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Fuel-Oxidant Control

Careful adjustment of fuel-to-oxidant ratio, as well as total fuel-oxidant volume, is required for best response of a flame source. Some elements are best determined in a fuel-rich environment and others in a fuel-lean flame. Control of fuels and oxidants normally is made by use of pressure-reducing valves. Two sets of valves are required, one on the tank for pressure reduction, and the other for close control of the volume of gases entering the burner or mixing chamber. Control by pressure-reducing valves is usually sufficient to produce good, steady flames but does not provide close adjustment or monitoring of the quantities of fuel and oxidant consumed. In some cases it may be advisable to install flow meters in the gas supply systems so rates of gas consumption can be monitored and controlled. [Pg.218]

Care needs to be exercised in the use of fuels and oxidants. If compressed air is used, it should be filtered before compression and as it leaves the high-pressure tank. Acetylene requires special care since it is supplied as a solution in acetone under pressure. As the pressure in the tank is reduced, considerable acetone may escape with the acetylene. A glass-wool filter will aid in restricting the flow of acetone into the burner. [Pg.218]

Fuel-gas mixtures also may cause explosions. It is important that manufacturer s recommendations on gas and oxidant flow be followed. [Pg.218]


The counterflow configuration has been extensively utilized to provide benchmark experimental data for the study of stretched flame phenomena and the modeling of turbulent flames through the concept of laminar flamelets. Global flame properties of a fuel/oxidizer mixture obtained using this configuration, such as laminar flame speed and extinction stretch rate, have also been widely used as target responses for the development, validation, and optimization of a detailed reaction mechanism. In particular, extinction stretch rate represents a kinetics-affected phenomenon and characterizes the interaction between a characteristic flame time and a characteristic flow time. Furthermore, the study of extinction phenomena is of fundamental and practical importance in the field of combustion, and is closely related to the areas of safety, fire suppression, and control of combustion processes. [Pg.118]

The burner used for flame AA is a premix burner. It is called that because all the components of the flame (fuel, oxidant, and sample solution) are premixed, as they take a common path to the flame. The fuel and oxidant originate from pressurized sources, such as compressed gas cylinders, and their flow to the burner is controlled at an optimum rate by flow control mechanisms that are part of the overall instrument unit. [Pg.251]

Any refractory material that does not decompose or vaporize can be used for melt spraying. Particles do not coalesce within the spray. The temperature of the particles and the extent to which they melt depend on the flame temperature, which can be controlled by the fuel oxidizer ratio or electrical input, gas flow rate, residence time of the particle in the heat zone, the particle-size distribution of the powders, and the melting point and thermal conductivity of the particle. Quenching rates are very high, and the time required for the molten particle to solidify after impingement is typically 10-4 to... [Pg.45]

In direct aspiration FLAA, a sample in the aerosol form is aspirated into a flame fueled with acetylene. An oxidant (air or nitrous oxide) is mixed with the acetylene fuel to create the necessary temperature conditions. Depending on the fuel/oxidant ratio, the temperature of the flame may range from 2400 to 2800°C. Precise temperature control is critical in FLAA analysis, as the concentrations of ionized and unionized species of a vaporized element are sensitive to the temperature of the flame. [Pg.233]

If nitrogen oxide control is one of the catalytic requirements, the stoichiometry of air-to-fuel ratio must be kept nearly stoichiometric to reduce NO then air must be added and CO and hydrocarbons oxidized in a second part of the catalyst bed. [Pg.97]

Ignition of a fuel-oxidizer mixture occurs when an external source of energy initiates interactions among the controlling convective, transport and chemical processes. Whether the process results in deflagration, detonation, or is simply quenched depends on the intensity, duration, and volume affected by an external heat source. Ignition also will depend on the initial ambient properties of the mixture which determine the chemical induction... [Pg.344]

The use of zeolite-hosted semiconductor oxides as chemicai sensors towards oxidizing or reducing gases might be attractive. Since the alteration of the conductivity depends on changes of the oxide stoichiometry [93,94], shorter diffusion distances in smaller clusters should result in shorter response times of the sensors. Fast response is a prerequisite for the application of sensors based on changes of the bulk composition, e.g. in air/fuel ratio control devices. [Pg.73]

The rate of other fuel oxidation pathways that feed into the TCA cycle is also increased when ATP utilization increases. Insulin, other hormones and diet control the availability of fuels for these oxidative pathways. [Pg.374]

As reported by Avrami and Voreck (Ref 192), the only proplnt in that test was AK-14 Mod I which is a cast, fuel-oxidizer whose compn is 74% K perchlorate, 25% polyester-styrene copolymer (P-lO resin) and 1% carbon black. Two capsules were irradiated at two levels — the lower level at 7.0 x 10 ° n/cm° fast, 2.4 x lO n/cm° thermal and 3 x 10° R gamma, and the higher level at 3.5 x lO n/cm° fast, 1.7 x 10 n/cm° thermal and 1.5 x 10 R gamma — all in a pulse of about one millisecond. The tests conducted on the AK-14 Mod I proplnt did not show any significant changes although the 5-second expln temp results were not consistent with the control and steady-state results... [Pg.85]

As discussed in Section 4.1.2.2, the radionuclide control function which is performed by the upper plenum thermal protection structure is to limit chemical attack on the fuel by limiting fuel oxidation. This structure functions to provide protection to the upper vessel assuring primary coolant boundary reliability and restricting the possibility of air ingress to the core. [Pg.415]

Use a quality air/fuel ratio controller set as close to stoichiometric as practical, but erring on the oxidizing side (because dross is easier to remove than absorbed hydrogen)... [Pg.113]

Oxides of iron, aluminum, copper, zinc, and glass often form on their molten surfaces, becoming inclusions in the final casting, probably causing it to be a reject. It is therefore desirable to minimize excess oxygen in contact with a molten metal bath thus, a quality air/fuel ratio controller can be a major help in controlling product quality. [Pg.270]


See other pages where Fuel-Oxidant Control is mentioned: [Pg.218]    [Pg.218]    [Pg.81]    [Pg.135]    [Pg.147]    [Pg.192]    [Pg.269]    [Pg.2]    [Pg.372]    [Pg.84]    [Pg.301]    [Pg.264]    [Pg.65]    [Pg.254]    [Pg.119]    [Pg.162]    [Pg.468]    [Pg.161]    [Pg.817]    [Pg.33]    [Pg.33]    [Pg.59]    [Pg.300]    [Pg.285]    [Pg.533]    [Pg.414]    [Pg.254]    [Pg.15]    [Pg.16]    [Pg.450]    [Pg.657]    [Pg.365]    [Pg.231]    [Pg.755]    [Pg.756]    [Pg.318]    [Pg.110]    [Pg.270]   


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