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Activation process

From stochastic molecnlar dynamics calcnlations on the same system, in the viscosity regime covered by the experiment, it appears that intra- and intennolecnlar energy flow occur on comparable time scales, which leads to the conclnsion that cyclohexane isomerization in liquid CS2 is an activated process [99]. Classical molecnlar dynamics calcnlations [104] also reprodnce the observed non-monotonic viscosity dependence of ic. Furthennore, they also yield a solvent contribntion to the free energy of activation for tlie isomerization reaction which in liquid CS, increases by abont 0.4 kJ moC when the solvent density is increased from 1.3 to 1.5 g cm T Tims the molecnlar dynamics calcnlations support the conclnsion that the high-pressure limit of this unimolecular reaction is not attained in liquid solntion at ambient pressure. It has to be remembered, though, that the analysis of the measnred isomerization rates depends critically on the estimated valne of... [Pg.860]

Figure A3.8.3 Quantum activation free energy curves calculated for the model A-H-A proton transfer reaction described 45. The frill line is for the classical limit of the proton transfer solute in isolation, while the other curves are for different fully quantized cases. The rigid curves were calculated by keeping the A-A distance fixed. An important feature here is the direct effect of the solvent activation process on both the solvated rigid and flexible solute curves. Another feature is the effect of a fluctuating A-A distance which both lowers the activation free energy and reduces the influence of the solvent. The latter feature enliances the rate by a factor of 20 over the rigid case. Figure A3.8.3 Quantum activation free energy curves calculated for the model A-H-A proton transfer reaction described 45. The frill line is for the classical limit of the proton transfer solute in isolation, while the other curves are for different fully quantized cases. The rigid curves were calculated by keeping the A-A distance fixed. An important feature here is the direct effect of the solvent activation process on both the solvated rigid and flexible solute curves. Another feature is the effect of a fluctuating A-A distance which both lowers the activation free energy and reduces the influence of the solvent. The latter feature enliances the rate by a factor of 20 over the rigid case.
The combination of electrochemistry and photochemistry is a fonn of dual-activation process. Evidence for a photochemical effect in addition to an electrochemical one is nonnally seen m the fonn of photocurrent, which is extra current that flows in the presence of light [, 89 and 90]. In photoelectrochemistry, light is absorbed into the electrode (typically a semiconductor) and this can induce changes in the electrode s conduction properties, thus altering its electrochemical activity. Alternatively, the light is absorbed in solution by electroactive molecules or their reduced/oxidized products inducing photochemical reactions or modifications of the electrode reaction. In the latter case electrochemical cells (RDE or chaimel-flow cells) are constmcted to allow irradiation of the electrode area with UV/VIS light to excite species involved in electrochemical processes and thus promote fiirther reactions. [Pg.1945]

The reaction mechanisms of plasma polymerization processes are not understood in detail. Poll et al [34] (figure C2.13.6) proposed a possible generic reaction sequence. Plasma-initiated polymerization can lead to the polymerization of a suitable monomer directly at the surface. The reaction is probably triggered by collisions of energetic ions or electrons, energetic photons or interactions of metastables or free radicals produced in the plasma with the surface. Activation processes in the plasma and the film fonnation at the surface may also result in the fonnation of non-reactive products. [Pg.2807]

Information about critical points on the PES is useful in building up a picture of what is important in a particular reaction. In some cases, usually themially activated processes, it may even be enough to describe the mechanism behind a reaction. However, for many real systems dynamical effects will be important, and the MEP may be misleading. This is particularly true in non-adiabatic systems, where quantum mechanical effects play a large role. For example, the spread of energies in an excited wavepacket may mean that the system finds an intersection away from the minimum energy point, and crosses there. It is for this reason that molecular dynamics is also required for a full characterization of the system of interest. [Pg.254]

The observation that in the activated complex the reaction centre has lost its hydrophobic character, can have important consequences. The retro Diels-Alder reaction, for instance, will also benefit from the breakdown of the hydrophobic hydration shell during the activation process. The initial state of this reaction has a nonpolar character. Due to the principle of microscopic reversibility, the activated complex of the retro Diels-Alder reaction is identical to that of the bimoleciilar Diels-Alder reaction which means this complex has a negligible nonpolar character near the reaction centre. O nsequently, also in the activation process of the retro Diels-Alder reaction a significant breakdown of hydrophobic hydration takes placed Note that for this process the volume of activation is small, which implies that the number of water molecules involved in hydration of the reacting system does not change significantly in the activation process. [Pg.168]

We conclude that the beneficial effects of water are not necessarily limited to reactions that are characterised by a negative volume of activation. We infer that, apart from the retro Diels-Alder reaction also other reactions, in which no significant reduction or perhaps even an increase of solvent accessible surface area takes place, can be accelerated by water. A reduction of the nonpolar nature during the activation process is a prerequisite in these cases. [Pg.168]

