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Turbulent-flow burners

To summarize the major advantages and disadvantages of the nonpremix and premix burners, the advantages of the turbulent-flow burner are ... [Pg.270]

Thus, several factors are involved in the choice of a burner. Generally speaking, a premix burner is preferred for atomic-absorption work, except when a high-burning-velocity flame must be used. Turbulent-flow burners are widely used for atomic-emission measurements, but in recent years premix burners have also found more use, particularly with the high-temperature nitrous oxide-acetylene flame. [Pg.271]

FIGURE 9-4. The Beckman total-consumption turbulent-flow burner—aspirator. [Courtesy Beckman Instruments.] 1. Solution capillary 2. aspirating gas inlet 3. fuel gas inlet 4. centering screw 5. gas inlet and jacket 6. jacket. [Pg.216]

The total-consumption burner can be adjusted to produce a fuel-rich or oxidant-rich environment very easily since danger of an explosion is very low. All the nebulized sample enters the flame however, droplet size is quite variable and some droplets pass through the flame without complete evaporation and dissociation into atoms. The flame, because of its turbulence and high velocity, will entrain air surrounding the flame, which may react with sample elements and other constituents in the flame. Some use of sheathed turbulent flow burners has been made. The flame is surrounded by a sheath of inert gas to prevent entrainment of air into the flame. Such flames are said to provide greater flame stability and higher flame temperatures than unsheathed flames. [Pg.262]

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]

Laminar-flow burners produce a relatively quiet flame and a long path length for maximizing absorp-tioi>. These properties tend to enhance sensitivity and reproclucibility in AAS. The mixing chamber in this type of burner contains a potentially explosive mixture that can flash hack if the flow rates are too low. Note that the laminar-flow burner in Figure 9-5 is equipped with pressure relief vents for this reason. Other types of laminar-flow burners and turbulent-flow burners are available for atomic emission spectrometry and AFS. [Pg.652]

Pulverized fuel coal burners (typically turbulent air burners, vertical burners, or nozzle burners) receive hot primary air containing the PF and introduce the mixture to secondary air in such a way that it provides a stable flame. The flow rates of both primary and secondary air are controlled by dampers. An ignitor is required to initiate combustion, and the flame front is maintained close to the burner, with the heat of combustion used to ignite incoming PF. A flame safety device electronically scans the flame and initiates corrective action if required. [Pg.83]

Instantaneous schlieren photographs of turbulent Bunsen burner flames at P = 0.1 MPa (left) and P = l.OMPa (right). The flow at U = 2.0m/s is made turbulent, thanks to a perforated plate with hole diameter d = 2.0mm. The burner exit diameter is 20mm. (Reprinted from Frank, J.H., Kalt, P.A., and Bilger, R.W., Combust. Flame, 116, 220, 1999. With permission. Figure 9, p. 238, copyright Elsevier editions.)... [Pg.149]

Flagan, R. C. and J. P. Appleton (1974). A stochastic model of turbulent mixing with chemical reaction Nitric oxide formation in a plug-flow burner. Combustion and Flame 23, 249-267. [Pg.412]

R.C. Flagan and J.P. Appleton. A Stochastic Model of Turbulent Mixing with Chemical Reaction Nitric Oxide Formation in a Plug Flow Burner. Combust. Flame, 23 249,1974. [Pg.821]

Qb (for blow-off). For gradients less than gf, for example, line 1, the burning velocity is somewhere greater than the flow velocity, so the flame will flash back for gradients greater than g6, for example, line 2, the flow velocity is everywhere greater than the burning velocity, so the flame must blow off. Stability data for both laminar and turbulent flow may be correlated by gf and gb this is reasonable because in either case there is a laminar sublayer at the burner wall (23). [Pg.180]

Flow systems in use may be classified as heated laminar tubes, or plug flow tube reactors, (PFTR) and burners, or heated turbulent flow reactors and well-stirred reactors, or continuous stirred-tank reactors, (CSTR). [Pg.563]

Instrument detection limits (IDLs) for most metals by FIAA are in the low-ppm realm in contrast to graphite furnace AA (GFAA). The conventional premixed chamber-type nebulizer burner is common. The sample is drawn up through the capillary by the decreased pressure created by the expanding oxidant gas at the end of the capillary, and a spray of fine droplets is formed. The droplets are turbulently mixed with additional oxidant and fuel and pass into the burner head and the flame. Large droplets deposit and pass down the drain 85-90% of the sample is discarded in this way. Figures 10-15 in Ref. 2 (pp. 216-218) provides a good schematic of the laminar flow burner. [Pg.535]

FIGURE 9-5. Jarrell-Ash burner for flame emission (turbulent flow). [Courtesy Jarrell-Ash Division, Fisher Scientific Co.]... [Pg.216]

Turbulent-flow total-consumption burners were the standard for flame emission spectroscopy for a number of years. In spite of certain deficiencies, they also can serve as sample cells for atomic fluorescence. The most common types of total-consumption burners include a built-in sample aspirator system. Figures 9-4 and 9-5 show their general constructional features. Winefordner and Staab (see footnote 2) used this type of burner for their early studies on analytical atomic fluorescence. [Pg.307]

Turbulence. Turbulence is important to achieve efficient mixing of the waste, oxygen, and heat. Effective turbulence is achieved by Hquid atomization (in Hquid injection incinerators), soHds agitation, gas velocity, physical configuration of the reactor interior (baffles, mixing chambers), and cyclonic flow (by design and location of waste and fuel burners). [Pg.168]

Laminar Versus Turbulent Flames. Premixed and diffusion flames can be either laminar or turbulent gaseous flames. Laminar flames are those in which the gas flow is well behaved in the sense that the flow is unchanging in time at a given point (steady) and smooth without sudden disturbances. Laminar flow is often associated with slow flow from small diameter tubular burners. Turbulent flames are associated with highly time dependent flow patterns, often random, and are often associated with high velocity flows from large diameter tubular burners. Either type of flow—laminar or turbulent—can occur with both premixed and diffusion flames. [Pg.271]

The knowledge of turbulent premixed flames has improved from this very simple level by following the progress made in experimental and numerical techniques as well as theoretical methods. Much employed in early research, the laboratory Bunsen burners are characterized by relatively low turbulence levels with flow properties that are not constant everywhere in the flame. To alleviate these restrictions, Karpov et al. [5] pioneered as early as in 1959 the studies of turbulent premixed flames initiated by a spark in a more intense turbulence, produced in a fan-stirred quasi-spherical vessel. Other experiments carried out among others by Talantov and his coworkers allowed to determine the so-called turbulent flame speed in a channel of square cross-section with significant levels of turbulence [6]. [Pg.138]


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See also in sourсe #XX -- [ Pg.269 ]




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