Direct estimation of edge flame speeds of lifted laminar jet flames and a modified stabilization mechanism
Introduction
In 1965, Phillips first observed an interesting flame structure within a stratified methane-air mixing layer [1]. It had three flame branches: a lean premixed flame, a rich premixed flame, and a diffusion (or non-premixed) flame in the downstream. The propagation speed of this flame was much faster than the laminar burning velocity (LBV) of a stoichiometric mixture, and it increased as the thickness of the mixing layer grew. Almost two decades later, Ishikawa [2] observed similar unsteady flame structures in an experiment on ignition within a stratified fuel–air mixing layer. Dold [3] explained that these flame structures play key roles not only in stabilizing the lifted flames but also in the turbulent flame's propagation. This flame structure was later variously called a triple flame, a tribrachial flame, or an edge flame.
A representative study of the phenomenon using a laminar fuel jet from a small-scale contraction nozzle (with an inner diameter of 0.164, 0.195, or 0.247 mm) was conducted by Chung and Lee in 1991 [4]. The stabilization mechanism of the lifted flames was explained using the similarity between two equations for the velocity and the fuel concentration. They described the stabilization mechanism using the Schmidt number, which is defined as the ratio of kinematic viscosity to mass diffusivity, Sc ≡ ν/D, and insisted that the lifted flames could be theoretically stabilized when Sc > 1 or Sc < 0.5. A number of experimental studies showed that stable liftoff flames existed when Sc > 1. However, the other stabilization condition of Sc < 0.5 was not observed experimentally. In practice, hydrogen flames could not be stabilized as a lifted flame, and the excessive mass diffusion at the nozzle exit was suspected to be the main reason [4]. Nevertheless, it was questionable why this practical instability corresponding to Sc < 0.5 could not be explained theoretically.
In further investigation, the relationship between the fuel concentration gradient (FCG or ∂YF/∂r) and the edge flame speed (EFS or Sedge), denoted hereafter as the EFS/FCG relationship, has been of particular interest. Because the FCG is a main parameter that governs the edge flame's curvature and scalar dissipation rate, the EFS/FCG relationship has been pursued in studies on combustion dynamics and turbulent flames. Although Phillips had reported a similar trend [1], a direct EFS/FCG relationship was first explored by Kioni et al. in 1993 [5]. They used a system consisting of a multi-slot part and a diverging channel connected at the downstream. They measured the flow rate, fuel concentration, and flame location in the diverging channel. The EFS was defined as the average flow velocity of the cold flow at the location of the flame front. The EFS was much faster than the LBV of the stoichiometric mixture, but the EFS/FCG relationship was not clear. Ruetsch et al. [6] analytically explained that the EFS was faster than the LBV mainly due to the flow re-direction in the upstream of the flame. Thus, the EFS would reach its maximum at the smallest FCG, as follows:
Here is the LBV of an un-stretched stoichiometric flame, and ρu/ρb is the density ratio of the unburned to burned mixtures.
Various experimental cases were explored by the Chung's research group, including the effects of fuel-dilution [7] and air-premixing [8] on the liftoff heights. In a detailed study on flame stabilization by Lee and Chung [9], it was shown that the flow velocity in the upstream of the lifted flame was larger than . In addition, a representative result of the EFS/FCG relationship was obtained by Ko and Chung [10] for unstable methane flames (Sc < 1). They used a fuel tube (di= 2.08 mm) relatively larger than those used in the previous studies [4], [7], [8], [9]. Using a high-speed camera, they recorded unsteady flame propagation to the tube tip after ignition at the downstream with a high-power laser. The relative flame speed to the theoretical cold flow velocity was defined as the EFS, and the FCG was estimated partly from the experimental results. Using this data, the EFS/FCG relationship was derived for methane flames, and it was shown that EFS decreases monotonically with the increase in FCG.
The EFS/FCG relationship hidden within the stable lifted flame was partly extracted through a numerical study conducted by Chen and Bilger [11]. The non-reactive flow velocity and species concentration were solved numerically for the same conditions of the previous experiment [4] regarding the stable lifted propane–air flames. Using the local flow velocity at the liftoff height, some results comparable to the EFS/FCG relationship could be extracted. However, it was a formidable task to determine the various EFS/FCG relationships using this method, because every experimental condition required an additional respective numerical simulation.
