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Premix burner system

Because of the high combustion velocity the flame cannot be burned on a premix burner system. [Pg.20]

Figure 6.8 (a) Premix burner system. [Courtesy of PerkinElmer Inc., Shelton, CT (www. [Pg.394]

Figure 6.8 (a) Premix burner system. [ 1993-2014 PerkinElmer, Inc. All rights reserved. Printed with permission, (www.perkinelmer.com).] (b) Schematic nebulizer designs. (Top), modified Babington type (left), concentric (the most common in FAAS) (right) cross-flow type. (From Parsons, M.L., Atomic absorption and flame emission, in Ewing, G.A., ed.. Analytical Instrumentation Handbook, 2nd edn., Marcel Dekker, Inc., New York, 1997. Used with permission.)... [Pg.450]

Van Oijen, J.A., Lammers, F.A., de Goey, L.P.H. Modeling of complex premixed burner systems by using flamelet-generated manifolds. Combust. Flame 127, 2124-2134 (2001)... [Pg.310]

It is often desired to substitute directiy a more readily available fuel for the gas for which a premixed burner or torch and its associated feed system were designed. Satisfactory behavior with respect to dashback, blowoff, and heating capabiHty, or the local enthalpy dux to the work, generally requires reproduction as neady as possible of the maximum temperature and velocity of the burned gas, and of the shape or height of the dame cone. Often this must be done precisely, and with no changes in orifices or adjustments in the feed system. [Pg.524]

Figure 4.1.2 is a photograph of a coimterflow burner assembly. The experimental particle paths in this cold, nonreacting, counterflow stagnation flow can be visualized by the illumination of a laser sheet. The flow is seeded by submicron droplets of a silicone fluid (poly-dimethylsiloxane) with a viscosity of 50 centistokes and density of 970 kg/m, produced by a nebulizer. The well-defined stagnation-point flow is quite evident. A direct photograph of the coimterflow, premixed, twin flames established in this burner system is shown in Figure 4.1.3. It can be observed that despite the edge effects. Figure 4.1.2 is a photograph of a coimterflow burner assembly. The experimental particle paths in this cold, nonreacting, counterflow stagnation flow can be visualized by the illumination of a laser sheet. The flow is seeded by submicron droplets of a silicone fluid (poly-dimethylsiloxane) with a viscosity of 50 centistokes and density of 970 kg/m, produced by a nebulizer. The well-defined stagnation-point flow is quite evident. A direct photograph of the coimterflow, premixed, twin flames established in this burner system is shown in Figure 4.1.3. It can be observed that despite the edge effects.
In fuel-lean premixed burners, the primary air ratio determines the quality of combustion changing the rotational speed of the flue gas fan has also some influence. An ionization probe is used to determine the quality of combustion. A dedicated system, developed at GWI, provides accurate detection and analysis of the ionization signal. This includes a metering device, which is provided with a rectangular supply voltage, thus warranting very accurate ionization signals. [Pg.47]

Prompt NO mechanisms In dealing with the presentation of prompt NO mechanisms, much can be learned by considering the historical development of the concept of prompt NO. With the development of the Zeldovich mechanism, many investigators followed the concept that in premixed flame systems, NO would form only in the post-flame or burned gas zone. Thus, it was thought possible to experimentally determine thermal NO formation rates and, from these rates, to find the rate constant of Eq. (8.49) by measurement of the NO concentration profiles in the post-flame zone. Such measurements can be performed readily on flat flame burners. Of course, in order to make these determinations, it is necessary to know the O atom concentrations. Since hydrocarbon-air flames were always considered, the nitrogen concentration was always in large excess. As discussed in the preceding subsection, the O atom concentration was taken as the equilibrium concentration at the flame temperature and all other reactions were assumed very fast compared to the Zeldovich mechanism. [Pg.423]

Bluff-body flame stabilization in nonpremixed and partially premixed gaseous systems is complicated by the mixing of fuel and oxidizer. In addition to the aspects considered above, it is necessary to control the fuel distribution in the burner. [Pg.185]

Schematic diagram of a concentric nebulizer system for a premixed burner. Schematic diagram of a concentric nebulizer system for a premixed burner.
A flame spectrometric detection (FSD) system was used to study a variety of metal chelates including the UO(tfac)2, Cr(tfac)3, Cr(hfac)3, Al(tfac)3, Cu(tfac)2, Fe(hfac)2, Cu(hfac)2, Co(hfac)2 and tricarbonylchromium complexes. The GC column was connected by a heated stainless steel line to a flame spectrometer, working in a laminar flow regime with a N2O-C2H2 premix burner that could be heated without distortion of the flame, and a monochromator provided the selective response required for the FSD. The system included a splitter to allow simultaneous FID and FSD chromatograms . ... [Pg.701]

