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Equilibrium, attainment

Conversion at Equilibrium. The maximum urea conversion at equilibrium attainable at 185°C is ca 53% at infinite heating time. The conversion at equiUbtium can be increased either by raising the reactor temperature or by dehydrating ammonium carbamate in the presence of excess ammonia. Excess ammonia shifts the reaction to the right side of the overall equation ... [Pg.300]

Thus for the equilibrium attained when zinc metal reacts with acid,... [Pg.331]

Kd = distribution coefficient (as defined above) s/m = salt to metal ratio by weight F = fraction of equilibrium attained B = effects of side reactions... [Pg.386]

The production process chosen in this work involved at least bromine in the liquid phase. In order to implement a production process, it is important to have knowledge of the reaction s kinetics, i.e. how soon is the equilibrium attained. In cases where the BrCI should be used immediately following its production, it is important to avoid high levels of unreacted chlorine, since it might result in undesired chlorinations etc. [Pg.318]

This solid is iodine trichloride, ICl3(S). When the U-tube is stoppered, it contains a mixture of IC1(d, Cl2(g) and ICl3(s). Eventually, the number of moles of each component remains constant and a state of equilibrium attained. [Pg.82]

Sampling rate extrapolation into the low log Ko range is more difficult, because of the increasing resistance of the membrane, which causes the sampling rates to fall below the values that are predicted by Eq. 3.51. Fortunately, this extrapolation is less critical, because compounds that are less hydrophobic than the PRCs typically have attained a substantial degree of equilibrium. As a result, aqueous concentration estimates for these compounds are quite insensitive to uncertainties in the sampling rates. Alternatively, when the log Kow interval between successive PRCs is small, the degree of equilibrium attained by analytes with intermediate log Ko values may be obtained by interpolation. The aqueous concentrations may be subsequently calculated from the partition coefficients and corrected for partial equilibrium attainment. [Pg.69]

In this present chapter, we will be looking at a slightly more complicated situation, i.e. one in which the contents of two redox half cells are not separated but are allowed to mix. Because mixing occurs, redox chemistry can occur, i.e. electron-transfer reactions are not forbidden. Any electrochemical equilibrium attained is thus a genuine thermodynamic equilibrium and is not frustrated . [Pg.86]

In developing a suitable calorimeter, factors of primary importance include a steady and sufficient stirring rate, accurate measurement of temperature changes, accurate measurement of the electrical energy equivalent, sufficiently rapid attainment of thermal equilibrium, attainment of suitable rating or steady-state periods, and small changes in the latter due to the increase in viscosity when the powder is broken into the liquid. [Pg.267]

Measurement of the results of reaction with other chemicals in terms of amount of sample or reactant consumed, product formed, or thermal energy liberated, or determination of equilibrium attained... [Pg.95]

In the years following Berzelius, a number of further examples of catalytic action were discovered, but scientific appreciation of their mode of action had to await the arrival of experimental and theoretical techniques for the study of reaction rates. It then became possible for F.W. Ostwald to define a catalyst as a substance that increases the rate at which a chemical system approaches equilibrium, without being consumed in the process. This handy form of words encapsulates the essential truth of the catalytic effect, and has stood the test of time it carries with it a number of important implications that we should now explore. The first of these is that the position of equilibrium attained in a catalysed reaction is exactly the same as that which would ultimately be arrived at in its absence this must be so because the equilibrium constant K is determined by the Gibbs free energy of the process, and this in turn is fixed by the enthalpy and entropy changes, thus ... [Pg.2]

Suitable absorbance changes allowed the determination of the pseudo-first order rate of attainment of the equilibrium, k (equation 35), both in the presence and the absence of the surfactants. Fro m these values and the values of (the equilibrium constant for equation (36) in the presence of surfactants), y and were obtained. The results indicated that, in the case of 19 micelles exerted a greater effect on the second-order rate constants, y, than on y (Table 13). More specifically, is in creased considerably by CTAB and decreased by NaLS, while y is decreased by both surfactants but to a much greater extent by NaLS (Table 13). For the sulfonphthalein indicators 20, sodium dodecyl sulfate has no significant effect on k whereas CTAB decreases k for the equilibrium attainment. Qualitatively the effects of micelles on the equilibria for... [Pg.357]

