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Rate, actual intrinsic

The ratio of actual rate to intrinsic rate is the effectiveness factor ... [Pg.364]

It depends only on J sJkj A, which is a dimensionless group known as the Thiele modulus. The Thiele modulus can be measured experimentally by comparing actual rates to intrinsic rates. It can also be predicted from first principles given an estimate of the pore length =2 . Note that the pore radius does not enter the calculations (although the effective diffusivity will be affected by the pore radius when dpore is less than about 100 run). [Pg.364]

Consequently, the activation energy will be determined by means of the data obtained at 600 rpm, where the values of the observed rate represent the actual intrinsic rate. Since the reaction is of first order with respect to ethanol,... [Pg.425]

Actual rate] = niO) [intrinsic rate of fresh catalyst]... [Pg.375]

The chain-length dependence of the propagation rate coefficient is of a more chemical nature in that it is caused by differences in the activation energy and the frequency factor of the actual, intrinsic, rate coefficients of the addition reaction for different size radicals. chain-length averaged propagation rate coefficient is defined by Eq. 4,... [Pg.24]

CO conversion is a function of both temperature and catalyst volume, and increases rapidly beginning at just under 100°C until it reaches a plateau at about 150°C. But, unlike NO catalysts, above 150°C there is Htde benefit to further increasing the temperature (44). Above 150°C, the CO conversion is controUed by the bulk phase gas mass transfer of CO to the honeycomb surface. That is, the catalyst is highly active, and its intrinsic CO removal rate is exceedingly greater than the actual gas transport rate (21). When the activity falls to such an extent that the conversion is no longer controUed by gas mass transfer, a decline of CO conversion occurs, and a suitable regeneration technique is needed (21). [Pg.512]

The somewhat controversial theory of risk homeostasis is relevant to a discussion of risk taking. RHT was developed initially in the area of driving behavior (Wilde, 1984). The theory states that accident rates are not determined by actual levels of intrinsic risk but by the levels of risk acceptable to individuals in the situation. The theory implies that people adjust their risk-taking behavior to maintain a constant level of perceived risk. Thus, if improved safety measures are introduced (e.g., better guarding, improved protection systems then individuals will behave in a more risky fashion in order to maintain their accustomed levels of risk. [Pg.138]

Actually, the system capacitance and the pressure-decay rate measure the rate of capacitance discharge of the system. Because the combustion process is known to be controlled by pressure, the pressure-decay rate will disturb the combustion process. If the decay rate is greater than the intrinsic pressure-growth rate of the controlling reaction, the combustion process will not recover. This suggests that the pressure-decay rate dP/dt is the intrinsic term, rather than the capacitance term (L ). [Pg.63]

Few fixed-bed reactors operate in a region where the intrinsic kinetics are applicable. The particles are usually large to minimize pressure drop, and this means that diffusion within the pores. Steps 3 and 7, can limit the reaction rate. Also, the superficial fluid velocity may be low enough that the external film resistances of Steps 2 and 8 become important. A method is needed to estimate actual reaction rates given the intrinsic kinetics and operating conditions within the reactor. The usual approach is to define the effectiveness factor as... [Pg.362]

Note that we have defined "interface angle" as the angle between the growing crystal and the residual melt. Rate of pulling also ciffects the quality of the crystal as well as the actual number of intrinsic defects which may appear in the final crystal. In the upper left of 6.4.7., aflat-... [Pg.264]

Bertole et al.u reported experiments on an unsupported Re-promoted cobalt catalyst. The experiments were done in a SSITKA setup, at 210 °C and pressures in the range 3-16.5 bar, using a 4 mm i.d. fixed bed reactor. The partial pressures of H2, CO and H20 in the feed were varied, and the deactivation, effect on activity, selectivity and intrinsic activity (SSITKA) were studied. The direct observation of the kinetic effect of the water on the activity was difficult due to deactivation. However, the authors discuss kinetic effects of water after correcting for deactivation. The results are summarized in Table 1, the table showing the ratio between the results obtained with added water in the feed divided by the same result in a dry experiment. The column headings refer to the actual experiments compared. It is evident that adding water leads to an increase in the overall rate constant kco. The authors also report the intrinsic pseudo first order rate-coefficient kc, where the overall rate of CO conversion rco = kc 6C and 0C is the coverage of active... [Pg.18]

Rigorous treatment of the para-selectivity requires a knowledge of the intrinsic value of the rate constant for all the reactions involved and of the absolute value of the crystal size and of the diffusivity, all under reaction conditions. These values are obtainable only with considerable difficulty and effort. As has been mentioned, the 30 percent sorption time for o-xylene at 120°c, t0.3/ is proportional to the actual values, r2/D. [Pg.296]

The activity in terms of 1st order rate constant khcalc was calculated in Table 2 from (8) and (9) with effective diffusivity Dejf=5.3-10 6 m2/s and intrinsic rate constant =33000 Nm3/h/m3 = 23 s"1 fitted to the measurements. This simple and useful method models the measured influence of particle size satisfactorily for a first optimization of particle size and shape. The 35% higher activity measured for the 9-mm Daisy compared to the 12-mm Daisy, however, exceeds the 25% expected from (8), and this illustrates the importance of measuring the activity of the actual shape. [Pg.333]

The relationship between the structure of the tertiary amine and the intrinsic rate of racemization was clear. This effect has been studied before by Williams,[32 among others. Two families of bases were compared trialkylamines and 4-alkylmorpholines. The trends were most clearly expressed in the experiments using Boc-Ser(OBzl)-NCA. The rate was decreased within each family as the steric bulk of the amine was increased. This result was consistent with the direct enolization mechanism that requires a close approach of the tertiary amine for the abstraction of the a-proton. The rate was much lower with 4-alkyl-morpholines than with trialkylamines because of the decreased basicity of the former (triethylamine and 4-ethylmorpholine have similar structures TEA is actually more hindered). The most favorable results with respect to racemization were obtained when a weak base was combined with a sterically hindered substituent, as with 4-cyclohexylmorpholine. In the case of Boc-Phe-NCA, the same trends were seen, except that racemization by the 4-alkylmorpholines was so slow that the differences within that family were not significant. [Pg.666]

The intrinsic lifetime of triplet Ti state tp°, is the reciprocal of the rate constant kp, for phosphorescence emission and the actual lifetime if, is the reciprocal of the sum of all the steps which deactivate tne triplet. [Pg.147]


See other pages where Rate, actual intrinsic is mentioned: [Pg.278]    [Pg.147]    [Pg.541]    [Pg.132]    [Pg.278]    [Pg.33]    [Pg.43]    [Pg.140]    [Pg.111]    [Pg.375]    [Pg.364]    [Pg.367]    [Pg.369]    [Pg.29]    [Pg.452]    [Pg.246]    [Pg.81]    [Pg.31]    [Pg.38]    [Pg.20]    [Pg.350]    [Pg.101]    [Pg.51]    [Pg.102]    [Pg.84]    [Pg.18]    [Pg.165]   
See also in sourсe #XX -- [ Pg.35 , Pg.139 , Pg.250 , Pg.254 , Pg.266 , Pg.292 , Pg.297 , Pg.333 , Pg.335 , Pg.380 ]




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