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Droplet phase reactions

A particularly simpicsolution is obtained in the case ofagrowth law oftheform c/ = vX corresponding to a droplet-phase reaction (Chapter 10). If the initial size distribution is of a power law form, tl — hv Noo, substitution in (11.43) results in the following expression ... [Pg.321]

This form is quite different from the diffusional growth expression (13.7) in its dependence on particle size in this case, larger particles grow faster than smaller ones. McMurry et ai. (1981) analyzed data for several power plant plumes (Fig. 13.6a). They found that both diffusion to the particles and droplet phase reaction contributed to plume aerosol growth (Fig. 13.6b). However, the droplet-phase reactions accounted for less than 20% of total aerosol volume growth. [Pg.370]

Figure 13.6 (a) Volume distributions for the Cumberland power plant (Clarksville, TN) measured at various locations in the plume downwind from the plant on 8/10/79. Secondary aerosol accumulated in all particles up to 1 m—in contrast with the Navajo plant aerosol (Fig. 13.5) which was limited to dp < 0.3 /im. (b) Particle diameter growth rates calculated from data shown in part (a) with a best-fit curve based on an interpolation formula that reduces to the diffusion mechanism for the smaller particles (13,7) and droplet phase reaction for the larger particles (13.8). (After McMurry et al., 1981.)... [Pg.371]

Sulfate ion i.s the chemical component usually present in highest concentration in the submieron atmospheric aerosol. Almo.st all of the sulfate results from the atmospheric oxidation of SO either by homogeneous gas-phase reactions or by aerosol- or droplet-phase reactions. Reaction with the hydroxyl radical OH is thought to be the major ga.s-phase mechanism. Many solution-phase processes are possible, including reaction with dissolved HiO and reactions with 0 catalyzed by dissolved metals such as Fe and Mn (Seinfeld and Pandis, 1998). [Pg.374]

Fogs in polluted environments have the potential to increase aerosol concentrations by droplet-phase reactions but, at the same time, to cause reductions because of the rapid deposition of larger fog droplets compared to smaller particles (Pandis et al. 1990). Pandis et al. (1992) estimated that more than half of the sulfate in a typical aerosol air pollution episode was produced inside a fog layer the previous night. [Pg.966]

Surfactants provide temporary emulsion droplet stabilization of monomer droplets in tire two-phase reaction mixture obtained in emulsion polymerization. A cartoon of tliis process is given in figure C2.3.11. There we see tliat a reservoir of polymerizable monomer exists in a relatively large droplet (of tire order of tire size of tire wavelengtli of light or larger) kinetically stabilized by surfactant. [Pg.2596]

Vanadium-Sodium Compounds Most Corrosive. Physical property data for vanadates, phase diagrams, laboratory experiments, and numerous field investigations have shown that the sodium vanadates are the lowest melting compounds and are the most corrosive to metals and refractories. These compounds are thought to form by either the vapor phase reaction of NaCI and V2O5 or by the combination of fine droplets of these materials upon the cooler parts of combustion equipment. [Pg.265]

SO2 oxidation to H2SO4 on aerosols, in cloud droplets, and by gas phase reactions following attack by OH. [Pg.152]

Typical results, shown in Fig. 21(a), demonstrate that the rate constant for the reaction between TCNQ and aqueous Fe(CN)g increases with increasing driving force, promoted by decreasing [CIO4 as evidenced by the steeper Fe(CN)g concentration profiles. Moreover, the Tafel plot obtained for ET between Fe(CN)g and TCNQ is linear with an apparent measured a value of 0.31 0.02. In these studies, the concentration of reactant in the droplet phase was always at least 10 times the concentration of the reactant in the receptor phase, to ensure that depletion (and diffusional) effects within the droplet were negligible. [Pg.356]

In the first scheme the metal boiling point is less than the oxide boiling point and the model consists of a vaporising droplet of metal surrounded by a detached reaction zone where condensed oxides appear as fine droplets. The reaction rate is said to be controlled by the vapour phase diffusion of metal and atmospheric oxygen into the reaction zone as in Figure 5.6. [Pg.89]

Diffusion into the bulk. This is determined by the diffusion coefficient in the liquid (D,). Diffusion within the bulk aqueous phase is much slower than gas-phase diffusion and can be rate-limiting under conditions of high reactant concentrations where the rate of the chemical reaction is high. This appears to have been a problem in some experimental studies of some aqueous-phase reactions relevant to the atmosphere where either bulk solutions or large droplets and reactant concentrations higher than atmospheric were used (Freiberg and Schwartz, 1981). [Pg.158]

It is likely that there are as yet ill-defined aqueous-phase reactions in the airborne seawater droplets that release photochemically labile chlorine gases. For example, Oum et al. (1998a) have shown that Cl2 is formed when sea salt aerosols above their deliques-... [Pg.180]

