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Particle determinations

During Stages II and III the average concentration of radicals within the particle determines the rate of polymerization. To solve for n, the fate of a given radical was balanced across the possible adsorption, desorption, and termination events. Initially a solution was provided for three physically limiting cases. Subsequentiy, n was solved for expHcitiy without limitation using a generating function to solve the Smith-Ewart recursion formula (29). This analysis for the case of very slow rates of radical desorption was improved on (30), and later radical readsorption was accounted for and the Smith-Ewart recursion formula solved via the method of continuous fractions (31). [Pg.24]

Also, in cases where the dimensions of a regular particle vary throughout a bed of such particles or are not known, but where the fractional free volume and specific surface can be measured or calculated, the shape factor can be calculated and the equivalent diameter of the regular particle determined from Figure 2. [Pg.369]

Nanoparticles of the semicondnctor titanium dioxide have also been spread as mono-layers [164]. Nanoparticles of TiOi were formed by the arrested hydrolysis of titanium iso-propoxide. A very small amount of water was mixed with a chloroform/isopropanol solution of titanium isopropoxide with the surfactant hexadecyltrimethylammonium bromide (CTAB) and a catalyst. The particles produced were 1.8-2.2 nm in diameter. The stabilized particles were spread as monolayers. Successive cycles of II-A isotherms exhibited smaller areas for the initial pressnre rise, attributed to dissolution of excess surfactant into the subphase. And BAM observation showed the solid state of the films at 50 mN m was featureless and bright collapse then appeared as a series of stripes across the image. The area per particle determined from the isotherms decreased when sols were subjected to a heat treatment prior to spreading. This effect was believed to arise from a modification to the particle surface that made surfactant adsorption less favorable. [Pg.89]

The amount of particles determine the quantity of decay products that stay in the air (equilibrium fraction, F) and the fraction of activity associated with the "unattached or ultrafine mode of the size distribution (fDot) These decay products are certainly harmful at high concentrations but we cannot yet detect the effects at normal levels because the vast majority of lung cancer death are due to smoking. Models predict that potentially 9000 lung cancer deaths per year in the United States are due to indoor radon. Methods are currently available and new methods are being developed and tested for lowering the levels of radon in indoor air. [Pg.583]

The evaluation of the reaction cross sections as a function of the initial state of the reactants and final state of the products has been described by Karplus, Porter and Sharma (1965), and Greene and Kuppermann (1968) using classical equations of motions for interacting species. For a given potential V(rb r2, r3), a set of initial coordinates and momenta for the particles determine uniquely the collision trajectory and the occurrence of reaction. The method is described as follows. [Pg.229]

FIGURE 13.13. Hydrodynamic diameters of colloidal particles determined by QELS as a function of the hydrosol pH. [Pg.265]

We consider a transfer reaction of redox electrons in which the interfacial transfer of electrons is in quasi-equilibrium ( Hh =0) and the diffusion of redox particles determines the overall reaction rate. The anodic diffusion current, and the anodic limiting current of diffusion, inm, in the stationary state of the electrode reaction are given, respectively, in Eqns. 8-33 and 8-34 ... [Pg.247]

Brilman et al. [42] and Lin et al. [44] using a numerical method, Nagy [48] by using an analytical method, investigated the effect of the second, third, etc. particles (perpendicular to the gas-liquid interface) on the absorption rate. They obtained that, in most cases, the first particle determines the absorption rate. However, in special cases, the effect of these particles can also be important. Nagy solved the mass transfer problem analytically for the number of particles in the diffusion path [48]. For the sake of completeness we will give the absorption rate for that case, as well (for details see [48] ). The mass transfer is accompanied here by a first-order chemical reaction. This situation is illustrated in Fig. 1 where three particles are located behind each other. The absorption rate... [Pg.59]

Why is it that some substances readily mix to form solutions while others do not Whether one substance dissolves in another substance is largely dependent on the inter-molecular forces present in the substances. For a solution to form, the solute particles must become dispersed throughout the solvent. This process requires the solute and solvent to initially separate and then mix. Another way of thinking of this is that the solute particles must separate from each other and disperse throughout the solvent. The solvent may separate to make room for the solute particles or the solute particles may occupy the space between the solvent particles. Determining whether one substance dissolves in another requires examining three different intermolecular forces present in the substances—between the... [Pg.126]

TABLE 10.12 Concentrations of 10 PAHs in National Institute of Standards and Technology (NIST) Standard Reference Material SRM 1649 Air Particles Determined by Dual Programmable Fluorescence Detector Method... [Pg.464]

Let us skip the next region temporarily and consider the range Q > 1. As mentioned above, intraparticle interference within the primary particles determines the function P(Q) in this case, and the functional form of P(Q) is determined by the shape of the primary particle (assumed here to be spherical). For spheres, one can show that... [Pg.225]