Allen, L.H, and Matijevic, E 1969. Stability of colloidal silica. J. Colloid Interface Sci., 31 287-396. Anderson, A.T., 1967. The dimensions of oxygen isotopic equilibrium attainment during prograde metamorphism. J. Geol., 75 323-331. [Pg.283]

Summary Phosfdiazene bases represent a new class of highly active non-ionic catalysts that rapidly polymerize cyclosiloxanes with equilibrium attained in very short reaction times at very low catalyst levels. To date, phosphazene base catalysts have been considered an academic curiosity because of the complicated and hazardous synthetic protocol used to prepare them. A facile synthetic process has been developed, which yields ionic phosphazene bases in three steps with an overall yield of qrproximately 75%. This is achieved through nucleophilic substitution of ionic phosphonitrilic chloride oligomers with secondary amines, followed by anion exchange. These ionic phosphazenes were found to exhibit similar reactivity in the ring-opening polymerization of cyclosiloxanes to that of the non-ionic phosphazene base. [Pg.628]

The partition coefficient is the driving force for removal of the volatile species to the gas phase in establishing equilibrium, attainment of which depends on the particular procedure. This coefficient depends on the analyte concentration it decreases with increasing concentration but remains constant over a concentration range that depends on the particular type of compound. Thus, the range of virtual constancy for BTX (benzene, toluene and o-xylene) is 0.1-10 pg/ml as a result, these compounds can only be determined reliably at concentrations below 10 pg/ml [68]. [Pg.114]

In all of the above crystal studies, bond lengths and bond angles were found to be similar to those of the corresponding purines. As with all X-ray diffraction work, it can not be assumed that a structure found in an anhydrous crystal would necessarily recur in a hydrated one (which, unfortunately, cannot always be obtained), nor do crystal studies necessarily reflect the tautomeric equilibrium attained in aqueous solution. [Pg.123]

In other words, the decay rates of parent and daughter are equal, and their concentrations are equal, when expressed in terms of Bq/m or other units of radioactivity. This condition is known as secular equilibrium. Attainment of secular equilibrium between a parent and daughter can occur only when kp kp. In a closed system, secular equilibrium among all the daughters in a decay series may also be attained if the decay constant of the initial parent is much less than that of any of its daughters. Such is the case for and Th. If secular equilibrium is attained in such a series, then... [Pg.492]

Figure 6. Model E analytical schlieren patterns of purified LPS. Equilibrium attained at 36,000 rpm at 25°C for 18 hours in 2°C sector cells. A 34% CsCl pattern of B. abortus LPS, sample from preparation run in Figure 5A. B 34% CsCl pattern of B. abortus LPS. C 39% CsCl pattern of P. multocida LPS. Figure 6. Model E analytical schlieren patterns of purified LPS. Equilibrium attained at 36,000 rpm at 25°C for 18 hours in 2°C sector cells. A 34% CsCl pattern of B. abortus LPS, sample from preparation run in Figure 5A. B 34% CsCl pattern of B. abortus LPS. C 39% CsCl pattern of P. multocida LPS.
Figure 21-7 shows some commercially available, equilibrium attainment chambers for paper chromatographic separations. Some are vented to a hood system, so that easily combustible or explosive mixtures are not formed. [Pg.252]

Catalyst added None forward and reverse equilibrium attained sooner rates increase equally None... [Pg.567]

The rate of equilibrium attainment mainly during the batchwise arrangement is strongly affected by the concentration of a substance to be isolated in the sorption solution. Fig. 4.7.6 shows the rate of adsorption of trypsin on to soybean trypsin inhibitor-agarose particles in suspensions in solutions containing equal amounts of trypsin but of a different concentration [129]. The rate of sorption is determined on the basis of the residual activity of trypsin measured at various time intervals. [Pg.341]


See other pages where Equilibrium, attainment is mentioned: [Pg.103]    [Pg.165]    [Pg.50]    [Pg.580]    [Pg.284]    [Pg.69]    [Pg.30]    [Pg.150]    [Pg.1054]    [Pg.150]    [Pg.229]    [Pg.765]    [Pg.37]    [Pg.2221]    [Pg.768]    [Pg.632]    [Pg.274]    [Pg.321]    [Pg.100]    [Pg.121]    [Pg.62]    [Pg.30]    [Pg.427]    [Pg.163]    [Pg.632]   


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Attainable

Attainment

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Equilibrium rate, surface pressure attainment

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