Big Chemical Encyclopedia

Chemical substances, components, reactions, process design ...

Articles Figures Tables About

Mechanisms coal combustion

Although the data presented here are limited to a single coal burned in two combustor operating modes, several important observations can be made about the fine particles generated by pulverized coal combustion. The major constituents of the very small nucleation generated particles vary with combustion conditions. High flame temperatures lead to the volatilization of refractory ash species such as silica and alumina, probably by means of reactions which produce volatile reduced species such as SiO or Al. At lower flame temperatures which minimize these reactions other ash species dominate the fine particles. Because the major constitutents of the fine particles are relatively refractory, nucleation is expected to occur early in the combustion process. More volatile species which condense at lower temperatures may also form new particles or may condense on the surfaces of the existing particles. Both mechanisms will lead to substantial enrichment of the very small particles with the volatile species, as was observed for zinc. [Pg.170]

Linak, W. P. Wendt, J. O. L. 1994. Trace-metal transformation mechanisms during coal combustion. Fuel Processing Technology, 39, 173-198. [Pg.206]

As a result of the well-documented environmental concerns posed by coal combustion, and the disposal of CCPs, a large body of research has focused on characterizing the mechanisms of mobilization and attenuation of trace elements in coal and its ash. Based on their reported distribution in the solid phases of both source coals and coal ash, knowledge of the thermal transformations that occur to major mineral constituents during coal combustion, and a limited number of studies that have identified discrete solid phases of trace elements, a conceptual model of the chemical and mineralogical characteristics of trace elements in coal ash has been developed. [Pg.240]

The seasonal distribution of particle-associated PAHs is controlled by a combination of emission factors (EFs), dispersion conditions and chemical mechanisms (Caricchia et al., 1999 Menichini et al., 1999). This balance depends on the relative importance of degradation processes and emission sources (Guo et al., 2003b). The highest PAH concentrations of a sampling site were usually obtained from winter samples, and the differences were far higher in northern cities than southern ones, suggesting that coal combustion for space heating contributes the most PAHs in winter in Northern China. [Pg.243]

The lacking special description of the Gibbs phase rule in MEIS that should be met automatically in case of its validity is very important for solution of many problems on the analysis of multiphase, multicomponent systems. Indeed, without information (at least complete enough) on the process mechanism (for coal combustion, for example, it may consist of thousands of stages), it is impossible to specify the number of independent reactions and the number of phases. Prior to calculations it is difficult to evaluate, concentrations of what substances will turn out to be negligibly low, i.e., the dimensionality of the studied system. Besides, note that the MEIS application leads to departure from the Gibbs classical definition of the notion of a system component and its interpretation not as an individual substance, but only as part of this substance that is contained in any one phase. For example, if water in the reactive mixture is in gas and liquid phases, its corresponding phase contents represent different parameters of the considered system. Such an expansion of the space of variables in the problem solved facilitates its reduction to the CP problems. [Pg.47]

The presented brief survey of basic mechanisms of NO formation during coal combustion allows the MEIS construction with their simultaneous inclusion in the kinetic constraints. Kinetic constraints can be formulated according to the third way among those considered in Section 3.4. [Pg.56]

The studies on NO formation by the traditional MEIS have been performed at Melentiev Energy Systems Institute for a long time. In parallel with MEIS the use was made of kinetic models and full-scale experiments that assisted in turn to gain information for variant calculations on MEIS. The results of these calculations allowed the conditions for nitrogen oxides formation by different mechanisms to be determined and the ways for improvement of coal combustion technology to increase environmental safety of boiler units to be outlined. [Pg.61]

At the same time calculations on the modified MEIS are possible without additional kinetic models and do not require extra experimental data for calculations, which makes it possible to use less initial information and obviously reduces the time and labor spent for computing experiment. Furthermore, there arise principally new possibilities for the analysis of methods to mitigate emissions from pulverized-coal boilers, since at separate modeling of different mechanisms of NO formation the measures taken can result in different consequences for each in terms of efficiency. Consideration of kinetic constraints in MEIS will substantially expand the sphere of their application to study other methods of coal combustion (fluidized bed, fixed bed, etc.) and to model processes of forming other pollutants such as polyaromatic hydrocarbons, CO, soot, etc. [Pg.62]

Although the fly ash particle size distribution in the submicron regime is explained qualitatively by a vaporization/homogeneous nucleation mechanism, almost all of the available data indicate particles fewer in number and larger in size than predicted theoretically. Also, data on elemental size distributions in the submicron size mode are not consistent with the vapor-ization/condensation model. More nonvolatile refractory matrix elements such as A1 and Si are found in the submicron ash mode than predicted from a homogeneous nucleation mechanism. Additional research is needed to elucidate coal combustion aerosol formation mechanisms. [Pg.276]

Mechanisms involved in organic emissions at coal combustion are very complex and not well known. It is not necessary for the emitted organic compounds to be part of the volatile coal structure, neither the particulate matter emission needs to be unbumed material [2]. The devolatilization and the p5rolytic processes joined to any fuel combustion imply radicals release, which is the cause of the new organic and particulate matter emissions by pyrosynthesis retrogressive reactions [2].Therefore, the radicals interactions and the... [Pg.403]

Therefore, and because of the Ca presence, a possible Ca catal)4ic role could be guessed. The chelating mechanisms reported [10,11] at polymeric pyrolysis can not be applied to coal combustion because the inert-reducing atmosphere at pyrolysis process has not relation to the oxidation conditions at the combustion atmospheres. However, other additional effect in the LCL runs could influence the PAH emission and distribution. This effect would be a possible catalytic role performed by Ca. [Pg.407]

The coarse mode is largely composed of primary particles generated by mechanical pro-ce.sses such as soil dust raised by llie wind and/or vehicular traffic and construction activities. Coarse particles arc also emitted in gu.ses from industrial sources such as coal combustion and smelting. The coarse mode often peaks at about lO/tin. The chemical composition of the coarse mode is for the most part the sum of the chemical components of the primary aerosol emissions. However, there may be some contributions from gas-to-particle conversion, such as ammonium nitrate, as discussed below. [Pg.361]

Besides, new combustion conditions increasingly being specified in order to minimize NOx emissions in power plant stack gases result in increased carbon content in the fly ash produced under these new conditions. This further restricts the types and amounts of fly ash that can be utilized as a filler, and decreases commercial applications of coal combustion fly ash even more. Therefore, many methods have been developed to remove carbon particles from the fly ash and minimize the adverse effects of the carbon on characteristics of the filler materials. These methods include chemical combustion, gravitational, flotational, electrostatic, magnetic, and mechanical means, and combinations of these [12-19]. [Pg.148]


See other pages where Mechanisms coal combustion is mentioned: [Pg.1598]    [Pg.4]    [Pg.44]    [Pg.31]    [Pg.223]    [Pg.490]    [Pg.654]    [Pg.142]    [Pg.119]    [Pg.2]    [Pg.69]    [Pg.108]    [Pg.111]    [Pg.25]    [Pg.54]    [Pg.63]    [Pg.141]    [Pg.267]    [Pg.1420]    [Pg.189]    [Pg.189]    [Pg.547]    [Pg.257]    [Pg.266]    [Pg.142]    [Pg.218]    [Pg.232]    [Pg.164]    [Pg.291]    [Pg.1912]    [Pg.1384]    [Pg.148]    [Pg.254]    [Pg.768]    [Pg.1902]    [Pg.1602]    [Pg.735]   
See also in sourсe #XX -- [ Pg.66 ]




SEARCH



Coal combustion fluid mechanics

Coal mechanism

Mechanisms combustion

© 2024 chempedia.info