In the case of the retro Diels-Alder reaction, the nature of the activated complex plays a key role. In the activation process of this transformation, the reaction centre undergoes changes, mainly in the electron distributions, that cause a lowering of the chemical potential of the surrounding water molecules. Most likely, the latter is a consequence of an increased interaction between the reaction centre and the water molecules. Since the enforced hydrophobic effect is entropic in origin, this implies that the orientational constraints of the water molecules in the hydrophobic hydration shell are relieved in the activation process. Hence, it almost seems as if in the activated complex, the hydrocarbon part of the reaction centre is involved in hydrogen bonding interactions. Note that the... [Pg.168]

If the fraction of sites occupied is 0, and the fraction of bare sites is 0q (so that 00 + 1 = 0 then the rate of condensation on unit area of surface is OikOo where p is the pressure and k is a constant given by the kinetic theory of gases (k = jL/(MRT) ) a, is the condensation coefficient, i.e. the fraction of incident molecules which actually condense on a surface. The evaporation of an adsorbed molecule from the surface is essentially an activated process in which the energy of activation may be equated to the isosteric heat of adsorption 4,. The rate of evaporation from unit area of surface is therefore equal to... [Pg.42]

Intrinsic Kinetics. Chemisorption may be regarded as a chemical reaction between the sorbate and the soHd surface, and, as such, it is an activated process for which the rate constant (/ ) follows the familiar Arrhenius rate law ... [Pg.257]

Micropore Diffusion. In very small pores in which the pore diameter is not much greater than the molecular diameter the diffusing molecule never escapes from the force field of the pore wall. Under these conditions steric effects and the effects of nonuniformity in the potential field become dominant and the Knudsen mechanism no longer appHes. Diffusion occurs by an activated process involving jumps from site to site, just as in surface diffusion, and the diffusivity becomes strongly dependent on both temperature and concentration. [Pg.258]

Subsequent studies (63,64) suggested that the nature of the chemical activation process was a one-electron oxidation of the fluorescer by (27) followed by decomposition of the dioxetanedione radical anion to a carbon dioxide radical anion. Back electron transfer to the radical cation of the fluorescer produced the excited state which emitted the luminescence characteristic of the fluorescent state of the emitter. The chemical activation mechanism was patterned after the CIEEL mechanism proposed for dioxetanones and dioxetanes discussed earher (65). Additional support for the CIEEL mechanism, was furnished by demonstration (66) that a linear correlation existed between the singlet excitation energy of the fluorescer and the chemiluminescence intensity which had been shown earher with dimethyl dioxetanone (67). [Pg.266]

Catalyst CAS Registry Number Activator Processing temperature, °C... [Pg.319]

A sulfur condenser follows the reactor. These processes, ie, Superclaus or Parson s Hi-Activity process, can boost the overall sulfur recovery to up to 99.2%. [Pg.213]

The metaboHsm of a material may result in the formation of a transformation product of lower intrinsic toxicity than the parent molecule ie, a process of detoxification has occurred. In other cases, the end result is a metaboHte, or metaboHtes, of intrinsically greater toxicity than the parent molecule, ie, metaboHc activation has occurred. Some examples of detoxification and metaboHc-activation processes are given in Table 2. [Pg.230]

Activation Processes. To be useful ia battery appHcations reactions must occur at a reasonable rate. The rate or abiUty of battery electrodes to produce current is determiaed by the kinetic processes of electrode operations, not by thermodynamics, which describes the characteristics of reactions at equihbrium when the forward and reverse reaction rates are equal. Electrochemical reaction kinetics (31—35) foUow the same general considerations as those of bulk chemical reactions. Two differences are a potential drop that exists between the electrode and the solution because of the electrical double layer at the electrode iaterface and the reaction that occurs at iaterfaces that are two-dimensional rather than ia the three-dimensional bulk. [Pg.511]

For an ion to move through the lattice, there must be an empty equivalent vacancy or interstitial site available, and it must possess sufficient energy to overcome the potential barrier between the two sites. Ionic conductivity, or the transport of charge by mobile ions, is a diffusion and activated process. From Fick s Law, J = —D dn/dx), for diffusion of a species in a concentration gradient, the diffusion coefficient D is given by... [Pg.351]

Electrical conduction ia glasses is mainly attributed to the migration of mobile ions such as LE, Na", K", and OH under the influence of an appHed field. At higher temperatures, >250° C, divalent ions, eg, Ca " and Mg ", contribute to conduction, although their mobiUty is much less (14). Conduction ia glass is an activated process and thus the number of conducting ions iacreases with both temperature and field. The temperature—resistivity dependence is given... [Pg.356]

A wide range of clay materials have been used for decolorizing. These may be substantially cmde clay such as fuller s earth, which largely contains montmorillonite as the active clay ingredient, or specially treated attapulgites, montmorillonites, and kaolinites. Proprietary acid activation processes are frequentiy used for production of clay-derived materials of superior performance. [Pg.210]

Catalytic Oxidization. A principal technology for control of exhaust gas pollutants is the catalyzed conversion of these substances into innocuous chemical species, such as water and carbon dioxide. This is typically a thermally activated process commonly called catalytic oxidation, and is a proven method for reducing VOC concentrations to the levels mandated by the CAAA (see Catalysis). Catalytic oxidation is also used for treatment of industrial exhausts containing halogenated compounds. [Pg.502]