This dependence of the S(IV) concentrations on the pH of the droplet plays a critical role in determining which oxidant dominates the S(IV) oxidation. As discussed in more detail later, the rates of the various aqueous-phase reactions show different dependencies on pH. Some have rate coefficients that increase with... [Pg.302]

It was assumed that there were no limitations on the rates of oxidation due to mass transport as discussed in detail by Schwartz and Freiberg (1981), this assumption is justified except for very large droplets (> 10 yarn) and high pollutant concentrations (e.g., 03 at 0.5 ppm) where the aqueous-phase reactions are very fast. It was also assumed that the aqueous phase present in the atmosphere was a cloud with a liquid water content (V) of 1 g m-3 of air. As seen earlier, the latter factor is important in the aqueous-phase rates of conversion of S(IV) thus the actual concentrations of iron, manganese, and so on in the liquid phase and hence the kinetics of the reactions depend on the liquid water content. [Pg.326]

Heterogeneous Copolymerization. When copolymer is prepared in a homogeneous solution, kineiic expressions can be used to predict copolymer composition Bulk and dispersion polymerization are somewhat different since the reaction medium is heterogeneous and polymeri/aiion occurs simultaneously in separate loci. In bulk polymerization, for example, the monomer swollen polymer particles support polymerization within the particle core us well as on the particle surface, lit aqueous dispersion or emulsion polymeri/aiion the monomer is actually dispersed in two or three distinct phases a continuous aqueous phase, a monomer droplet phase, and a phase consisting of polymer particles swollen at Ihe surface with monomer. This affect the ultimate polymer composition because llie monomers are partitioned such that the monomer mixture in the aqueous phase is richer in the more water-soluble monomers than the two organic phases. [Pg.627]

Atmospheric Oxidation of SOo to Sulfate. Regardless of the source, sulfur dioxide is oxidized under atmospheric conditions in the gas phase, cloud droplets or on the surface of wet aerosol particles. The gas phase reaction (Equation 4)... [Pg.373]

Recently, the VLS growth method has been extended beyond the gas-phase reaction to synthesis of Si nanowires in Si-containing solvent (Holmes et al, 2000). In this case 2.5-nm Au nanocrystals were dispersed in supercritical hexane with a silicon precursor (e.g., diphenylsilane) under a pressure of 200-270 bar at 500°C, at which temperature the diphenylsilane decomposes to Si atoms. The Au nanocrystals serve as seeds for the Si nanowire growth, because they form an alloy with Si, which is in equilibrium with pure Si. It is suggested that the Si atoms would dissolve in the Au crystals until the saturation point is reached then they are expelled from the particle to form a nanowire with a diameter similar to the catalyst particle. This method has an advantage over the laser-ablated Si nanowire in that the nanowire diameter can be well controlled by the Au particle size, whereas liquid metal droplets produced by the laser ablation process tend to exhibit a much broader size distribution. With this approach, highly crystalline Si nanowires with diameters ranging from 4 nm to 5 nm have been produced by Holmes et al. (2000). The crystal orientation of these Si nanowires can be controlled by the reaction pressure. [Pg.184]

The development of environmentally acceptable incineration technologies for the disposal of hazardous wastes is dependent on an understanding of the roles of (1) atomization or method of introduction of the waste materials, (2) evaporation and condensed-phase reactions of the waste droplets in the incinerator environment, (3) turbulent mixing in the incinerator, (4) kinetics of the thermal degradation and oxidation of the chemical species in question, and (5) heat transfer in the incinerator. [Pg.288]

The process of miniemulsion allows in principle the use of all kinds of monomers for the formation of particles, which are not miscible with the continuous phase. In case of prevailing droplet nucleation or start of the polymer reaction in the droplet phase, each miniemulsion droplet can indeed be treated as a small nanoreactor. This enables a whole variety of polymerization reactions that lead to nanoparticles (much broader than in emulsion polymerization) as well as to the synthesis of nanoparticle hybrids, which were not accessible before. [Pg.95]


See other pages where Droplet phase reactions is mentioned: [Pg.397]    [Pg.286]    [Pg.374]    [Pg.32]    [Pg.397]    [Pg.286]    [Pg.374]    [Pg.32]    [Pg.519]    [Pg.279]    [Pg.397]    [Pg.66]    [Pg.807]    [Pg.1487]    [Pg.515]    [Pg.554]    [Pg.102]    [Pg.115]    [Pg.116]    [Pg.492]    [Pg.171]    [Pg.100]    [Pg.315]    [Pg.153]    [Pg.126]    [Pg.206]    [Pg.41]   


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