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Rate initial

CO2 corrosion often occurs at points where there is turbulent flow, such as In production tubing, piping and separators. The problem can be reduced it there is little or no water present. The initial rates of corrosion are generally independent of the type of carbon steel, and chrome alloy steels or duplex stainless steels (chrome and nickel alloy) are required to reduce the rate of corrosion. [Pg.94]

Here (D is the diffusion coefficient and C is the concentration in the general bulk solution. For initial rates C can be neglected in comparison to C/ so that from Eqs. IV-59 and IV-60 we have... [Pg.150]

Qualitative examples abound. Perfect crystals of sodium carbonate, sulfate, or phosphate may be kept for years without efflorescing, although if scratched, they begin to do so immediately. Too strongly heated or burned lime or plaster of Paris takes up the first traces of water only with difficulty. Reactions of this type tend to be autocat-alytic. The initial rate is slow, due to the absence of the necessary linear interface, but the rate accelerates as more and more product is formed. See Refs. 147-153 for other examples. Ruckenstein [154] has discussed a kinetic model based on nucleation theory. There is certainly evidence that patches of product may be present, as in the oxidation of Mo(lOO) surfaces [155], and that surface defects are important [156]. There may be catalysis thus reaction VII-27 is catalyzed by water vapor [157]. A topotactic reaction is one where the product or products retain the external crystalline shape of the reactant crystal [158]. More often, however, there is a complicated morphology with pitting, cracking, and pore formation, as with calcium carbonate [159]. [Pg.282]

Nitration at a rate independent of the concentration of the compound being nitrated had previously been observed in reactions in organic solvents ( 3.2.1). Such kinetics would be observed if the bulk reactivity of the aromatic towards the nitrating species exceeded that of water, and the measured rate would then be the rate of production of the nitrating species. The identification of the slow reaction with the formation of the nitronium ion followed from the fact that the initial rate under zeroth-order conditions was the same, to within experimental error, as the rate of 0-exchange in a similar solution. It was inferred that the exchange of oxygen occurred via heterolysis to the nitronium ion, and that it was the rate of this heterolysis which limited the rates of nitration of reactive aromatic compounds. [Pg.11]

The effect of nitrous acid on the nitration of mesitylene in acetic acid was also investigated. In solutions containing 5-7 mol 1 of nitric acid and < c. 0-014 mol of nitrous acid, the rate was independent of the concentration of the aromatic. As the concentration of nitrous acid was increased, the catalysed reaction intervened, and superimposed a first-order reaction on the zeroth-order one. The catalysed reaction could not be made sufficiently dominant to impose a truly first-order rate. Because the kinetic order was intermediate the importance of the catalysed reaction was gauged by following initial rates, and it was shown that in a solution containing 5-7 mol 1 of nitric acid and 0-5 mol 1 of nitrous acid, the catalysed reaction was initially twice as important as the general nitronium ion mechanism. [Pg.58]

The evidence outlined strongly suggests that nitration via nitrosation accompanies the general mechanism of nitration in these media in the reactions of very reactive compounds.i Proof that phenol, even in solutions prepared from pure nitric acid, underwent nitration by a special mechanism came from examining rates of reaction of phenol and mesi-tylene under zeroth-order conditions. The variation in the initial rates with the concentration of aromatic (fig. 5.2) shows that mesitylene (o-2-0 4 mol 1 ) reacts at the zeroth-order rate, whereas phenol is nitrated considerably faster by a process which is first order in the concentration of aromatic. It is noteworthy that in these solutions the concentration of nitrous acid was below the level of detection (< c. 5 X mol... [Pg.91]

