 18, 397 (2001)
Kim SD, Jun JG, Yoo KS, J. Korean Solid Wastes Engineering, 18, 410 (2001)
Kim SS, Kim SH, Fuel, 79, 1943 (2000) 
Kim SS, Chung YJ, J. Korean Ind. Eng. Chem., 14(6), 793 (2003)
Kim SS, Kim S, Chem. Eng. J., 98(1-2), 53 (2004) 
Kim SS, Jeon JK, J. Korean Ind. Eng. Chem., 15(5), 564 (2004)
Kim SS, Jeon JK, J. Ind. Eng. Chem., Submitted (2004)
Kim YS, Hwang GC, Bae SY, Yi SC, Korean J. Chem. Eng., 16(2), 161 (1999)
Korea Lubricating Oil Industries Association Bulletin (2002)
Lee CG, Kim JS, Song PS, Choi GS, Kang Y, Choi MJ, Korean J. Chem. Eng., 20(1), 133 (2003)
Park JJ, Park K, Park JW, Kim DC, Korean J. Chem. Eng., 19(4), 658 (2002)

The Korean Institute of Chemical Engineers. F5, 119, Anam-ro, Seongbuk-gu, 233 Spring Street Seoul 02856, South Korea.
TEL. No. +82-2-458-3078FAX No. +82-507-804-0669E-mail : kiche@kiche.or.kr

Copyright (C) KICHE.all rights reserved.

- Korean Journal of Chemical Engineering 상단으로