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Particles reaction

Figure 1 is a TEM photograph of the Cu (10wt%)/Al2O3 catalyst prepared by water-alcohol method, showing the dispersed state of copper and was confirmed the particle sizes from XRD data. Figure 2 is X-ray diffraction patterns of above-mention catalysts, was used to obtain information about phases and the particle size of prepared catalysts. Metal oxide is the active species in this reaction. Particle sizes were determined fix)m the width of the XRD peaks by the Debye-Scherrer equation. [Pg.303]

Figure 5.6 Scanning electron microscopy images of a silica-entrapped palladium catalyst amenable for a variety of C-C forming reactions (particle sizes are from 60 to 125 pm). Figure 5.6 Scanning electron microscopy images of a silica-entrapped palladium catalyst amenable for a variety of C-C forming reactions (particle sizes are from 60 to 125 pm).
In either group of electrode reactions, the energy level of reacting particles (electrons or ions) in the electrode depends linearly on the electrode potential. Hence, the reaction afiinily (A = — AG) can be varied over a wide range by simply controlling the electrode potential. This is one of the characteristics of electrode reactions, in contrast with ordinary chemical reactions whose affinity can be varied in a relatively narrow range by controlling the temperature and the concentration of reaction particles. [Pg.213]

The reaction path from the initial state to the final state of an elementary step is represented by the potential eneigy curves of the initial and final states of a reacting particle as shown in Fig. 7-6, where the reaction coordinate x denotes the position of a reaction particle moving across a compact double layer on the electrode interface. [Pg.221]

The reaction order is a kinetic parameter representing the effect of the activity of a reaction particle on the reaction rate and is used to elucidate the mechanism of the reaction. The reaction order, Ck, with respect to a particle k is defined in Eqn. 7-34 ... [Pg.225]

The dipole moments of activated complexes in reactions of chain propagation and termination calculated from the data of Figure 2, using Equations 2a and 3a, are (n )2 = (8.1 0.1) debyes and (/x )6 = (11.1 0.1) debyes. This is consistent with the dipole moments of activated complexes we calculated for two possible structures of the activated complex (7, 10). Thus, the variations in k2 and kQ constants with methyl ethyl ketone dilution by benzene agree with the concept of strictly electrostatic interaction between the solvent and the reaction particles. [Pg.166]

Chemical reactions are classified usually as diffusion-controlled, whose rate is limited by a reactant spatial approach to each other, and reaction-controlled (kinetic stage), whose rate is limited by a reaction elementary event. For systems with ideal reactant mixing considered in Section 2.1.1, there is no mechanism of reactant mutual approach. On the other hand, the kinetic equations (2.1.40) distinguish between reaction in physically infinitesimal volumes and the distant reactant motion in a whole reaction volume. In the absence of reaction particle diffusion is described by equation... [Pg.69]

Luminescence in Charge-Transfer and Ion-Molecule Reactions Ion-Molecule Reactions (Particle Transfer)... [Pg.176]

For gas-solid heterogeneous reactions particle size and average pore diameter will influence the reaction rate per unit mass of solid when internal diffusion is a significant factor in determining the rate. The actual mode of transport within the porous structure will depend largely on the pore diameter and the pressure within the reactor. Before developing equations which will enable us to predict reaction rates in porous solids, a brief consideration of transport in pores is pertinent. [Pg.111]

Figure 7. A spectrum of particles resulting from nuclear reactions and scattering from a thick Si3Ni standard. Conditions 2H ions normally incident at an energy of 1.41 MeV, and resulting reaction particles detected at a 165° angle by a surface-barrier diode detector. The particle group marked a, is from the 14N(d,a)i2C reaction and is used to profile N in samples. Figure 7. A spectrum of particles resulting from nuclear reactions and scattering from a thick Si3Ni standard. Conditions 2H ions normally incident at an energy of 1.41 MeV, and resulting reaction particles detected at a 165° angle by a surface-barrier diode detector. The particle group marked a, is from the 14N(d,a)i2C reaction and is used to profile N in samples.
Figure 9. A partial spectrum of a particles resulting from the 12C(3He,a0)nC reaction as applied to a Ti6Al4V alloy sample implanted with 3 X 1017 I2C atoms/cm2 at 75 keV. Conditions 3He ions normally incident at an energy of 2.775 MeV, and resulting reaction particles detected at a 135° angle with a magnetic spectrometer. The higher energy peak is due to surface contamination and is resolved from the implanted distribution. (Reproduced, with permission, from Ref. 5. Copyright, North-Holland Publishing Co.)... Figure 9. A partial spectrum of a particles resulting from the 12C(3He,a0)nC reaction as applied to a Ti6Al4V alloy sample implanted with 3 X 1017 I2C atoms/cm2 at 75 keV. Conditions 3He ions normally incident at an energy of 2.775 MeV, and resulting reaction particles detected at a 135° angle with a magnetic spectrometer. The higher energy peak is due to surface contamination and is resolved from the implanted distribution. (Reproduced, with permission, from Ref. 5. Copyright, North-Holland Publishing Co.)...
Tn is the bulk melting temperature, 7 and p are the surface energy and the density of the solid phase and the liquid phase noted by the subscripts s and 1 and L is the latent heat of fusion. This phenomenon is due to the increase in the fraction of surface atoms. The Pawlow law is verified experimentally for particles larger than 5 nm and more sophisticated thermodynamic models have been developed which can be applied down to 2-nm particles [54]. During catal 4ic reactions, particles are generally solid, but in the case of carbon nanotubes synthesized by CVD, the catalyst particles could melt at temperatures lower than the bulk melting point. [Pg.254]