Fig. 5.2. Initial rates of nitration of mesitylene and phenol under zeroth-order conditions. Temperature 25 °C. [AcONOo] = r. 7 x io mol 1 . [HNO ] < 10" mol 1. ... Fig. 5.2. Initial rates of nitration of mesitylene and phenol under zeroth-order conditions. Temperature 25 °C. [AcONOo] = r. 7 x io mol 1 . [HNO ] < 10" mol 1. ...
The concentration of aluminum in serum can be determined by adding 2-hydroxy-1-naphthaldehyde p-methoxybenzoyl-hydrazone and measuring the initial rate of the resulting complexation reaction under pseudo-first-order conditions.The rate of reaction is monitored by the fluorescence of the metal-ligand complex. Initial rates, with units of emission intensity per second, were measured for a set of standard solutions, yielding the following results... [Pg.630]

A serum sample treated in the same way as the standards has an initial rate of 0.313 emission intensity/s. What is the concentration of aluminum in the serum sample ... [Pg.630]

Substituting the sample s initial rate into the calibration equation gives an aluminum concentration of 0.331 )J,M. [Pg.630]

Noncatalytic Reactions Chemical kinetic methods are not as common for the quantitative analysis of analytes in noncatalytic reactions. Because they lack the enhancement of reaction rate obtained when using a catalyst, noncatalytic methods generally are not used for the determination of analytes at low concentrations. Noncatalytic methods for analyzing inorganic analytes are usually based on a com-plexation reaction. One example was outlined in Example 13.4, in which the concentration of aluminum in serum was determined by the initial rate of formation of its complex with 2-hydroxy-1-naphthaldehyde p-methoxybenzoyl-hydrazone. ° The greatest number of noncatalytic methods, however, are for the quantitative analysis of organic analytes. For example, the insecticide methyl parathion has been determined by measuring its rate of hydrolysis in alkaline solutions. [Pg.638]

Sensitivity The sensitivity for a one-point fixed-time integral method of analysis is improved by making measurements under conditions in which the concentration of the monitored species is larger rather than smaller. When the analyte s concentration, or the concentration of any other reactant, is monitored, measurements are best made early in the reaction before its concentration has substantially decreased. On the other hand, when a product is used to monitor the reaction, measurements are more appropriately made at longer times. For a two-point fixed-time integral method, sensitivity is improved by increasing the difference between times t and f2. As discussed earlier, the sensitivity of a rate method improves when using the initial rate. [Pg.640]

Pseudo-Order Reactions and the Method of Initial Rates Unfortunately, most reactions of importance in analytical chemistry do not follow these simple first-order and second-order rate laws. We are more likely to encounter the second-order rate law given in equation A5.11 than that in equation A5.10. [Pg.753]

A variation on the use of pseudo-ordered reactions is the initial rate method. In this approach to determining a reaction s rate law, a series of experiments is conducted in which the concentration of those species expected to affect the reaction s rate are changed one at a time. The initial rate of the reaction is determined for each set of conditions. Comparing the reaction s initial rate for two experiments in which the concentration of only a single species has been changed allows the reaction order for that species to be determined. The application of this method is outlined in the following example. [Pg.754]

Figure 6.3 shows some data which constitute a test of Eq. (6.26). In Fig. 6.3a, Rp and [M] are plotted on a log-log scale for a constant level of redox initiator. The slope of this line, which indicates the order of the polymerization with respect to monomer, is unity, showing that the polymerization of methyl methacrylate is first order in monomer. Figure 6.3b is a similar plot of the initial rate of polymerization—which essentially maintains the monomer at constant con-centration—versus initiator concentration for several different monomer-initiator combinations. Each of the lines has a slope of indicating a half-order dependence on [I] as predicted by Eq. (6.26). Figure 6.3 shows some data which constitute a test of Eq. (6.26). In Fig. 6.3a, Rp and [M] are plotted on a log-log scale for a constant level of redox initiator. The slope of this line, which indicates the order of the polymerization with respect to monomer, is unity, showing that the polymerization of methyl methacrylate is first order in monomer. Figure 6.3b is a similar plot of the initial rate of polymerization—which essentially maintains the monomer at constant con-centration—versus initiator concentration for several different monomer-initiator combinations. Each of the lines has a slope of indicating a half-order dependence on [I] as predicted by Eq. (6.26).
C with AIBN and measured the initial rates of polymerization for the ... [Pg.417]

