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Reaction limitation

Chlorination of Methane. Methane can be chlorinated thermally, photochemicaHy, or catalyticaHy. Thermal chlorination, the most difficult method, may be carried out in the absence of light or catalysts. It is a free-radical chain reaction limited by the presence of oxygen and other free-radical inhibitors. The first step in the reaction is the thermal dissociation of the chlorine molecules for which the activation energy is about 84 kj/mol (20 kcal/mol), which is 33 kJ (8 kcal) higher than for catalytic chlorination. This dissociation occurs sufficiendy rapidly in the 400 to 500°C temperature range. The chlorine atoms react with methane to form hydrogen chloride and a methyl radical. The methyl radical in turn reacts with a chlorine molecule to form methyl chloride and another chlorine atom that can continue the reaction. The methane raw material may be natural gas, coke oven gas, or gas from petroleum refining. [Pg.514]

Griskey (5) and Chen 6) studied the reaction of nylon 6,6 and 6,10 in a SPP in a stream of dry nitrogen in the temperature range of 90 - 180°C. They found that the reaction limiting step... [Pg.137]

If the reaction order does not change, reactions with n < 1 wiU go to completion in finite time. This is sometimes observed. Solid rocket propellants or fuses used to detonate explosives can bum at an essentially constant rate (a zero-order reaction) until all reactants are consumed. These are multiphase reactions limited by heat transfer and are discussed in Chapter 11. For single phase systems, a zero-order reaction can be expected to slow and become first or second order in the limit of low concentration. [Pg.46]

The indication for venom immunotherapy is based on a history of systemic allergic reactions to Hymenoptera stings and positive diagnostic tests, skin tests and/or venom-specific serum IgE antibodies [45, 49]. In the presence of only mild systemic allergic reactions, limited to the skin, immunotherapy is not generally recommended in the USA not for children, in Europe not for children and adults, unless they are heavily exposed and had repeated such reactions. [Pg.153]

In order to confirm the proposed mechanism described above, in which O2 may have a positive effect on NO absorption, the comparative experiments have been carried out. The results are shown in Fig. 1, from which one can see that the presence of O2 will greatly improve the NO removal performance. In the absence of O2, NO coordination occurs according to Eq. (2), a reversible reaction limited by equilibrium, the NO removal decreases from the initial 100% to about 60% in one hour. In the presence of O2 however, contribution of Eq. (2) is little, the most coordination of NO is certainly attributed to the cascade reactions from Eq.(3) to Eq.(6), and the final reaction of Eq. (7), which will not be constrained by the reaction equilibrium, and thus the NO removal can be maintained 100% in 2-3 hours. [Pg.231]

In a similar way, electrochemistry may provide an atomic level control over the deposit, using electric potential (rather than temperature) to restrict deposition of elements. A surface electrochemical reaction limited in this manner is merely underpotential deposition (UPD see Sect. 4.3 for a detailed discussion). In ECALE, thin films of chemical compounds are formed, an atomic layer at a time, by using UPD, in a cycle thus, the formation of a binary compound involves the oxidative UPD of one element and the reductive UPD of another. The potential for the former should be negative of that used for the latter in order for the deposit to remain stable while the other component elements are being deposited. Practically, this sequential deposition is implemented by using a dual bath system or a flow cell, so as to alternately expose an electrode surface to different electrolytes. When conditions are well defined, the electrolytic layers are prone to grow two dimensionally rather than three dimensionally. ECALE requires the definition of precise experimental conditions, such as potentials, reactants, concentration, pH, charge-time, which are strictly dependent on the particular compound one wants to form, and the substrate as well. The problems with this technique are that the electrode is required to be rinsed after each UPD deposition, which may result in loss of potential control, deposit reproducibility problems, and waste of time and solution. Automated deposition systems have been developed as an attempt to overcome these problems. [Pg.162]

