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Industrial data precipitation

The results of Fig. 2.7 indicate that a significant fraction of particles in the nanometer size range will escape from electrostatic precipitator. for /i/oot values of the order of 10 ion sec cm . Such particles tend to form in high-temperature processes such as coal combustion, incineration, and the smelting of ores. Data are lacking on nanoparticle emissions from industrial electrostatic precipitators treating gases from coal-fired power plants or smelters. [Pg.46]

While. H. J. (1963) Industrial Electrostatic Precipitation, Addison-Wesley, Reading, MA. This highly readable monograph contains much practical operating data as well as discussions of fundamentals. [Pg.57]

Precipitation over North America gradually becomes more acidic from west to east, especially in industrialized areas of the Northeast. This acid rain may be a result of the release of nitrogen and sulfur oxides into the atmosphere. The colors and numbers (see key) indicate pH measured at field laboratories in 2004. Data from National Atmospheric Deposition Program/National Trends Network http //nadp.sws.uiuc.edu. [Pg.551]

A very limited amount of individual plant specific data for the aluminum forming industry is available. Data available on the influent and effluent streams are discussed briefly in the following subsections for specific plants. This aluminum processing plant uses lime precipitation (pH adjustment) followed by coagulant addition and sedimentation as its treatment system. Data... [Pg.214]

The electrostatic precipitator in Example 2.2 is typical of industrial processes the operation of most process equipment is so complicated that application of fundamental physical laws may not produce a suitable model. For example, thermodynamic or chemical kinetics data may be required in such a model but may not be available. On the other hand, although the development of black box models may require less effort and the resulting models may be simpler in form, empirical models are usually only relevant for restricted ranges of operation and scale-up. Thus, a model such as ESP model 1 might need to be completely reformulated for a different size range of particulate matter or for a different type of coal. You might have to use a series of black box models to achieve suitable accuracy for different operating conditions. [Pg.43]

D. Rainwater Analysis. IC is also being applied to the analysis of ions in rainwater (13). Measurements of precipitation samples are being collected at remote or baseline stations to provide an estimate of the natural ion concentration observed in rain unaffected by man s activity. These measurements will provide data, to study increases of certain constituents with time due to energy and industrial oroduction. [Pg.241]

A knowledge of the chemical components in the deposition throughout Japan is needed in order to evaluate the effect of increasing rain acidity. Intensive studies have been done on the chemical components in precipitation or deposition, especially at the industrialized area of the Pacific side. However, systematic data are lacking for the less industrialized area on the Japan Sea side. [Pg.257]

Fig. 4.3. Schematic of dry rod and plate electrostatic precipitator (after Oglesby and Nichols, 1978). The rods have sharp horizontal protrusions (nails) which promote corona formation. Dusty gas flows between the plates and around the rods. A large electrical potential (60 000 V) is applied between the rods and plates. This negatively charges the dust particles - causing them to approach and adhere to the positive collection plates. The dust is gathered by periodically rapping the plates, causing sheets of dust to fall into dust bins below, Fig. 4.4. Table 4.2 gives industrial precipitation data. Fig. 4.3. Schematic of dry rod and plate electrostatic precipitator (after Oglesby and Nichols, 1978). The rods have sharp horizontal protrusions (nails) which promote corona formation. Dusty gas flows between the plates and around the rods. A large electrical potential (60 000 V) is applied between the rods and plates. This negatively charges the dust particles - causing them to approach and adhere to the positive collection plates. The dust is gathered by periodically rapping the plates, causing sheets of dust to fall into dust bins below, Fig. 4.4. Table 4.2 gives industrial precipitation data.
A free-radical polymerization mechanism can be excluded on the basis of the polymer microstructure and experiments with radical inhibitors. Rhodium(I)-spe-cies, formed by reduction of Rh " salts used as catalyst precursors by butadiene monomer, have been suggested as the active species. The catalyst is stable during the aqueous polymerization for over 30 h [23]. Catalyst activities are moderate with up to ca. 2x10 TO h [24, 25]. By contrast to industrially important free-radical copolymerization, styrene is not incorporated in the rhodium-catalyzed butadiene polymerization [26]. Only scarce data is available regarding the stability and other properties of the polymer dispersions obtained. Precipitation of considerable portions of the polymer has been mentioned at high conversions in butadiene polymerization [23, 27]. [Pg.237]

In the first stage of the studies an assessment of the dynamics of the main emissions from the industrial plants and the contents of each component was performed, based on the data from statistical reports (Glavgidromet, 2001). At the same time, the changes of the chemical composition of the gas phase, atmospheric aerosols, and precipitation during the same period were analyzed, and possible impacts of atmospheric fallouts on the environment were assessed. [Pg.394]


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See also in sourсe #XX -- [ Pg.36 ]

See also in sourсe #XX -- [ Pg.36 ]

See also in sourсe #XX -- [ Pg.36 ]




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