Premixing experiments

This section is arranged as follows First, premixed combustion is discussed based on the experiments performed under controlled conditions. To establish these conditions the experiments were conducted in explosion vessels, balloons, plastic bags, and soap bubbles. Second, some experiments under uncontrolled conditions... 

Elsworth et al. (1983) report experiments performed in an open-topped channel 52 m long x 5 m high whose width was variable from 1 to 3 m. Experiments were performed with propane, both premixed as vapor and after a realistic spill of liquid within the channel. In some of the premixed combustion tests, baffles 1-2 m high were inserted into the bottom of the channel. Ignition of the propane-air mixtures revealed typical flame speeds of 4 m/s for the spill tests, and maximum flame speeds of 12.3 m/s in the premixed combustion tests. Pressure transducers recorded strong oscillations, but no quasi-static ovetpressure. 

This expression was checked in many early experiments on premixed flames with a fixed equivalence ratio. Light... 

Dunn-Rankin, D. and Sawyer, R.R, Tulip flames Changes in shape of premixed flames propagating in closed tubes. Experiments in Fluids, 24,130-140,1998. 

Samaniego, J.M. and Mantel, T, Fundamental mechanisms in premixed turbulent flame propagation via flame-vortex interactions Part I Experiment, Combust. Flame, 118, 537, 1999. 

The creation of a steady flame hole was previously carried out by Fiou et al. [36]. In their experiments, a steady-annular premixed edge flame was formed by diluting the inner mixture below the flammability limit, for both methane/air and propane/air mixtures. They found that a stable flame hole was established when the outer mixture composition was near stoichiometry. Their focus, however, was on the premixed flame interaction, rather than on the edge-flame formation, extinction, or propagation. 

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]. 

Nevertheless, despite all these remarkable achievements, some open questions still remain. Among them is the influence of the molecular transport properties, in particular Lewis number effects, on the structure of turbulent premixed flames. Additional work is also needed to quantify the flame-generated turbulence phenomena and its relationship with the Darrieus-Landau instability. Another question is what are exactly the conditions for turbulent scalar transport to occur in a coimter-gradient mode Finally, is it realistic to expect that a turbulent premixed flame reaches an asymptotic steady-state of propagation, and if so, is it possible, in the future, to devise an experiment demonstrating it ... 

In Chapfer 7.2, J.H. Frank and R.S. Barlow describe the basic characteristics of non-premixed flames wifh an emphasis on fundamenfal phenomena relevant to predictive modeling. They show how the development of predictive models for complex combustion systems can be accelerated by combining closely coupled experiments and numerical simulations. 

A polymer of the polyacrylamide type was injected as a 0.5% solution from an axially-placed nozzle at the bellmouth entrance. The experiments showed that the central thread provided drag reduction almost equivalent to premixed solutions of the same total polymer concentration flowing in the pipe. Overall concentrations of 1, 2, 4, and 20 ppm were used. Moreover, the effects were additive 2 ppm thread overall concentration plus 2 ppm premixed gave drag reductions equivalent to 4 ppm of either type. Reynolds numbers of up to 300,000 were investigated. In other experiments, a number of different polymer fluids were injected on the centerline of a water pipe-flow facility [857]. Two distinct flow regions were identified ... 

Quasiliving Polymerization of IBVE in CHzClz at -70° and -90°C. IBVE was polymerized by introducing the monomer slowly and continuously into a premixed -DCC/AgSbF6 charge in CH2Cl2 at -70 or -90°C. In all experiments polymer yields at any time... 

The first step to verify the feasibility of this was to do experiments to see if the level of emulsifier El has an effect on the droplet size obtained during the emulsification. Figure 4 shows the effect of the level of El added to the premix vessel on the average droplet size of the emulsion after homogenization. The relative droplet size shown in Figure 4 are relative to the droplet size obtained in the reference (100% El). Figure 4 clearly shows that up to about 25% El there... 

This seemingly simple series of events does not address all the requirements. If the device is preparing media does that mean it prepares a buffer to be diluted or only degasses the premixed media When media is dispensed, is there a need to perform a preliminary dispense to assure removal of the previous media If samples are to be read on-line is dilution required prior to reading Systems intended for method development (MD) will have many different requirements than one intended for QA. The value of the automation to the user may be very different for each of these two areas. In fact the MD user may not appreciate the need to automate more than one run at a time and will prefer a semiautomated system, since the MD user may have many different experiments to perform that may be labor intensive. Just a few... 

There were many early experimental investigations of bluff-body stabilization. Most of this work [69] used premixed gaseous fuel-air systems and typically plotted the blowoff velocity as a function of the air-fuel ratio for various stabilized sizes, as shown in Fig. 4.56. Early attempts to correlate the data appeared to indicate that the dimensional dependence of blowoff velocity was different for different bluff-body shapes. Later, it was shown that the Reynolds number range was different for different experiments and that a simple independent dimensional dependence did not exist. Furthermore, the state of turbulence, the temperature of the stabilizer, incoming mixture temperature, etc., also had secondary effects. All these facts suggest that fluid mechanics plays a significant role in the process. 

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