Big Chemical Encyclopedia

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

Articles Figures Tables About

Particle transfer

Naturally, neither of these approximations is valid near the border between the two regions. Physically sensible are only such parameters, for which b < 1. Note that even for a low vibration frequency Q, the adiabatic limit may hold for large enough coupling parameter C (see the bill of the adiabatic approximation domain in fig. 30). This situation is referred to as strong-fiuctuation limit by [Benderskii et al. 1991a-c], and it actually takes place for heavy particle transfer, as described in the experimental section of this review. In the section 5 we shall describe how both the sudden and adiabatic limits may be viewed from a unique perspective. [Pg.71]

When an impacting particle transfers energy to a near sinface carbon atom in an amount sufficient to overcome the lattice bond energy or surface binding energy, some carbon atoms may be displaced and move in a direction defined by the angle... [Pg.412]

In addition to the trace gases, many impurities, both soluble chemicals and insoluble particles, transfer from the atmosphere to the ice sheets and have measurable concentrations in ice cores. Such measurements are a window onto the... [Pg.484]

Radakovitch O, Cherry RD, Heussner S (1999) Particulate fluxes on the Rhone continental margin (NW Mediterranean). Part III °Po and 4 b data and the particle transfer scenario. Deep-Sea Res I 46 1539-1563... [Pg.492]

Linear Energy Transfer (LET)—A measure of the energy that a charged particle transfers to a material per unit path length. [Pg.279]

The inner electrical potential 0 may consist of two components. Firstly, the phase may possess some excess electrical charge supplied from outside. This charge produces an outer electrical potential 0. This is defined as the limit of the ratio w/q for <7—>0, where w is the work expended for the infinitely slow transfer of charge q from an infinite distance to a point in the vacuum adjacent to the surface of the given phase and just outside the range of image forces. A particle transferred from this point further on in the... [Pg.157]

The acceptance criteria for the Gibbs ensemble were originally derived from fluctuation theory [17]. An approximation was implicitly made in the derivation that resulted in a difference in the acceptance criterion for particle transfers proportional to 1/N relative to the exact expressions given subsequently [18]. A full development of the statistical mechanics of the ensemble was given by Smit et al. [19] and Smit and Frenkel [20], which we follow here. A one-component system at constant temperature T, total volume V, and total number of particles N is divided into two regions, with volumes Vj and Vu = V - V, and number of particles Aq and Nu = N - N. The partition function, Q NVt is... [Pg.357]

Equation (10.7) implies that sampling is performed uniformly in the volume itself. The acceptance criterion for particle transfers, written here for transfer from region II to region I is... [Pg.358]

The same pseudo-ensemble concept has been used by Camp and Allen [44] to obtain a pseudo-Gibbs method in which particle transfers are substituted by volume fluctuations of the two phases. The volume fluctuations are unrelated to the ones required for pressure equality (10.7) but are instead designed to correct imbalances in the chemical potentials of some of the components detected, for example, by test particle insertions. [Pg.361]

While the main driving force in [43, 44] was to avoid direct particle transfers, Escobedo and de Pablo [38] designed a pseudo-NPT method to avoid direct volume fluctuations which may be inefficient for polymeric systems, especially on lattices. Escobedo [45] extended the concept for bubble-point and dew-point calculations in a pseudo-Gibbs method and proposed extensions of the Gibbs-Duhem integration techniques for tracing coexistence lines in multicomponent systems [46]. [Pg.361]

Assay preparation. Transfer not less than 20 Capsules to a blender jar or other container, and add about 150 mL of methylene chloride, and cool in a solid carbon dioxide acetone mixture until the contents have solidified. If necessary, transfer the mixture of capsules and methylene chloride to a blender jar, and blend with high-speed blender until all the solids are reduced to fine particles. Transfer the mixture to a 500-mL volumetric flask, add n-heptane to volume, mix, and allow solids to settle. Transfer an accurately measured volume of this solution, equivalent to 250 mg of valproic acid, to a 100 mL volumetric flask, dilute with w-heptane to volume, and mix. Transfer 5.0 mL to a container equipped with a closure. Add 2.0 mL of the internal standard solution, close the container, and mix. [Pg.227]

Linear energy transfer (LET) A function of the capacity of the radiation to produce ionization. LET is the rate at which charged particles transfer their energies to the atoms in a medium and a function of the energy and velocity of the charged particle. See Radiation dose. [Pg.1755]

Quantum mechanical tunneling. Tunneling is the phenomenon by which a particle transfers through a reaction barrier due to its wave-like property.Figure 1 graphically illustrates this for a carbon-hydrogen-carbon double-well system Hydrogen... [Pg.406]

Electrons, as any other charged particles, transfer their energy to the material, and through that they pass in two types of interaction ... [Pg.13]

Population transfer between sites in a lattice is a ubiquitous phenomenon in condensed matter physics. Because a lattice space has a different symmetry than does continuous space, protocols to alter the evolution of population in a lattice system with an external field must differ slightly from the protocols used for the same purpose in continuous space. With this observation in mind, Masuda and Rice extended the fast-forward protocol to apply to lattice systems and applied then-formalism to enhancing site-to-site particle transfer in a BEC [ 18]. We now briefly review that formalism. [Pg.65]

