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Solid particles in the air

From the hygiene standpoint, particles of a size from 2.0 down to 0.1 / m are the most dangerous. The biological effect of the dust on the organism depends on its composition and physical properties. These characteristics affect the solubility in liquids, the toxicity, the electric charge, etc. The dust particles exert the following effects  [Pg.792]


Dust Consists of small, very fine, solid particles in the air the sources of dust could be from the following Automotive paint Batteries Brake fluid Engine degreaser Epoxies and adhesives Flea powder Gasoline Herbicides Insecticides Mothballs Oil-based paints Paint stripper Photographic chemicals Polishes containing nitrobenzenes Wood preservatives. [Pg.603]

Dust Chemical snbstances consisting of small, very fine, solid particles in the air Dysplasia Abnormal development or growth... [Pg.206]

The concept of air as a colloid and the term aerosol for air containing an assembly of suspended particles were originally introduced by Schmauss and Wigand (1929). Colloids are inherently stable because fine particles are subject to Brownian motion and resist settling by sedimentation. The individual aerosol particles may be solid, liquid, or of a mixed variety, and all types are found in the atmosphere. Solid particles in the air are called dust. They are primarily formed by the erosion of minerals at the earth surface and enter the atmosphere by wind force. Sea spray from the ocean surface provides a prolific source of liquid droplets, which upon evaporation produce sea-salt crystals or a concentrated aqueous solution thereof. Solid and liquid particles also arise from the condensation of vapors when the vapor pressure exceeds the saturation point. For example, smoke from the open and often incomplete combustion of wood or agricultural refuse arises at least in part from the condensation of organic vapors. [Pg.278]

The type of air contaminants that occur in the workplace depends on the raw materials used and the processes involved. Air contaminants can be classified into two groups based on their physical properties (1) aerosols (a suspension of liquid or solid particles in the air), and (2) gases/vapors. [Pg.59]

Wall-to-bed heat-transfer coefficients were also measured by Viswanathan et al. (V6). The bed diameter was 2 in. and the media used were air, water, and quartz particles of 0.649- and 0.928-mm mean diameter. All experiments were carried out with constant bed height, whereas the amount of solid particles as well as the gas and liquid flow rates were varied. The results are presented in that paper as plots of heat-transfer coefficient versus the ratio between mass flow rate of gas and mass flow rate of liquid. The heat-transfer coefficient increased sharply to a maximum value, which was reached for relatively low gas-liquid ratios, and further increase of the ratio led to a reduction of the heat-transfer coefficient. It was also observed that the maximum value of the heat-transfer coefficient depends on the amount of solid particles in the column. Thus, for 0.928-mm particles, the maximum value of the heat-transfer coefficient obtained in experiments with 750-gm solids was approximately 40% higher than those obtained in experiments with 250- and 1250-gm solids. [Pg.129]

Consider a fluidized bed operated at an elevated temperature, e.g. 800°C, and under atmospheric pressure with ah. The scale model is to be operated with air at ambient temperature and pressure. The fluid density and viscosity will be significantly different for these two conditions, e.g. the gas density of the cold bed is 3.5 times the density of the hot bed. In order to maintain a constant ratio of particle-to-fluid density, the density of the solid particles in the cold bed must be 3.5 times that in the hot bed. As long as the solid density is set, the Archimedes number and the Froude number are used to determine the particle diameter and the superficial velocity of the model, respectively. It is important to note at this point that the rale of similarity requires the two beds to be geometrically similar in construction with identical normalized size distributions and sphericity. It is easy to prove that the length scales (Z, D) of the ambient temperature model are much lower than those in the hot bed. Thus, an ambient bed of modest size can simulate a rather large hot bed under atmospheric pressure. [Pg.542]

Macromolecular substances such as synthetics (Sellin 1982 Berman 1978), biopolymers (Hoyt 1985), or surfactants (Shenoy) have proved to be effective flow improvers . Suspended fibers and solid particles (e.g., Metzner 1977,1976 McComb 1981), however, may also produce this effect. Small suspended particles in the air ( dust ) have been found to cause drag reductions of the same order of magnitude as polymers in liquids (Rossetti). [Pg.101]

In a measurement of air pollution, air was drawn through a filter at the rate of 26.2 liters per minute for 48.0 hours. The filter gained 0.0241 grams in mass because of entrapped solid particles. Express the concentration of solid contaminants in the air in units of micrograms per cubic meter. [Pg.8]

CDDs are released into the air in emissions from municipal solid waste and industrial incinerators. Exhaust from vehicles powered with leaded and unleaded gasoline and diesel fuel also release CDDs to the air. Other sources of CDDs in air include emissions from oil- or coal-fired power plants, burning of chlorinated compounds such as PCBs, and cigarette smoke. CDDs formed during combustion processes are associated with small particles in the air, such as ash. The larger particles will be deposited close to the emission source, while very small particles may be... [Pg.24]

While in the air compartment, the contaminant solubilizes in the vapor-liquid phase or is associated with aerosol particles by adsorption. It is also prone to desorption from the aerosol particles into the vapor phase. Relevant properties of the air used to model transport of partitioning of a contaminant in the air compartment include temperature, turbulence, wind speed, size and composition of aerosol particles, etc.16,19 Relevant properties of the contaminant that measure its tendency to partition among the vapor, liquid, and solid phases in the air include its aqueous solubility (Saq), vapor pressure (VP), Henry s constant... [Pg.228]

