Full Text:   <3704>

CLC number: TK124

On-line Access: 2012-11-29

Received: 2012-07-04

Revision Accepted: 2012-10-25

Crosschecked: 2012-11-16

Cited: 1

Clicked: 4957

Citations:  Bibtex RefMan EndNote GB/T7714

-   Go to

Article info.
1. Reference List
Open peer comments

Journal of Zhejiang University SCIENCE A 2012 Vol.13 No.12 P.969-978

http://doi.org/10.1631/jzus.A1200168


Method for determining effective flame emissivity in a rotary kiln incinerator burning solid waste


Author(s):  Jin-cai Du, Qun-xing Huang, Jian-hua Yan

Affiliation(s):  State Key Laboratory of Clean Energy Utilization, Zhejiang University, Hangzhou 310027, China; more

Corresponding email(s):   hqx@zju.edu.cn

Key Words:  Thermographic temperature measurement, Effective flame emissivity, Rotary kiln incinerator, Air/waste equivalence ratio


Share this article to: More <<< Previous Article|

Jin-cai Du, Qun-xing Huang, Jian-hua Yan. Method for determining effective flame emissivity in a rotary kiln incinerator burning solid waste[J]. Journal of Zhejiang University Science A, 2012, 13(12): 969-978.

@article{title="Method for determining effective flame emissivity in a rotary kiln incinerator burning solid waste",
author="Jin-cai Du, Qun-xing Huang, Jian-hua Yan",
journal="Journal of Zhejiang University Science A",
volume="13",
number="12",
pages="969-978",
year="2012",
publisher="Zhejiang University Press & Springer",
doi="10.1631/jzus.A1200168"
}

%0 Journal Article
%T Method for determining effective flame emissivity in a rotary kiln incinerator burning solid waste
%A Jin-cai Du
%A Qun-xing Huang
%A Jian-hua Yan
%J Journal of Zhejiang University SCIENCE A
%V 13
%N 12
%P 969-978
%@ 1673-565X
%D 2012
%I Zhejiang University Press & Springer
%DOI 10.1631/jzus.A1200168

TY - JOUR
T1 - Method for determining effective flame emissivity in a rotary kiln incinerator burning solid waste
A1 - Jin-cai Du
A1 - Qun-xing Huang
A1 - Jian-hua Yan
J0 - Journal of Zhejiang University Science A
VL - 13
IS - 12
SP - 969
EP - 978
%@ 1673-565X
Y1 - 2012
PB - Zhejiang University Press & Springer
ER -
DOI - 10.1631/jzus.A1200168


Abstract: 
Temperature is the most important parameter for the improvement of combustion efficiency and the control of pollutants. In order to obtain accurate flame temperatures in a rotary kiln incinerator using non-intrusive thermographic method, the effective flame emissivity was studied. A combined narrow- and wide-band model and Mie scattering method were used to calculate the radiative properties for gases and fly-ash particles under different combustion conditions. The effects of the air/waste ratio and fly-ash particles on the effective flame emissivity were discussed. The results of numerical calculations showed that the effective emissivity decreased from 0.90 to 0.80 when the air/waste ratio increased from 1.0 to 1.8, and the effect of the fly-ash particles was ignorable under the conditions discussed in this paper. Experimental measurement results indicated that the accuracy of the thermographic temperature measurements improved significantly if the setting of the flame emissivity was adjusted according to the air/waste ratio.

Darkslateblue:Affiliate; Royal Blue:Author; Turquoise:Article

Reference

[1]Águeda, A., Pastor, E., Pérez, Y., Planas, E., 2010. Experimental study of the emissivity of flames resulting from the combustion of forest fuels. International Journal of Thermal Sciences, 49(3):543-554.

[2]Ballester, J., Garcia-Armingol, T., 2010. Diagnostic techniques for the monitoring and control of practical flames. Progress in Energy and Combustion Science, 36(4):375-411.

[3]Bohren, C.F., Huffman, D.R., 1983. Absorption and Scattering of Light by Small Particles. John Wiley & Sons, New York, p.128.

[4]Buekens, A., Huang, H., 1998. Comparative evaluation of techniques for controlling the formation and emission of chlorinated dioxins/furans in municipal waste incineration. Journal of Hazardous Materials, 62(1):1-33.

[5]Chang, F.C., Rhodes, C.A., 1995. Computer Modeling of Radiation and Combustion in a Rotary Solid-Waste Incinerator. Argonne National Lab, US Department of Energy Report ANL/ET/CP-85778.