However, if we set the furnace temperature just slightly greater than T2, we would obtain a reaction limited to that of A - B, and thus could identily the intermediate reaction product, B. This technique is called isothermal thermogravimetry. Thus, we can follow a solid state reaction by first surveying via d3mamic TGA. If there are any intermediate products, we can isolate each in turn, and after cooling (assmning each is stable at room temperature) cam identify it by x-ray analysis. Note that we can obtain an assay easily ... [Pg.385]

Let us illustrate first how different (idealized) aggregation processes may result in different structures. There is extensive literature on diffusion-limited aggregation (DLA) (for a comprehensive review, see Meakin, 1988). Three methods of simulation are common (standard) diffusion-limited aggregation (DLA), reaction-limited aggregation (RLA), and linear trajectory aggregation (LTA). DLA structures are generated by placing a seed particle in the middle of a lattice. Other particles are placed in the lattice... [Pg.180]

Fig. 37. Typical clusters obtained by diffusion-limited aggregation (DLA). Top Two-dimensional diffusion-limited aggregation. Bottom Reaction-limited hierarchical cluster-cluster aggregation (HCCA) (Meakin, 1988 with permission, from the Annual Review of Physical Chemistry, Vol. 39. by Annual Reviews www.Annual/Reviews.org). Fig. 37. Typical clusters obtained by diffusion-limited aggregation (DLA). Top Two-dimensional diffusion-limited aggregation. Bottom Reaction-limited hierarchical cluster-cluster aggregation (HCCA) (Meakin, 1988 with permission, from the Annual Review of Physical Chemistry, Vol. 39. by Annual Reviews www.Annual/Reviews.org).
In situ SAXS investigations of a variety of sol-gel-derived silicates are consistent with the above predictions. For example, silicate species formed by hydrolysis of TEOS at pH 11.5 and H20/Si = 12, conditions in which we expect monomers to be continually produced by dissolution, are dense, uniform particles with well defined interfaces as determined in SAXS experiments by the Porod slope of -4 (non-fractal) (Brinker, C. J., Hurd, A. J. and Ward, K. D., in press). By comparison, silicate polymers formed by hydrolysis at pH 2 and H20/Si = 5, conditions in which we expect reaction-limited cluster-cluster aggregation with an absence of monomer due to the hydrolytic stability of siloxane bonds, are fractal structures characterized by D - 1.9 (Porod slope — -1.9) (29-30). [Pg.319]

The hydrogenation of para-substituted anilines over rhodium catalysts has been investigated. An antipathetic metal crystallite size effect was observed for the hydrogenation of /Moluidinc suggesting that terrace sites favour the reaction. Limited evidence was found for catalyst deactivation by the product amines. Catalysts with pore diameters less than 13.2 nm showed evidence of diffusion control on the rate of reaction but not the cis trans ratio of the product. [Pg.77]

Fig. 3. Variation of autocorrelation function with changes in the equilibrium constant in the fast reaction limit. A and B have different diffusion coefficients but the same optical (fluorescence) properties. This figure illustrates how, for the simple isomerization process, A B, a change in the diffusion coefficient is sufficient to indicate the progress of the reaction. This example is calculated for a two-dimensional (planar) system in the fast reaction limit (kf + k ) 4Dj /w2. Therefore, only a single diffusion process is... Fig. 3. Variation of autocorrelation function with changes in the equilibrium constant in the fast reaction limit. A and B have different diffusion coefficients but the same optical (fluorescence) properties. This figure illustrates how, for the simple isomerization process, A B, a change in the diffusion coefficient is sufficient to indicate the progress of the reaction. This example is calculated for a two-dimensional (planar) system in the fast reaction limit (kf + k ) 4Dj /w2. Therefore, only a single diffusion process is...
Rate Expressions for Heterogeneous Catalytic Reactions Limited by the Rates of Chemical Processes... [Pg.182]

This reaction is always in competition with the deNOx reaction, limiting the maximum of NOx conversion to N2. It must be pointed out that, during the TPSR tests performed... [Pg.282]