A few years later, the same method used in the previous study for methane [10] was applied to measure the EFS/FCG relationships for propane flames [12]; i.e., the unsteady flame propagation after ignition was recorded using a high-speed camera, and the EFS was estimated at the conditions of lower flow rates. It is notable that lifted flames could also be stabilized at higher flow rates because a small tube diameter (di= 0.254 mm) was used in that study. The structures of lifted stable flames were investigated at higher flow rates independently [13]. Nevertheless, unstable propagating flames at lower flow rates were used to measure the EFS [12]. A similar experiment was conducted again to investigate the effects of velocity gradient, and improved experimental results for the EFS/FCG relationship was reported [14]. Later, some of those results will be compared with the results from this study. A number of studies have been conducted to investigate lifted flames, and they have been summarized in review papers [15], [16].
In addition to the small jet experiments, the EFS/FCG relationships were directly measured for methane and propane flames using an improved multi-slot-burner with a contraction nozzle; i.e., in an open space [17], within a diverging channel [18], and with fuel dilution [19]. It was shown that the EFS has a turning point at a small critical FCG, and this was proposed to be the criterion that distinguished a premixed edge flame from an ordinary diffusion edge flame. When the FCG was larger than the critical value, an ordinary trend was obtained, and the EFS decreased as the FCG grew. Some results from the open space study [17] will be compared with the results of this study. However, the burner used in [17], [18], [19] was not suitable for producing a larger FCG, which might be more important in turbulent combustion studies.
To construct abundant database and knowledge related to the structures of edge flames, an efficient method is needed that can extract the EFS/FCG relationship from various stable lifted flames. In addition, an analytical explanation is also necessary to address why the theoretical stabilization condition of Sc < 0.5 could not be observed in practical experiments. In this study, therefore, the connections between experimental results and similarity solutions were investigated. 1) The liftoff heights of propane flames were measured again with a higher order of resolution for various parameters including the tube diameter, air-premixing ratio, and nitrogen-dilution ratio. 2) The analytic method was improved so that the EFS/FCG relationship could be extracted from the similarity solution just by using the simple experimental values for the flow rates and liftoff heights. 3) A unique stabilization criterion for a lifted laminar jet flame, Sc > 1, was derived theoretically, and the ambiguous criterion of Sc < 0.5 could be eliminated.
Section snippets
Experimental methods
A schematic of the experimental setup, which is similar to those used in previous studies, is shown in Fig. 1. Three fuel-tubes were used, after polishing their end-tips. The outer diameters were measured with a micrometer gauge and the inner diameters were estimated from the relative scales in the microscopic images. The inner/outer diameters (di/do) of the three tubes were 0.224/0.416 mm (tube-1), 0.317/0.515 mm (tube-2), and 0.466/0.716 mm (tube-3).
Pure propane (>99.5%), propane/air
Classical similarity solutions
It is known that the stream wise velocity, u, and the fuel mass fraction, YF, of a laminar jet flow can be determined from their similarity solutions as follows [4]:
In this study, the velocity profile index of zero (i= 0) was used for a fully developed parabolic flow (meanwhile, i= 1 for a uniform flow). YF, e is the fuel mass fraction at the tube exit, R is the tube inner radius, ν is the kinematic viscosity, and the similarity
Sensitivity of the edge flame speed
Because the value of the EFS was complicated by various parameters, the sensitivity of each parameter was numerically examined, as shown in Fig. 9. When any influential parameter, ψ, was increased by 10%, the relative variation in the EFS was defined as the sensitivity, sens (ψ), and then was evaluated as follows:
For each parameter, sensitivities were compared for three different FCG values, marked as (i), (ii), and (iii) in Fig. 6.
Conclusions
In this study, previous analytic theories on lifted flames were improved. The edge flame speed (EFS) was directly estimated from the simple experimental relation between flow rate and liftoff height. It was shown that the simplified classic theory could not explain the relationship between the EFS and the fuel concentration gradient (FCG). Because the relation between EFS and FCG is one of the most important characteristics for the flame stabilization mechanism of lifted flames, a new analytic
Acknowledgment
This work was supported by a Research Grant from KAIST under the title “Study of flame structures under conditions of high temperature and MILD combustion”, and was partly supported by the BK21-plus program.
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