In these burners gas flow depends on the underpressure created in a venturi system by the air flow. Fuel and air control is not good and a high excess of air is required. The 6% of CO2 contents means that less than double air compared to stechiometric condition is required. Figure 34.8 gives a rough indication of CO and NO, level reached with this technology. Atmospheric burners are premixed burners because air and fuel are mixed before burning, but "premixed burners" for... [Pg.709]

Heated Chamber Burner. One approach, which is now being offered commercially, is a burner in which the mixing chamber is heated to a temperature between 300 and 500°C. by infrared radiation. After introduction, the sample is converted into a vapor. It then passes into a cooling chamber, where the steam is condensed and allowed to flow out of a drain tube. In the ideal case, only the solid components of the sample are passed into the burner head. The heated chamber system overcomes the previously noted factor that standard premix burners are only 5% to 10% eflScient. By being able to use all of the sample that had been introduced, the heated chamber burner can produce ten to twenty times higher absorption for a given concentration. [Pg.206]

To carry out the analysis in the best manner possible, a study was conducted on the various hollow cathode lamps, burners, and optical systems to assess them as to their advantages and disadvantages in the analysis of water. Particular emphasis was given to the comparison of the total consumption and premix burners (6, 7). The results are presented here in the form of conservative values attainable of sensitivity and precision, and a discussion of the differences noted. [Pg.237]

Figure 10.9. Premix nebulizer-burner system. Adapted from G. D. Christian andF. J. Feldman, Atomic Absorption Spectroscopy Applications in Agriculture, Biology, and Medicine, New York Wiley-Inter-science, 1970, p 80, by permission of John Wiley and Sons. Figure 10.9. Premix nebulizer-burner system. Adapted from G. D. Christian andF. J. Feldman, Atomic Absorption Spectroscopy Applications in Agriculture, Biology, and Medicine, New York Wiley-Inter-science, 1970, p 80, by permission of John Wiley and Sons.
Figure 33 Premix burner (Unicam Analytical Systems Ltd.)... Figure 33 Premix burner (Unicam Analytical Systems Ltd.)...
Flashback is more likely with an acetylene-oxygen mixture than with any of the other fuel-oxidant combinations in common use. Flame propagation in this system is at 1130cm/sec. This imposes severe limitations on the use of acetylene and oxygen with premixed burners. The relatively low flame propagation rate of nitrous oxide and acetylene (180cm/sec) is a definite advantage for the system. [Pg.268]

The laminar flow premixed flame systems are characterized by their reduced noise and light scattering properties as compared with turbulent flow burners. A choice of fuel-oxidant combinations also is available for... [Pg.307]

Scattered radiation interference is greater with a total-consumption burner than with premixed systems. Larger and more nonuniform droplet sizes are observed with total-consumption burner systems. The area of observation in a flame also is a factor in scattered radiation interference. Figure 11-3 illustrates this effect. Scattering is greater in both turbulent... [Pg.311]

Modem premixing burners function differently. The fuel gas and oxygen/air are mixed in an upstream section. This gas mixture is then delivered directly to the burner, which has just one inlet Combustion takes place immediately once the mixture has passed the joint nozzle system. [Pg.102]

A flame trap is employed where premixed air and gas is used in combustion equipment and prevents the flame passing upstream into the pipe system. Flame traps should be situated as near as possible to the gas burner. This is so that the flame does not have a long pipe mn in which it might accelerate to such a speed as to form a detonation wave and make the trap useless. [Pg.282]

Much of the discussion of oxygen flame calorimetry presented in section 7.3 is directly applicable to fluorine flame calorimetry. As in the case of bomb calorimetry, however, the special properties of fluorine combustion systems and problems associated with handling fluorine require a somewhat different experimental method [109,115,116]. Thus, for example, a metal burner should be used. Also, the fact that the mixing of many gases with F2 may lead to spontaneous ignition hinders the use of a premixed flame. Fluorine combustion calorimetry has been used to study the thermochemistry of important reactions, such as... [Pg.123]


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See also in sourсe #XX -- [ Pg.16 , Pg.17 ]




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