Styrene is reported to undergo reduction upon treatment with trifluoroacetic acid and triethylsilane,203 although competing polymerization reactions limit the yield of ethylbenzene to only 30% (Eq. 63).70 Vinylcyclopropane is reduced to ethylcy-clopropane within 30 minutes under similar conditions (Eq. 64) 232 It is important to note that the cyclopropane ring of ethylcyclopropane can be opened under these reaction conditions, albeit with longer reaction times, to give some trans-2-pentene in the final reaction mixture.233... [Pg.35]

Reactions Limited by Rotational Diffusion in Polymer Matrix... [Pg.13]

When the rate of initiation is very low the important moment of chain reaction becomes the kinetics of the establishment of the stationary concentration of free radicals. This time is comparable with the lifetime of the radical that reaction limits the chain propagation. The... [Pg.204]

Of these reactions, the reaction of the peroxyl radical with phosphite is the slowest. The rate constant of this reaction ranges from 102 to 103 L mol 1 s 1 which is two to three orders of magnitude lower than the rate constant of similar reactions with phenols and aromatic amines. Namely, this reaction limits chain propagation in the oxidation of phosphites. Therefore, the chain oxidation of trialkyl phosphites involves chain propagation reactions with the participation of both peroxyl and phosphoranylperoxyl radicals ... [Pg.599]

Therefore, the ability of (530a) to be involved in [4+ 2]-cycloaddition reactions with some olefins and dienes is very important in dihydrooxazines chemistry, although the ene reactions limit the use of this nitrosoalkene in organic synthesis. [Pg.712]


See other pages where Reaction limitation is mentioned: [Pg.1930]    [Pg.2685]    [Pg.80]    [Pg.4]    [Pg.473]    [Pg.719]    [Pg.166]    [Pg.325]    [Pg.49]    [Pg.18]    [Pg.67]    [Pg.344]    [Pg.401]    [Pg.483]    [Pg.496]    [Pg.1473]    [Pg.175]    [Pg.319]    [Pg.121]    [Pg.122]    [Pg.170]    [Pg.52]    [Pg.471]    [Pg.184]    [Pg.174]   
See also in sourсe #XX -- [ Pg.211 ]

See also in sourсe #XX -- [ Pg.19 ]




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A Continuous Reaction-Limited Dissolution Model

