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Encounter-volume

Conceptually, SPMD data fills a gap between exposure assessments based on direct analytical measurement of total residues in water and air, and the analysis of residues present in biomonitoring organisms. SPMDs provide a biomimetic approach (i.e., processes in simple media that mimic more complex biological processes) for determining ambient HOC concentrations, sources, and gradients. Residues accumulated in SPMDs are representative of their environmental bioavailability (see Section 1.1.) in water and air and the encounter-volume rate as defined by Landrum et al. (1994) is expected to be proportional to the uptake rate. SPMD-based estimates of water concentrations can be readily compared to aquatic toxicity data (generally based on dissolved phase concentrations) and SPMD extracts can be used to screen for toxic concentrations of HOCs using bioassays or biomarker tests. [Pg.32]

Some introductory comments on the conceptual basis of SPMD uptake (ku) and release (ke) rate constants and the associated sampling rates (i.e., Rs) are in order. The can be conceptualized as the volume of air or water cleared of chemical per unit sampler mass or volume per unit time (e.g., mL g d or mL mL d ) and Rs is the volume of air or water cleared per unit time (e.g., L d ). Thus, the only difference between ku and Rs is that Rs is not normalized to a unit mass or unit volume of sampler. In the context of organism exposure (see Section l.L), the SPMD is equivalent to the encounter volume times the fractional bioavailability of the chemical (which excludes dietary uptake). The release rate constant (d ) is equal to kuK J. [Pg.39]

Upon heating water becomes less viscous (section 15.2). This makes the transport of reactants faster. If the diffusive step is fast compared with the reactive stage taking place within the boundaries of the reaction encounter volume, the overall rate of bimolecular reactions is limited by the chemical transformation, and k k. Following the transition state theory (TST) the bimolecular reaction eqn (15.9) can be considered as a two-step process, in which the transition state complex AB, formed in a reversible step, decays into products in an irreversible step. [Pg.387]

The self-reaction of the hydrogen radical, H H - H2, is supposed to be truly diffusion-controlled. The accepted reaction radius of 0.19 nm (Table 15.1) is, by a factor of 3.5, greater than the hydrodynamic radius /"h obtained from eqn (15.3) for T>h(25) = 7x 10 m s The fast diffusion of H and the long time of spin relaxation, 1.3 x 10 s, make spin relaxation before diffusing out of the encounter volume rather improbable. Figure 15.12 shows that the kinetic data are well reproduced by the Smoluchowski equation assuming the temperature dependence for Dh from eqn (15.5) and the spin factor jSspi = 0.25. [Pg.389]

In some depositional environments, e.g. fluviatile channels, marked differences in reservoir thickness will be encountered. Hence the assumption of a constant thickness, or a linear trend in thickness across the field will no longer apply. In those cases a set of additional maps will be required. Usually a net oil sand (NOS) map will be prepared by the production geologist and then used to evaluate the hydrocarbon volume in place. [Pg.156]

The units of concentration most frequently encountered in analytical chemistry are molarity, weight percent, volume percent, weight-to-volume percent, parts per million, and parts per billion. By recognizing the general definition of concentration given in equation 2.1, it is easy to convert between concentration units. [Pg.18]

Particulate gravimetry is commonly encountered in the environmental analysis of water, air, and soil samples. The analysis for suspended solids in water samples, for example, is accomplished by filtering an appropriate volume of a well-mixed sample through a glass fiber filter and drying the filter to constant weight at 103-105 °C. [Pg.264]

In molecular weight determinations it is conventional to dissolve a measured mass of polymer m2 into a volumetric flask and dilute to the mark with an appropriate solvent. We shall use the symbol Cj to designate concentrations in mass per volume units. In practice, 100-ml volumetric flasks are often used, in which case C2 is expressed in grams per 100 ml or grams per deciliter. Even though these are not SI units, they are encountered often enough in the literature to be regarded as conventional solution units in polymer chemistry. [Pg.550]

This chapter is the only place in this volume that we encounter electrical units. Certain equations in electrostatics differ by the factor 47t, depending on whether they are written for SI or cgs units. To help clarify this situation, the chapter contains an appendix on electrical units which may be helpful, particularly when references based on other units are consulted. [Pg.660]