Usually, free-radical initiators such as azo compounds or peroxides are used to initiate the polymerization of acrylic monomers. Photochemical (72—74) and radiation-initiated (75) polymerizations are also well known. At a constant temperature, the initial rate of the bulk or solution radical polymerization of acrylic monomers is first order with respect to monomer concentration and one-half order with respect to the initiator concentration. Rate data for polymerization of several common acrylic monomers initiated with 2,2 -azobisisobutyronittile (AIBN) [78-67-1] have been determined and are shown in Table 6. The table also includes heats of polymerization and volume percent shrinkage data. [Pg.165]

Because the chemiluminescence intensity can be used to monitor the concentration of peroxyl radicals, factors that influence the rate of autooxidation can easily be measured. Included are the rate and activation energy of initiation, rates of chain transfer in cooxidations, the activities of catalysts such as cobalt salts, and the activities of inhibitors (128). [Pg.269]

The units oi sp are /mofh U Initial rate of polymerization is calculated from and the concentration of AIBN using the following equation ... [Pg.263]

The thiol ( -dodecyl mercaptan) used ia this recipe played a prominent role ia the quaUty control of the product. Such thiols are known as chain-transfer agents and help control the molecular weight of the SBR by means of the foUowiag reaction where M = monomer, eg, butadiene or styrene R(M) = growing free-radical chain k = propagation-rate constant = transfer-rate constant and k = initiation-rate constant. [Pg.468]

Thus the thiol 0 2 25511 is capable of terminating a growiug chain and also initiating a new chain. If the initiation-rate constant, k is not much slower than the propagation-rate constant, the net result is the growth of a new chain without any effect on the overall polymerization rate (retardation). That represents a tme chain transfer, ie, no effect on the rate but a substantial decrease iu molecular weight (12). [Pg.468]

One Anson unit is the amount of enzyme that, under standard conditions, digests hemoglobin at an initial rate, Hberating per minute an amount of TCA-soluble product which produces the same color with phenol reagent as one milliequivalent of tyrosine (91). [Pg.301]

Unprotected racemic amines can be resolved by enantioselective acylations with activated esters (110,111). This approach is based on the discovery that enantioselectivity of some enzymes strongly depends on the nature of the reaction medium. For example, the enantioselectivity factor (defined as the ratio of the initial rates for (3)- and (R)-isomers) of subtiHsin in the acylation of CX-methyl-ben zyl amine with tritiuoroethyl butyrate varies from 0.95 in toluene to 7.7 in 3-methyl-3-pentanol (110). The latter solvent has been used for enantioselective resolutions of a number of racemic amines (110). [Pg.343]

A furdrer complication is that in these slowly growing oxide films, tire spread of the oxide across the metal surface is limited in the early stages by nucleation and growth control. The bare patches of metal between the oxide nuclei will clearly be exposed to a higher oxygen potential and new oxide nuclei will grow at a different initial rate than on the existing nuclei. [Pg.253]

The well-known difficulty with batch reactors is the uncertainty of the initial reaction conditions. The problem is to bring together reactants, catalyst and operating conditions of temperature and pressure so that at zero time everything is as desired. The initial reaction rate is usually the fastest and most error-laden. To overcome this, the traditional method was to calculate the rate for decreasingly smaller conversions and extrapolate it back to zero conversion. The significance of estimating initial rate was that without any products present, rate could be expressed as the function of reactants and temperature only. This then simplified the mathematical analysis of the rate fianction. [Pg.29]


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Acyl peroxide initiators, decomposition rates