A Discrete Reaction-Limited Dissolution Model

A typical branched chain reaction showing explosion limits

Acid-Base Reactions Affecting the Limiting Current

Activation-limited reaction

Aggregation reaction-limited

Aggregation reaction-limited, computer

Aromatic compounds Friedel-Crafts reactions, limitations

Catalytic reaction steps rate-limiting step

Catalytic reactions rate limiting steps

Chain-limiting reactions

Chemical reaction processes limitations

Chemical reaction processes process operating limits

Chemical reactions detection limits

Chemical reactions limiting reactant

Chemical reactions, kinetics high-pressure limit

Cluster aggregation, diffusionlimited/reaction-limited

Colloidal reaction-limited aggregation

Competitive-consecutive reactions limiting cases

Consecutive reactions diffusion limited

Dense (non-porous) membranes and surface reaction limitation

Detection limit enzymatic reaction

Diffusion controlled limit, reaction

Diffusion mass transfer-limited reactions

Diffusion-controlled limit on reaction rate

Diffusion-limited reactions

Diffusion-limited reactions, Smoluchowski equation

Diffusion-limited surface reaction

Discrete, reaction-limited dissolution process

El reaction rate-limiting step

ElcB reaction rate-limiting step

Electrophilic substitution reaction limitations

Energy transfer limited reactions

Enzyme reactions rate limiting transformation

Epoxide reactions limiting mechanism

Equilibrium, chemical/reaction limitations

Equilibrium-limited reaction

Equilibrium-limited reaction systems

Explosion limits sensitized reaction

Facilitated diffusion fast reaction limit

Fischer esterification reaction limitations

Fischer-Tropsch reaction chain growth limit

Fluid—solid reactions limitations

Friedel-Crafts alkylation reaction limitations

Friedel-Crafts reaction, acylation limitations

Friedel-Crafts reactions, limitations

Grignard reaction limitations

Grignard reaction, aldehydes and limitations

Heck reaction chain-limiting reactions

Intramolecular reactions limitations

Ionic reactions, limiting quantities

Irreversible surface-reaction-limited

Irreversible surface-reaction-limited rate laws

Is the Surface Reaction Rate-Limiting

Isodesmic reaction limitations using

Kinetic expressions derived for diffusion limited reactions

Kinetics and Mass Transfer Limitations of the Electrode Reaction

Knoevenagel reaction limitation

Limitation of reaction

Limitation on reaction

Limitation on reaction rate

Limitation, in multiscale reaction networks

Limitations of Friedel-Crafts Reactions

Limitations on Electrophilic Substitution Reactions with Substituted Benzenes

Limitations on non-steady-state kinetic behaviour imposed by the reaction mechanism

Limiting Unimolecular Nucleophilic Reactions—Effects of Structure and Solvent

Limiting current, electrochemical reactions

Limiting reactant chemical reactions involving

Limiting reactant reaction yield

Limiting reactant, reaction kinetics

Limiting-current measurement electrochemical reactions used

Limiting-current measurement redox reaction

Limiting-reactant problem reaction table

Limiting-reactant problem solving for reaction in solution

Liquid phase component transport limited reactions

Mannich reaction limitations

Mass transfer limitation on reaction

Mass transfer limited reactions

Metabolic pathways rate-limiting reactions

Molecular Design Limited Reactions Databases

Multiphasic Reactions General Features, Scope, and Limitations

Neutron irradiation reactions limitations

Oscillatory reactions rate-limiting mechanisms

Oxygen reduction reaction limiting diffusion current densities

Parallel reactions limiting cases

Photocyclization reactions, limitations

Polymerase chain reaction detection limits

Process reaction-limited

Propagation reactions Limiting monomer conversion

Rate expression, adsorption limiting reversible reaction

Rate-limiting enzyme reaction

Rate-limiting reactions

Rate-limiting steps chemical reaction

Rate-limiting steps, in reactions

Rate-limiting surface reactions

Reaction Limited Aggregation (RLA)

Reaction Limited Regime-Uniqueness

Reaction cavity limitations

Reaction constant rate-limiting step and

Reaction equilibrium limit

Reaction limit

Reaction limit

Reaction limiting step

Reaction mechanisms rate-limiting step approximation

Reaction paths, potential energy surfaces limitations

Reaction rate limited transport

Reaction rate limiting step

Reaction rates, diffusion controlled limit

Reaction stoichiometry limiting reactant

Reaction thermodynamic equilibrium limited

Reaction-limited aggregation computer simulation

Reaction-limited cluster aggregation

Reaction-limited cluster aggregation RLCA)

Reaction-limited cluster aggregation mechanism

Reaction-limited cluster aggregation, example

Reaction-limited dissolution

Reaction-limited growth

Reaction-limited regime

Reaction-limited regime estimation

Reactions Limiting High Polymer Formation

Reactions That Involve a Limiting Reactant

Reactions rate-limited by a diffusion process

Reactions rate-limited by an interface process

Reactive spreading reaction limited

Reimer-Tiemann reaction limitations

Relaxation time reaction limitation with comparable

Scope and limitations of a reaction

Self-limiting reaction

Self-limiting surface reactions

Shapiro reaction limitations

Stoichiometry limiting reactions

Surface reaction desorption limiting

Surface reaction limiting forms

Surface-reaction-limited operations

The H2 O2 reaction p-Ta ignition limits in closed vessels

The Limits of Reaction

The Photochemical Reaction Limit

Thermodynamically limited reactions

Topological reaction limit

Transport limitation by reaction-diffusion interaction

Transport limited reactions

Ugi reaction limitations

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