Combustion and Heat Transfer Dynamics in a Premixed Laminar Flat-flame Burner

Author(s):  
Ludwig Haber ◽  
David Losh ◽  
Uri Vandsburger ◽  
William Baumann ◽  
William Saunders
1993 ◽  
Vol 92 (1-3) ◽  
pp. 201-207 ◽  
Author(s):  
L. P. H. de GOEY ◽  
A. van MAAREN ◽  
R. M. QUAX

Author(s):  
Jorge Luis Rentería Peláez ◽  
Luis Fernando Cardona Sepulveda ◽  
Bernardo Argemiro Herrera Múnera

In this work, a numerical analysis was performed about the effect of a flat-flame burner incidence degree on the heat transfer of an industrial scale frit melting furnace, which uses a flat-flame natural gas oxy-combustion burner. The thermal performance of the furnace was evaluated by predicting the temperature distributions, the recirculation of the combustion gases, and the heat flow to the load, using three different geometrical configurations, differing in the inclination of the burner at 0°, 3.5°, 7° with respect to the longitudinal axis. The simulations were carried out using the ANSYS® Fluent software. The Steady Laminar Flamelet (SFM) model, the k-epsilon realizable model, and the discrete ordinates model were used to model combustion, turbulence, and radiation, respectively. The weighted model of the sum of gray gases (WSGGM) was used for the coefficient of absorption of the combustion species. It was observed that the furnace temperature estimated with the simulations is similar to that found in the actual process. Additionally, the simulations showed that for the angle of 7°, the flame collides with the frit, which could generate deposition of frit particles in the internal walls of the furnace; this would affect the emissivity of the refractory material. The 3.5degree angle showed a better distribution of heat flow to the frit and recirculation rate compared to the burner at 0° and 7°.


2010 ◽  
Vol 49 (4) ◽  
pp. 783-795 ◽  
Author(s):  
Takayuki Fuyuto ◽  
Helmut Kronemayer ◽  
Burkhard Lewerich ◽  
Jan Brübach ◽  
Taketoshi Fujikawa ◽  
...  

2013 ◽  
Vol 27 (2) ◽  
pp. 942-953 ◽  
Author(s):  
Aaron D. Lewis ◽  
Thomas H. Fletcher
Keyword(s):  

2019 ◽  
Vol 37 (3) ◽  
pp. 2705-2713 ◽  
Author(s):  
Xuebin Wang ◽  
Adewale Adeosun ◽  
Zhongfa Hu ◽  
Zhenghang Xiao ◽  
Dishant Khatri ◽  
...  

2013 ◽  
Vol 27 (6) ◽  
pp. 3022-3038 ◽  
Author(s):  
Randy C. Shurtz ◽  
Thomas H. Fletcher
Keyword(s):  

2016 ◽  
Vol 31 (3) ◽  
pp. 2228-2235 ◽  
Author(s):  
Yang Xu ◽  
Shuiqing Li ◽  
Ye Yuan ◽  
Qiang Yao

Measurements of the burning velocities of methane, ethane, propane, butane, ethylene, carbon monoxide and cyanogen mixtures with air, in the range about 4 to 8 cm, are made by the flat-flame burner method with an accuracy of 2 to 3%. The results can be represented by a straight-line relationship between composition and burning velocity except for carbon monoxide which is sensitive to the percentage of water vapour present. Extrapolated values agree well with recent measurements of faster flames. Measurements are also made on binary mixtures with air of the gases, including hydrogen. The mixture law holds except with mixtures containing carbon monoxide. Limits of inflammability are also determined and the burning velocities at the limits average 3⋅6 cm/s. The mixtures obey the Le Chatelier rule accurately, except for carbon monoxide mixtures. The burning velocities of the hydrocarbons can be represented approximately by a straight-line relationship with the heat generated and with the maximum flame temperature, but correlation is best when thermal conductivity is introduced. At a given velocity the excess energy maintained by the flame appears to be constant for all the hydrocarbons investigated, except methane, which behaves slightly differently. The burning velocities of the hydrocarbons are controlled by a reaction which provides reasonable values of the activation energies and probably precedes the sudden development of chain branching.


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