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1,2-Diarylethylenes activated processes

Activated Benfield process

Activated alumina process, regenerant

Activated carbon process

Activated carbons preparation process

Activated dough development process

Activated hopping process

Activated magnesia process

Activated process

Activated process models, yield stresses

Activated processes, course content

Activated rate processes

Activated sludge process

Activated sludge process design parameters

Activated sludge process kinetics

Activated sludge process microbiology

Activated sludge process operational problems

Activated sludge processes, wastewater

Activated swelling process

Activation as a process Implementation and governance

Activation control, anodic partial process

Activation control, leveling process

Activation controlled partial processes

Activation controlled processes

Activation energies of the relaxation process

Activation energy controlled process

Activation energy dehydration processes

Activation energy desorption process

Activation energy processes

Activation free energy heterogeneous processes

Activation free energy irreversible process

Activation in Heck-type processes

Activation process thermodynamic constants

Activation, reversible processes

Activation-deactivation processes

Activation-deactivation processes equilibrium constant

Activators mineral processing

Active Rotaxanes as Processive Enzyme Mimics

Active conservation treatment processes

Active ingredient bleach processing

Active metal brazing process

Active pharmaceutical ingredient milling process

Active pharmaceutical ingredient primary processes

Active pharmaceutical ingredient process characterization

Active pharmaceutical ingredient process optimization

Active pharmaceutical ingredient process qualification

Active pharmaceutical ingredients continuous processes

Active pharmaceutical ingredients crystallization process

Active pharmaceutical ingredients process development

Active pharmaceutical ingredients process integration

Active process

Actively caring decision process

Activity process

Addition of Active C-H compounds to Dienes the Rhone-Poulenc Process for Geranylacetone

Amorphous activation process

Apoptosis active process

Apparent Activation Energy of a Stepwise Process

Arrhenius activation process

Aseptic processing activity

Aseptic processing manufacturing activities

Batch process control activity model

Behavioral safety process: activities

Biotransformation processes metabolic activation

C-H Activation Reactions in Domino Processes

C-H activation processes

C-H bond activation processes

Calcium ion activation of metabolic processes

Carbon, activated removal processes

Cascade Processes Initiated by Conjugate Addition via Enamine Activation

Cascade Processes Initiated by Conjugate Addition via H-bonding Activation

Cascade Processes Initiated by Conjugate Addition via Other Mechanisms of Activation

Catalysis, photochemical activation process

Cell activation processes

Chemical activation process

Cholinergic receptors activation process

Collisional activation process

Conventional activated sludge process

Creep and stress relaxations as thermally activated processes

Diffusion Activated process

Diffusion activated rate process

Diffusion multi-activation process

Dopamine activation process

Enzyme activity modeling intracellular processe

First-order processes active transport

Fluidized activated carbon process

Heck-Type Processes Involving C-H Activation

Heterogeneous process activation energy

Heterogeneous process reductive activation

High-activity processes

Human Activities as Geochemical Processes

Hydrogen spillover activated process

Industrial activities processes

Instrumental neutron activation process

Isotherm activation processes

Liver enzyme, activation process

Living radical polymerization activation-deactivation processes

Low-activity processes

Membrane bioreactor activated sludge process

Membrane bioreactors activated sludge process

Mesoscopic Non-Equilibrium Thermodynamics of Activated Processes

Muscarinic cholinergic receptors activation process

Nephron active transport processes

Neutron activation analysis nuclear processes

New Processes for Existing Active Compounds

Nicotinic cholinergic receptors activation process

Oxidation photochemical activation process

Oxidation-reduction reaction activation process

Oxygen Activation for Fuel Cell and Electrochemical Process Applications

Pharmaceuticals process validation active pharmaceutical ingredients

Physical/thermal activation process

Physical/thermal activation process considerations

Physical/thermal activation process mechanisms

Physical/thermal activation process porous materials

Physical/thermal activation process rates

Physical/thermal activation process temperature coefficients

Plug-flow activated sludge process

Process Development Activities

Process engineer, role Activity analysis

Process parameters effective activation energy

Process synthesis tissue plasminogen activator

Process, continuous active

Processes, Solvents, and Methods of Activation

Processing Thermally activated

Processing facilities active

Processing temperature, activation

Processing times, activation index

Protein engineering process using sequence activity

Receptor activation, molecular processes

Repetitive activation processes)

Reversible chain transfer catalyzed activation processes

Risk assessment process activities

Sludge process, extended, activated

Sodium hydroxide activation process

Solution-diffusion mechanism activated process

Steam active reforming process

Stress relaxation as thermally activated process

Temperature-activation process

The Activation Process

Thermally activated process

Thermally activated processes, rate

Tissue plasminogen activator process

Transition metal complexes intermolecular activation processes

Waste activation process

Wastewater treatment activated sludge process

Water activity food processing

Yield as an Activated Rate Process

Yield as an activated rate process the Eyring equation

Zero-order processes active transport

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