Droplet streams combustion

Experimental. To further understand the process of droplet combustion and particulate formation, a more fundamental study of the effects of droplet size, local stoichiometry and gas-droplet relative velocity has been carried out. This work made use of a controlled flow variable slip reactor in which the combustion of droplet streams can be examined under well defined conditions. 

In an attempt to modify the observed droplet behavior, a brief qualitative investigation was carried out with blends of SRC-II heavy distillate and pure heptane. The objective was to enhance droplet disruptive combustion as a means of reducing effective droplet size and hence soot formation. With these fuels visible droplet fragmentation was found to occur throughout the droplet stream. The fragmentation produced new droplets on different trajectories these in turn were terminated by small disruptions, as described above. Three blends were used 60/40, 80/20, and 90/10. Secondary atomization was observed for all three, although the violence of the activity was noticeably reduced as the heptane content of the blend became smaller. This secondary atomization was a completely different process than the... 

Convection heat transfer is dependent largely on the relative velocity between the warm gas and the drying surface. Interest in pulse combustion heat sources anticipates that high frequency reversals of gas flow direction relative to wet material in dispersed-particle dryers can maintain higher gas velocities around the particles for longer periods than possible ia simple cocurrent dryers. This technique is thus expected to enhance heat- and mass-transfer performance. This is apart from the concept that mechanical stresses iaduced ia material by rapid directional reversals of gas flow promote particle deagglomeration, dispersion, and Hquid stream breakup iato fine droplets. Commercial appHcations are needed to confirm the economic value of pulse combustion for drying. 

Transient Heating of Droplets When a cold liquid fuel droplet is injected into a hot stream or ignited by some other source, it must be heated to its steady-state temperature Ts derived in the last section. Since the heat-up time can influence the V/2 law, particularly for high-boiling-point fuels, it is of interest to examine the effect of the droplet heating mode on the main bulk combustion characteristic—the burning time. 

COSILAB Combustion Simulation Software is a set of commercial software tools for simulating a variety of laminar flames including unstrained, premixed freely propagating flames, unstrained, premixed burner-stabilized flames, strained premixed flames, strained diffusion flames, strained partially premixed flames cylindrical and spherical symmetrical flames. The code can simulate transient spherically expanding and converging flames, droplets and streams of droplets in flames, sprays, tubular flames, combustion and/or evaporation of single spherical drops of liquid fuel, reactions in plug flow and perfectly stirred reactors, and problems of reactive boundary layers, such as open or enclosed jet flames, or flames in a wall boundary layer. The codes were developed from RUN-1DL, described below, and are now maintained and distributed by SoftPredict. Refer to the website http //www.softpredict.com/cms/ softpredict-home.html for more information. 

In order for fuel to combust and bum efficiently, it must be atomized into extremely small droplets. Fuel injectors aid tremendously in performing this role. However, if fuel viscosity is high, atomization into small droplets becomes difficult. Highly viscous fuel will not disperse freely after being sprayed from the fuel injector. The fuel instead sprays as a stream or large drops rather than as a fine mist. The result is a decrease in fuel efficiency and power due to incomplete burning of larger fuel droplets. 

Highly viscous diesel fuel will not atomize properly when sprayed from a fuel injector. It can spray as large droplets or as a stream instead of as an atomized mist. Incomplete combustion of fuel can result. 

Gas-continuous impinging streams with a liquid as the dispersed phase has wide application, such as in the combustion of liquid fuel droplets, absorption, water-spray cooling of air, etc. [9]. In such systems the dispersity of liquids plays a very important role affecting heat and mass transfer rates, because it influences both the interface area and the mean transfer coefficient. Wu et al. [68] investigated the influence of impinging streams on the dispersity of liquid. 

In another example of flame synthesis, H2 (or other fuel) and O2 are used for combustion, and droplets of an aqueous salt solution are entrained in one of the streams. In a particular example an aqueous salt solution of yttrium, barium, and copper nitrates was used to create the aerosol entrained in the dry O2 stream of a hydit en-o gen coan-nular diffusion flame with the oxidant as the inner stream. The result was an una lomerated YBa2Cu30 powder witti a critical superconducting temperature of 92 K [5] confirming its high paiily. 

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