Oil recovery from oily-sludge by pyrolysis method

被引:0
|
作者
Quan C. [1 ]
Li A. [1 ]
Gao N. [1 ]
Guo D. [1 ]
机构
[1] School of Environmental Science and Technology, Dalian University of Technology
关键词
Oil recovery; Oily-sludge; Pyrolysis;
D O I
10.3969/j.issn.1001-8719.2010.05.014
中图分类号
学科分类号
摘要
Pyrolysis characteristics of oily-sludge were studied by thermogravimetric(TG) analyzer and tubular furnace reactor. The effects of heating rates on oily-sludge pyrolysis and the effects of final pyrolysis temperature on the product distribution of oily-sludge pyrolysis were investigated. The kinetic parameters of oily-sludge were calculated with the method of Coats-Redfern. The products of oily-sludge pyrolysis were analyzed by elemental analysis, FT-IR and 1H NMR. The results indicated that TG curve of oily-sludge shifted to higher temperature, and its activation energy(E) and pre-exponential factor(A) values were increased with the increase of the heating rates. The optimum final pyrolysis temperature was 823 K, at which the oil yield of oily-sludge pyrolysis reached its maximum value of 40.36%. The recovered oil had the similar chemical composition to diesel oil, which could be reused. The pyrolysis residues of oily-sludge were black powder solid and residual oil content in it was about 0.0662%, meeting the national standard regulation for farm-oriented soil oil content(<0.3%).
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页码:742 / 746
页数:4
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共 10 条
  • [1] Wang Z., Guo Q., Liu X., Et al., Low temperature pyrolysis characteristics of oil sludge under various heating conditions, Energy & Fuels, 21, pp. 957-962, (2007)
  • [2] Shie J.L., Chang C.Y., Lin J.P., Et al., Use of inexpensive additives in pyrolysis of oil sludge, Energy & Fuels, 16, pp. 102-108, (2002)
  • [3] Song W., Liu J., Nie Y., Comparative study of pyrolysis and combustion process of oil sludge by TG-FT IR analysis, Journal of Tsinghua University (Science and Technology), 29, 7, pp. 2063-2067, (2008)
  • [4] Li S., Fang M., Shu L., Et al., Pyrolysis and combustion mechanism of wood with distribution activation energy model, Journal of Combustion Science and Technology, 12, 6, pp. 535-539, (2006)
  • [5] Jaber J.O., Probert S.D., Pyrolysis and gasification kinetics of Jordanian oil-shales, Applied Energy, 63, pp. 269-286, (1999)
  • [6] Quan C., Li A., Luan J., Et al., Study on the pyrolysis features and the kinetic analysis of the printed circuit board wastes, Journal of Safety and Environment, 28, 5, pp. 55-58, (2008)
  • [7] Gao N.J., Li A.M., Li W.J., Research into fine powder and large particle tyre pyrolysis, Waste Management & Research, 27, pp. 242-250, (2009)
  • [8] Wang Z., Fingas M., Developments in the analysis of petroleum hydrocarbons in oils, petroleum products and oil-spill-related environmental samples by gas chromatography, Journal of Chromatography A, 774, pp. 51-78, (1997)
  • [9] Fang Y., Jin X., Mineral composition and occurrence characteristics of polymetallic nodule in the eastern pacific ocean, Oceanologia et Limnologia Sinica, 31, 4, pp. 419-425, (2004)
  • [10] Bandosz T.J., Block K., Effect of pyrolysis temperature and time on catalytic performance of sewage sludge/industrial sludge-based composite adsorbents, Applied Catalysis B: Environmental, 67, pp. 77-85, (2006)