Figure 5. Photographic sequence in which an air bubble, on the tip of a capillary, is pushed down through an alkaline solution, at 80 °C, until it just touches a layer of bitumen that had been coated onto a silica surface. The bitumen spontaneously spreads over the surface of the bubble causing it to detach from the capillary and become engulfed. The presence of solid particles in the bitumen on the surface can be observed in the lower photo. (Photomicrographs by L. L. Schramm.)... Figure 5. Photographic sequence in which an air bubble, on the tip of a capillary, is pushed down through an alkaline solution, at 80 °C, until it just touches a layer of bitumen that had been coated onto a silica surface. The bitumen spontaneously spreads over the surface of the bubble causing it to detach from the capillary and become engulfed. The presence of solid particles in the bitumen on the surface can be observed in the lower photo. (Photomicrographs by L. L. Schramm.)...
Liquid and solid particles enter the air predominantly from natural sources only 11% comes from human activity. From these particles, so-called secondary particles are formed directly in the atmosphere, either during a change in the state of matter or in interactions of imissions connected with a formation of liquid and solid products. [Pg.510]

Another widely used method is solid state nuclear track detection. In the case of radon, an alpha track detector is used. It consists of a small piece of plastic enclosed in a container with a filter-covered opening. Alpha particles in the air strike the plastic and produce submicroscopic damage tracks. At the end of the measurement period the plastic is placed in a caustic solution that accentuates the damage tracks. The tracks are then counted using a microscope or automated counting system. [Pg.94]

Particulate Matter—A suspension of fine solid or liquid particles in the air, such as dust, fog, fumes, mist, smoke, or sprays. [Pg.309]

Adhesion of gas bubbles to solid particles. In the hydrometallurgical process, flotation, gas bubbles are attached to ore particles and carry them to the surface of the liquid phase. The attraction force is adhesion of circular line elements at the contact of a nonwetted solid phase (ore), liquid phase (aqueous solutions of flotation agents), and gas phase (air or hydrogen bubble). This system is presented in Figure 1.17. [Pg.12]

Particulates n. Finely divided solid or hquid particles in the air or in an emission. Particulates include dust, smoke, fumes, mist, spray, and fog. [Pg.696]

Oxidation of iron ore particles in the presence of air is carried out in a fluidised bed reactor. Solids are fed to the reactor at the rate of 10 kg/min. Mass hold-up of solid particles in the reactor is 300 kg. Feed consists of 20% (by weight) of 1 mm particles, 30% of 1.5 mm particles, 30% of 2 mm particles and 20% of 3 mm particles. SCM holds good and the reaction is rate controlling. The time for complete conversion of 3 mm particles is 3 h. Calculate the mean conversion of solids in the fluidised bed reactor. [Pg.308]

The scattering of light from automobile headlights by fogs and mists is an example of the Tyndall effect, as is the scattering of a light beam in a laser show by dust particles in the air in a darkened room. If the air didn t have any suspended solid particles you would not be able to see the laser beam. [Pg.535]

With the exception of capsaicin (originally proposed as a potential harassing agent in World War I) or pepper spray, tear gases are often a solid at room temperature and are dispersed in an aerosol (a suspension of fine particles in the air), in a liquid solvent (for example, Mace ), or as vapor generated using... [Pg.117]

In addition, solid particles in the feed stream can cause plugging of fixed beds of catalyst. In processing exhaust air streams containing VOCs, the presence of halogens is normally the most significant problem. Particulates, if present, can be filtered from the gas stream before they reach the catalyst, and the other poisons listed are seldom present in significant quantities in such streams. [Pg.1151]

If we change the temperature and pressure, we will change the values in Table 3.1. Clothes dry faster in a clothes dryer than on a clothesline, because in the dryer we heat the clothes and the air around them, thus increasing the equilibrium concentration of water in air, and making the process go faster. Conversely, if we lower the temperature of the air, the equilibrium concentration of water will decline. If there is an available solid surface, the water will condense on it, forming dew. If there is no surface, but there are enough fine particles in the air, the water will condense on them, forming clouds or fog. [Pg.38]

In some instances, the source of radon is in wastes from uranium mining or phosphate production. In most cases, it is emitted by the radioactive decay of present in small amounts in rocks and soils. Because radon is a gas, it readily passes through air passages in the body and is breathed in and out. The product formed when a Rn atom gives up an a particle is the isotope polonium-218, which also emits a particles. Unlike radon, polonium is a solid. Health hazards posed by radon seem to be from Po and other radioactive decay products becoming attached to dust particles in the air and then being breathed into the lungs. [Pg.1197]


See other pages where Solid particles in the air is mentioned: [Pg.9]    [Pg.204]    [Pg.9]    [Pg.204]    [Pg.23]    [Pg.22]    [Pg.157]    [Pg.74]    [Pg.263]    [Pg.23]    [Pg.829]    [Pg.422]    [Pg.292]    [Pg.166]    [Pg.130]    [Pg.271]    [Pg.140]    [Pg.263]    [Pg.668]    [Pg.739]    [Pg.458]    [Pg.19]    [Pg.1751]    [Pg.321]   


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