Kinetic Effects of Toluene Blending on n-Decane Diffusion Flame Extinction Limit

Author(s):  
Sang Hee Won ◽  
Wenting Sun ◽  
Yiguang Ju
2012 ◽  
Vol 159 (1) ◽  
pp. 221-229 ◽  
Author(s):  
Wenting Sun ◽  
Mruthunjaya Uddi ◽  
Sang Hee Won ◽  
Timothy Ombrello ◽  
Campbell Carter ◽  
...  

2011 ◽  
Vol 33 (1) ◽  
pp. 1163-1170 ◽  
Author(s):  
Sang Hee Won ◽  
Stephen Dooley ◽  
Frederick L. Dryer ◽  
Yiguang Ju

1991 ◽  
Vol 86 (1-2) ◽  
pp. 171-178 ◽  
Author(s):  
Takashi Niioka ◽  
Susumu Hasegawa ◽  
Tatsuro Tsukamoto ◽  
Jun'ichi Sato

Author(s):  
Douglas L. Straub ◽  
Jimmy D. Thornton ◽  
Geo. A. Richards ◽  
Doug Simmers ◽  
Pavel Shuk ◽  
...  

State-of-the-art gas turbines engines continuously strive for higher cycle efficiencies and lower pollutant emissions. The gas turbine combustor is critical for achieving these goals, and operation near the lean extinction limit is necessary. Slight changes in the flow splits (fuel and/or air) can lead to unexpected flame extinction, or other operational issues such as combustion oscillations. Operating these gas turbine combustors near the flame extinction limit could be improved if acceptable in-situ sensors for the combustion section were commercially available. Although exhaust gas oxygen sensors are commonly used in other combustion processes including large utility boilers and automobiles, the use of in-situ oxygen sensors in gas turbine engines has been limited. This paper will describe the results from rig tests in a pressurized lean premixed combustor. The O2 sensor technology used in these tests is commercially available for industrial boiler applications which typically operate near atmospheric pressure and oxygen levels that range from 0–3% of the effluent. In modern gas turbines, however, the amount of excess oxygen is considerably higher. These high levels of excess oxygen result in low level signals from the O2 sensor, which creates concern for in-situ monitoring in gas turbines. The results indicate that this sensor technology will operate at elevated pressure and at high levels of excess oxygen in the process gas suggesting possible application as an operational and diagnostic tool. Data will be presented to show the effects of different operating variables such as pressure, inlet-air temperature, heat-release, and fuel-air ratio.


Author(s):  
Baolu Shi ◽  
Tatsuya Kowari ◽  
Daisuke Shimokuri ◽  
Satoru Ishizuka

Methane/oxygen-air combustion has been attempted by using a rapidly mixed type tubular flame burner with four slits, from two of which a fuel is injected and from another two an oxidizer is injected. The oxygen concentration (molar) in the oxygen-air oxidizer has been varied from 21% (air) to 100% (pure oxygen). Results show that uniform tubular flame combustion can be obtained for a wide range of equivalence ratios, if the oxygen molar concentration in the oxygen-air oxidizer is less than about 50%. Above 50%, however, very intense turbulent combustion occurs frequently and the circular-shaped tubular flame is deformed as oval-shaped for most equivalence ratios. The uniform tubular flame range is reduced and quite limited in the vicinity of lean condition. Detailed observations show that for pure (or near pure) oxygen oxidizer, two diffusion flames are established between the fuel and oxidizer streams at the exits of the fuel slits, which prevents fuel from mixing with oxygen, resulting in a violent turbulent combustion downstream the slits. With use of a burner with smaller slit width, however, formation of the diffusion flame is inhibited and a uniform tubular flame can be established, although still limited close to the lean extinction limit. To fully understand the flame characteristics above, the burning velocities are calculated for various equivalence ratios as well as for various oxygen concentrations in the oxygen-air oxidizer using the CHEMKIN PREMIX code with the GRI kinetic mechanism.


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