Prefer monolithic confignration for intensification with surface area/volume usually 1.5 to 4 times greater than traditional pellets. Excellent for mass transfer controlled reactions. For gas reacting with solid nsnally heat transfer controlled, because these are highly exothermic or endothermic reactions. Particle size and size distribution are critical. These reactions may follow different patterns ... [Pg.1411]

At the end of the precipitation reaction, the solid particles must be colloidally stable if a uniform particle-size distribution is to be observed. A question important to final uniformity is the particle size when this stability is achieved. The particles will always feel the long-range van der Waals attractive interactions. Interactions of an electrostatic or solvation origin can give rise to a repulsive barrier that can provide kinetic stabilization. At the end of the reaction, particles precipitated from TEOS and titanium alkoxides have final particle number densities, N , of 1016—1018 m-3. These particles are suspended in a solvent with an ionic strength of approximately 10-4 M and have surface potentials of 10-35 mV. Our studies indicate that the particles also feel a short-range repulsive interaction that we have modeled as a solvation interaction with decay... [Pg.444]

Particle Geometry Largely Unaffected by Reaction Particle Geometry Strongly Affected by Reaction... [Pg.422]

The first sum goes over all target elements i, while the index k in the second sum represents the reaction particle type (primary or secondary proton, secondary neutron). Na is Avogadro s number, Ai the mass number (in amu) of the target element i, q the... [Pg.130]

What is a nuclear transformation How do you balance nuclear transformation reactions Particle accelerators are used to perform nuclear transformations. What is a particle accelerator ... [Pg.900]

Column 2 gives the binding energy of a proton in the compound nucleus. Columns 5, 6 give observed Q-values in MeV, taken mainly from reference [31]. Column 7 gives other reactions observed, a means that the reaction has been observed by detection of activity, p that the reaction particles have been observed. [Pg.66]


See other pages where Particles reaction is mentioned: [Pg.137]    [Pg.171]    [Pg.242]    [Pg.234]    [Pg.386]    [Pg.175]    [Pg.16]    [Pg.231]    [Pg.65]    [Pg.215]    [Pg.639]    [Pg.16]    [Pg.2040]    [Pg.213]    [Pg.1671]    [Pg.1411]    [Pg.313]    [Pg.260]    [Pg.69]    [Pg.71]    [Pg.453]    [Pg.453]    [Pg.566]    [Pg.1010]    [Pg.568]    [Pg.78]    [Pg.1131]    [Pg.70]   
See also in sourсe #XX -- [ Pg.65 ]

See also in sourсe #XX -- [ Pg.219 ]




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A stochastic model for surface reactions including energetic particle interactions

ATMOSPHERIC FATES OF PARTICLE-ASSOCIATED PAHs HETEROGENEOUS REACTIONS

Activation analysis charged particle reactions

Atmospheric Chemical Reactions Involving Particles

Chain reactions, heavy particle transfer

Charged-particle-induced reactions

Chemical Reaction and Diffusion inside a Catalyst Particle

Chemical reaction heavy particle transfer

Colloidal particles chemical reactions

Correlation between Metal Particle Size and Reaction Mechanisms

Dispersed porous particles reaction kinetics

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

Extension to Other Reaction Orders and Particle Geometries

FLUIDIZED-BED AND OTHER MOVING-PARTICLE REACTORS FOR FLUID-SOLID REACTIONS

Fluid-Particle Reactions Kinetics

Formation of atmospheric aerosol particles by chemical reaction and condensation

Gas - Particle Reactions

Neutron Detection by (n, Charged Particle) Reaction

Nonporous particle reactions

Nuclear Reaction Analysis and Particle-Induced Gamma-Ray Emission

Nuclear bombardment reactions using particle accelerators

Nuclear reactions charged-particle

Particle board reactions

Particle formation reaction controlled processes

Particle-scale apparent reaction rate

Particles, Drops, and Bubbles. Arbitrary Rate of Reaction

Particles, Drops, and Bubbles. First-Order Reaction

Particles, fundamental decay reactions

Particles, heterogeneous reactions

Photochemical Reactions of Particle-Associated PAHs

Polymerization reactions, heavy particle

Porous particles reactions

Rate of Reaction for Shrinking Spherical Particles

Reaction Inside Nonisothermal Particles

Reaction Kinetics of Carbon Particles

Reaction Routes at Small and Big Particles

Reaction and Diffusion in a Catalyst Particle

Reaction immobile particles

Reaction kinetics and particle

Reaction kinetics particles

Reaction of immobile particles

Reaction parameters catalyst particle size

Reaction rate catalyst particle size effect

Reactions Involving Highly-Excited Neutral Particles. Hot Atoms

Reactions of Gases at Particle Surfaces

Reactions of Nonporous Particles

Reactions of Porous Particles

Reactions of alpha particles with light nuclei

Reactions, colloidal model particles from

Shale particles, chemical reactions

Solid-state reactions particle size

The A B - C reaction. Stochastic particle generation

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

Tribocorrosion particle-surface reactions

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