The overall yield is essentially 100 by any of the preparation methods, but the physical characteristics of the ion exchangers are dependent on preparation conditions. For example, sodium titanate prepared by Eqs. la and lb with hydrolysis in one liter of water per mole of Ti(OC3H7)4 has a bulk density of 0.U5 g/cm3 and a specific surface area of lO-UO m /g. The same material prepared by Eqs. la and lb and hydrolyzed in a solution of 100 ml of water in 1000 ml of acetone for each mole of Ti(OC2H7)4 has a bulk density of 0.35 g/cm3 and a specific surface area of 200-UOO m /g. In all cases, the materials consist of agglomerates of 50-100 A particles with the degree of aggregation of the particles determining both the bulk density and surface area. [Pg.131]

Their physicochemical properties and the individual factors that we need to evaluate the equations of Box 23.1 are listed in Table 23.4. Except for the measurements that are specific for Lake Superior (input rates, concentrations of PCBs, composition of the particles determining, etc.), all the data were derived from information given in this book either in tables (e.g., Henry s Law constants) or indirectly by approximative relationships (e.g., Kd =foc K. ). More details are given in the footnotes to Table 23.4. [Pg.1065]

It is interesting that vacuum properties are determined and connected only by the properties of charged particles, and consequently only the properties of charged particles determine the electromagnetic properties of the vacuum. Particles that travel through the vacuum have another important property mass. However, this property and its magnitude are completely neglected. Our position is that the vacuum should have properties, that are connected with the mass of the particles, as well. A treatise on quantum mass theory (QMT) [4] elaborates on such properties of the vacuum. [Pg.657]

There are several inter-connections to be mentioned here. The first one concerns the extreme state. If h is the set of two particle determinants and the AGP wave function is constructed from gt, see Coleman [27] for the exact condition for the extreme state, the two-matrix (save the tail contribution from the remaining pair configurations) can be expressed as... [Pg.130]

Vaillancourt, R. D., and W. M. Balch. 2000. Size distribution of marine submicron particles determined by flow field-flow fractionation. Limnology and Oceanography 45 485-492. [Pg.213]

In the early work of Schulze ( 0, Linder and Picton (2) and Hardy (3) the sensitivity of colloidal dispersions to the addition of electrolytes was clearly demonstrated. Then in 1900 Hardy (4) showed that the stability of sols was connected with the electrophoretic mobility of the particles and he demonstrated, i) that the valency of the ion opposite in charge to that of the sol particles determined the ability of an electrolyte to coagulate a sol and that, ii) the effectiveness of the electrolyte increased rapidly with increase in valency of the counter-ion. These observations formed the basis of the so-called Schulze-Hardy rule. [Pg.38]

Consider a conical hopper flow where there is no-slip between the gas and the particle. Determine the distribution of mean stress of particles in the hopper flow. The particles can be assumed to be in a moving bed condition. [Pg.370]

Debrun, J. L., J. N. Barrandon, and P. Albert Contribution to Activation Analysis by Charged Particles Determination of Carbon and Oxygen in Pure Metals, Possibilities of Sulphur Determination. The 1968 International Con-... [Pg.90]


See other pages where Particle determinations is mentioned: [Pg.240]    [Pg.28]    [Pg.180]    [Pg.40]    [Pg.404]    [Pg.90]    [Pg.75]    [Pg.317]    [Pg.177]    [Pg.252]    [Pg.297]    [Pg.15]    [Pg.42]    [Pg.97]    [Pg.106]    [Pg.273]    [Pg.7]    [Pg.14]    [Pg.192]    [Pg.183]    [Pg.359]    [Pg.160]    [Pg.445]    [Pg.286]    [Pg.94]    [Pg.270]    [Pg.22]    [Pg.68]    [Pg.142]    [Pg.247]    [Pg.95]   
See also in sourсe #XX -- [ Pg.31 ]




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Determination of particle shape

Determination of particle size

Determination of particle size distribution by number

EXAFS particle size determination

Fraunhofer light scattering determine particle size

Magnetite particle size determinations

Number-averaged particle radius determination

Particle Size Determination from DPIs

Particle Velocity in Detonation and Its Determination

Particle coalescence, growth size, determination

Particle continued) determination

Particle diffusion coefficients determination

Particle dimensions, determination

Particle length, determination

Particle mobility, determination

Particle size determination

Particle size determination Coulter counter

Particle size determination dynamic light scattering

Particle size determination optical microscopy

Particle size determination scanning electron microscop

Particle size determination scattering techniques

Particle size determination sedimentation methods

Particle size determination test

Particle size determination transmission electron microscop

Particle size determination, electrical

Particle size determination, electrical zone sensing

Particle size determination, light scattering

Particle size determination, microscopy

Particle size determining

Particle surface potential determining ions

Particles specific heat determination

Polymer particle balances determination

Sediment particle size determination

The diffusion battery method for aerosol particle size determination

XANES particle size determination

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