Usage of phosphoms-based flame retardants for 1994 in the United States has been projected to be 150 million (168). The largest volume use maybe in plasticized vinyl. Other use areas for phosphoms flame retardants are flexible urethane foams, polyester resins and other thermoset resins, adhesives, textiles, polycarbonate—ABS blends, and some other thermoplastics. Development efforts are well advanced to find appHcations for phosphoms flame retardants, especially ammonium polyphosphate combinations, in polyolefins, and red phosphoms in nylons. Interest is strong in finding phosphoms-based alternatives to those halogen-containing systems which have encountered environmental opposition, especially in Europe. [Pg.481]

The chemical and mechanical dispersion of the drilled soHds tends to increase the percentage of smaH-sized soHds in a mud as drilling progresses. The incorporation of a limited amount of drilled soHds (several volume percent) is an economical way of increasing the density of low density muds, but it also reduces penetration rates hence, drilled soHds are usually kept to a minimum. The common clay and formation soHds encountered in normal drilling operations are as foUows ... [Pg.177]

Safety Showers. Safety showers and eyewash fountains or hoses should be installed where corrosive or toxic materials are handled. A large-volume, low velocity discharge from directly overhead should effect continuous drenching, ie, a minimum flow of 20 L/min (50 gal /min). Water to outside showers may be heated to a maximum temperature of 27°C by an electric heating cable. The valves for all safety showers should be at the same height and relative position to the shower head, and they should operate in the same way and direction. The shower station should be identified by paint of a bright, contrasting color. In areas where chemicals harmful to the eyes may be encountered, an eyewash fountain or spray should be available in case of splash accidents. [Pg.99]

Droplet Dispersion. The primary feature of the dispersed flow regime is that the spray contains generally spherical droplets. In most practical sprays, the volume fraction of the Hquid droplets in the dispersed region is relatively small compared with the continuous gas phase. Depending on the gas-phase conditions, Hquid droplets can encounter acceleration, deceleration, coUision, coalescence, evaporation, and secondary breakup during thein evolution. Through droplet and gas-phase interaction, turbulence plays a significant role in the redistribution of droplets and spray characteristics. [Pg.330]

Abrasive wear is encountered when hard particles, or hard projections on a counter-face, are forced against and moved relative to a surface. In aUoys such as the cobalt-base wear aUoys which contain a hard phase, the abrasion resistance generaUy increases as the volume fraction of the hard phase increases. Abrasion resistance is, however, strongly influenced by the size and shape of the hard-phase precipitates within the microstmcture, and the size and shape of the abrading species (see Abrasives). [Pg.373]

Hindered Settling When particle concentration increases, particle settling velocities decrease oecause of hydrodynamic interaction between particles and the upward motion of displaced liquid. The suspension viscosity increases. Hindered setthng is normally encountered in sedimentation and transport of concentrated slurries. Below 0.1 percent volumetric particle concentration, there is less than a 1 percent reduction in settling velocity. Several expressions have been given to estimate the effect of particle volume fraction on settling velocity. Maude and Whitmore Br. J. Appl. Fhys., 9, 477—482 [1958]) give, for uniformly sized spheres,... [Pg.678]


See other pages where Encounter-volume is mentioned: [Pg.3]    [Pg.33]    [Pg.335]    [Pg.3]    [Pg.33]    [Pg.335]    [Pg.116]    [Pg.769]    [Pg.2470]    [Pg.2522]    [Pg.587]    [Pg.871]    [Pg.66]    [Pg.81]    [Pg.41]    [Pg.391]    [Pg.56]    [Pg.431]    [Pg.432]    [Pg.171]    [Pg.191]    [Pg.121]    [Pg.202]    [Pg.429]    [Pg.297]    [Pg.182]    [Pg.298]    [Pg.67]    [Pg.257]    [Pg.128]    [Pg.168]    [Pg.225]    [Pg.334]    [Pg.352]    [Pg.532]    [Pg.248]    [Pg.514]    [Pg.579]   
See also in sourсe #XX -- [ Pg.3 , Pg.32 , Pg.33 , Pg.39 ]




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Encounter

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