Alkyl peroxide initiators, decomposition rates

Analysis of Initial Rate Data

And rate of initiation

Average, Instantaneous, and Initial Reaction Rates

Azonitrile initiators decomposition rates

Base-initiated ring-opening polymerization reaction rates

Chain initiation absolute rate

Characteristics of Specific Initial Rate Laws

Chloride ingress rates (initiation)

Crack initiation applied strain rate

Data analysis methods initial rates method

Decomposition rates, free radical initiators

Decomposition rates, free radical initiators hydroperoxides

Dehydrogenases initial rate equations

Dependence of Polymerization Rate on Initiator

Dispersion Initial reaction rate

Effective rate of initiation

Electron transfer rate initial correlations

Empirical radical initiating rate

Emulsion polymerization initiation rates

Enzymatic initial rates

Enzymatic synthesis initial reaction rate

Enzyme catalysis, activation energy initial reaction rate

Enzyme kinetics initial rate

Enzymes initial reaction rates

Factors affecting rate initiation

Flow rates initial guess

Graphical analysis of initial rate data

Hydroperoxide initiators, decomposition rates

INITIAL RATE CONDITION

INITIAL RATE ENZYME DATA

INITIAL RATE ENZYME DATA REPORTING

INITIAL RATE PHASE

Initial Rate Determination at Low Substrate

Initial Rates Iodine Clock

Initial Rates on the Concentrations of Initiator and Monomer

Initial hydration rate

Initial inactivation rate

Initial rate assumption

Initial rate assumption CHEMICAL KINETICS

Initial rate behavior

Initial rate constants

Initial rate curves

Initial rate data

Initial rate data graphical analysis

Initial rate data statistical analysis

Initial rate equations

Initial rate equations conformation change

Initial rate equations rapid equilibrium mechanism

Initial rate equations simple ordered mechanism

Initial rate equations three-substrate reactions

Initial rate estimation from reaction progress

Initial rate expressions

Initial rate method

Initial rate method addition

Initial rate method, kinetic analysis

Initial rate methods, reaction kinetics

Initial rate regime

Initial rate studies

Initial rates linear least squares analysis

Initial rates of exchange

Initial rates of formation

Initial rates total pressure dependence

Initial rates, measuring

Initial reaction rate

Initial relaxation-rate

Initial relaxation-rate definition

Initial transient rates

Initial-rate kinetics

Initial-rate measurement

Initiation rate

Initiation rate constant

Initiation rate constants free radical polymerizations

Initiation, rate, autoxidation

Initiation, rate, autoxidation linoleic acid

Initiator dissociation rate constant

Initiator flow rate

Initiators thermal decomposition rates

Ketone peroxide initiators, decomposition rates

Mechanistic rate laws initial rates

Method of initial rates

Michaelis parameters determination from initial rate

Obtaining Initial Rate Data

Ordered mechanism three-substrate reactions, initial rate

Organic solvents effect initiator decomposition rate

Perester initiators, decomposition rates

Poly initial growth rates

Polymerization initial rate

Pyrolysis initial rates

Radiationless Decay Rates of Initially Selected Vibronic States in Polyatomic Molecules

Rate constant for initiation

Rate constant of initiation

Rate constants for initiator decomposition

Rate constants free radical initiation

Rate density initial

Rate equations initial value problems

Rate expressions initiation

Rate of initiation

Rate of photochemical initiation

Rate of reaction initial

Reaction initial rate kinetics

Reactions initial rates method

Reactions initial reaction rate

Redox-initiated polymerization rate equation

Representative initial rate data

Representative initial rate data reactants

Solvents, initiation rates

Stabilization by Decreasing Initiation Rate

Step initiation rate

Stress Growth after Initiation of a Constant Shear Rate

Template polymerization initial reaction rate

Termination Free-radical initiators, rates

The Initial Evidence Based on Fatality Rates—Peltzman

The method of initial rates

The significance of initial rates

Time correlation functions initial decay rate

Using Initial Rates to Determine Rate Laws

Using the method of initial rates

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