Let us now construct an atomic model for the interface reactions and particle transfer across boundaries in order to interpret such kinetic parameters introduced before as the exchange current or the interface resistance. Tb this end, we replot Figure 10-7 as shown in Figure 10-9 a. This scheme allows us to quantify the processes occurring at a stationary interface in an electric field under load. Let us further simplify the model and consider crystals with immobile anions and the interface AY/AX as shown in Figure 10-9 b. AY merely serves as a source for the injection of atomic particles (SE s) into the sublattices of AX, or as a sink for SE s arriving from... [Pg.247]

The flow pattern is such that a cocurrent spray dryer must be relatively long and small in diameter (Fig. 2), whereas a countercurrent dryer is shorter and larger in diameter. A third type, sometimes referred to as a mixed-flow dryer (Fig. 3), uses an air pattern similar to a cyclone collector, i.e., the spray is introduced at the upcoming air stream (countercurrent) and the particles transfer to the air sweeping the wall (cocurrent). [Pg.1534]

Some of the particle-transfer reactions discussed previously and included in Table II probably proceed via an intermediate association step. For example, in propylene, the probable reaction sequence is... [Pg.127]

Several Other particle-transfer reactions have larger cross sections when the reactant ions are in electronically excited states. Two systems that have been studied extensively24 37,58,79a are... [Pg.131]


See other pages where Particle transfer is mentioned: [Pg.122]    [Pg.517]    [Pg.1815]    [Pg.536]    [Pg.74]    [Pg.74]    [Pg.103]    [Pg.24]    [Pg.118]    [Pg.615]    [Pg.360]    [Pg.145]    [Pg.382]    [Pg.393]    [Pg.258]    [Pg.161]    [Pg.814]    [Pg.710]    [Pg.120]    [Pg.530]    [Pg.517]    [Pg.67]    [Pg.9]    [Pg.349]    [Pg.123]    [Pg.123]    [Pg.124]    [Pg.126]    [Pg.131]   
See also in sourсe #XX -- [ Pg.69 ]




SEARCH



Absorbing particles transfer

Chain reactions, heavy particle transfer

Chain transfer particle

Charge Transfer Processes at Semiconductor Particles

Charged particles linear energy transfer

Chemical reaction heavy particle transfer

Collision cross particle transfer

Effects of Mass Transfer Around and within Catalyst or Enzymatic Particles on the Apparent Reaction Rates

Electron Transfer Along Bridging Molecules, Molecular Wires and Semiconductor Particles Embedded in Membranes

Excited ions heavy particle transfer

Extra particle mass-transfer limitations

Fast fluidization particle convective transfer

Fluid-to-Particle Mass Transfer in a Vessel

Formed zeolite particles, mass transfer

Gas-particle heat transfer

Gas-particle heat transfer coefficient

Gas-particle mass transfer

Gas-to-particle heat transfer

Heat Transfer Coefficient at Walls, to Particles, and Overall

Heat Transfer Under Constrained Flow Past Particles, Drops, or Bubbles

Heat and Mass Transfer Coefficients for Flow around Catalyst Particles

Heat transfer between gas and particles

Heat transfer coefficient particle effects

Heat transfer coefficient particle thermal conductivity effect

Heat transfer coefficient particle-bulk fluid

Heat transfer coefficient single particle

Heat transfer inside solid particles

Heat transfer particle convective component

Heat transfer, packed beds between particles and fluids

Heat transfer, reactors between particle and fluid

Heavy particle transfer

Heavy particle transfer and the Langevin orbiting theory

Linear energy transfer particle

Lipid transfer activity particles

Lipid transfer particle

Mass Transfer to Suspensions of Small Particles

Mass and Heat Transfer to Atmospheric Particles

Mass transfer catalyst particles

Mass transfer coefficient single particle

Mass transfer fluid-particle system

Mass transfer from a fluid to the surface of particles

Mass transfer immobilized enzyme particles

Mass transfer nonspherical particle

Mass transfer particle

Mass transfer particle diffusion

Mass transfer single particles

Mass transfer spherical particle

Mass transfer to a single particle

Metal-to-particle charge-transfer

Momentum transfer between particles

Particle bombardment-mediated gene transfer

Particle convective heat transfer

Particle convective heat transfer coefficient, axial

Particle convective transfer

Particle diameter ratio, heat transfer

Particle formation mass transfer

Particle intraparticle heat transfer

Particle mass transfer coefficients

Particle properties heat transfer

Particle transfer function

Particle transfer, intermolecular vibrations

Particle-to-fluid heat transfer

Particles energy transfer

Particles heat transfer from gases

Phosphorylating electron-transferring particle

Potential energy surface heavy particle transfer

Principal Considerations Related to Energy Transfer from Charged Particles

Semiconductor particle charge transfer

Semiconductor particle charge transfer processes

Single Particle Heat Transfer Modeling for Expanded Shale Processing

Single Particle Models - Mass- and Heat-transfer Resistances

The kinetics of photoinduced interfacial charge transfer in semiconductor particles

Thermodynamics of photoinduced charge transfer in semiconductor particles

Transfer Between Particles, Drops, or Bubbles and Flows, with Volume Reaction

Transfer Processes to Single Particles

Transfer Resistance of Adsorbent Particles

Tunneling heavy particle transfer

Vibrational frequency heavy particle transfer

© 2024 chempedia.info