[6]Docquier, N., Candel, S., 2002. Combustion control and sensors: a review. Progress in Energy and Combustion Science, 28(2):107-150.

[7]Edwards, D.K., 1962. Radiation interchanges in a non-gray enclosure containing an isothermal carbon dioxide and nitrogen gas mixture. Journal of Heat Transfer, 84(1):1-11.

[8]Edwards, D.K., Balakrishnan, A., 1973. Thermal radiation by combustion gases. International Journal of Heat and Mass Transfer, 16(1):25-40.

[9]GB 18484-2001, 2005. Pollution Control Standard for Hazardous Waste Incineration. Ministry of Environmental Protection and General Administration of Quality Supervision, Inspection and Quarantine of the People’s Republic of China. China Environmental Press, Beijing.

[10]Gohlke, O., Busch, M., 2001. Reduction of combustion by-products in WTE plants: O2 enrichment of under fire air in the Martin Syncom process. Chemosphere, 42: 545-550.

[11]Grosshandler, W.L., 1980. Radiative heat transfer in inhomogeneous gases: A simplified approach. International Journal of Heat and Mass Transfer, 23(11):1447-1459.

[12]HJ/T176-2005. Technical Specifications for Centralized Incineration Facility Construction on Hazardous Waste. Ministry of Environmental Protection of the People’s Republic of China. China Environmental Press, Beijing.

[13]Law, C.K., 2006. Combustion Physics. Cambridge University Press, New York, p.31-49.

[14]Li, W., Tong, T.W., 1995. A combined narrow- and wide-band model for computing the spectral absorption coefficient of CO2, CO, H2O, CH4, C2H2, and NO. Journal of Quantitative Spectroscopy and Radiative Transfer, 54(6):961-970.

[15]Manca, D., Rovaglio, M., 2002. Infrared thermographic image processing for the operation and control of heterogeneous combustion chambers. Combustion and Flame, 130: 277-297.

[16]Modest, M.F., 1991. The weighted-sum-of-gray-gases model for arbitrary solution methods in radiative transfer. Journal of Heat Transfer, 113(3):650-656.

[17]Modest, M.F., 2003a. Radiative Heat Transfer. McGraw Hill, New York, p.288-357.

[18]Modest, M.F., 2003b. Radiative Heat Transfer (2nd Ed.). Academic, New York, p.287-410.

[19]China Statistical Yearbook on Environment, 2009. National Bureau of Statistics and Ministry of Environmental Protection of the People’s Republic of China. China Statistics Press, Beijing.

[20]Ni, Y.W., Zhang, H.J., Fan, S., Zhang, X.P., Zhang, Q., Chen, J.P., 2009. Emissions of PCDD/Fs from solid waste incinerators in China. Chemosphere, 75(9):1153-1158.

[21]Parent, G., Acem, Z., Lechêne, S., Boulet, P., 2010. Measurement of infrared radiation emitted by the flame of a vegetation fire. International Journal of Thermal Sciences, 49(3):555-562.

[22]Planas-Cuchi, E., Chatris, J.M., López, C., Arnaldos, J., 2003. Determination of flame emissivity in hydrocarbon pool fires using infrared thermography. Fire Technology, 39(3):261-273.

[23]Rothman, L.S., Gordon, I.E., Barber, R.J., Dothe, H., Gamache, R.R., Goldman, A., Perevalov, V., Tashkun, S.A., Tennyson, J., 2010. HITEMP, the high-temperature molecular spectroscopic database. Journal of Quantitative Spectroscopy and Radiative Transfer, 111(15):2139-2150.

[24]Subramanya, M., Choudhuri, A.R., 2004. Operating Point Control of Combustion Processes Using Dynamic Flame Tracking. 2nd International Energy Conversion Engineering Conference, AIAA, p.5523.

[25]Sudheer, S., Prabhu, S.V., 2010. Measurement of flame emissivity of gasoline pool fires. Nuclear Engineering and Design, 240(10):3474-3480.

[26]Vosteen, B., Beyer, J., Bonkhofer, T., 2002. Simultaneous inner and outer thermography of rotary kilns for hazardous waste incineration. VGB PowerTech, 9:71-77.

Open peer comments: Debate/Discuss/Question/Opinion

<1>

Please provide your name, email address and a comment





Journal of Zhejiang University-SCIENCE, 38 Zheda Road, Hangzhou 310027, China
Tel: +86-571-87952783; E-mail: cjzhang@zju.edu.cn
Copyright © 2000 - 2024 Journal of Zhejiang University-SCIENCE