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Computer programs Catalyst

Table 2.1 Enantiomeric ratios (E) obtained in hydrolysis of butanoates la-15a and transesterifrcation of alcohols lb-9b and 13b-15b using 2-chloroethyl butanoate as acyl donor and lipase B from Candida antarctica (CALB) as catalyst. For significance of and R2 see Figure 2.9. F-values were determined from chromatographically measured ee and ee at several degrees of conversion and using the computer program E K calculator version 2.03. Note that the stereopreference of CALB changes from (R) to (S) when R2=F, ClandBr. Table 2.1 Enantiomeric ratios (E) obtained in hydrolysis of butanoates la-15a and transesterifrcation of alcohols lb-9b and 13b-15b using 2-chloroethyl butanoate as acyl donor and lipase B from Candida antarctica (CALB) as catalyst. For significance of and R2 see Figure 2.9. F-values were determined from chromatographically measured ee and ee at several degrees of conversion and using the computer program E K calculator version 2.03. Note that the stereopreference of CALB changes from (R) to (S) when R2=F, ClandBr.
Equations 6-94 and 6-97 are first order differential equations, and it is possible to solve for both the conversion and temperature of hydrogenation of nitrobenzene relative to the reactor length of 25 cm. A computer program PLUG61 has been developed employing the Runge-Kutta fourth order method to determine the temperature and conversion using a catalyst bed step size of 0.5 cm. Table 6-6 shows... [Pg.489]

Knowledge-based systems are computer programs which apply knowledge about a specific domain in order to derive new conclusions. These conclusions are on the level of a human expert in this field, but constrained by the field of expertise. Applied to catalysis, the knowledge base contains heuristics about relationships between chemical and physico-chemical properties of solids and their catalytic properties, as well as known properties for such solids which may be used as components of catalysts [2, 18]. An expert system is able to combine this knowledge about different catalyst properties which may be necessary to catalyze the required reaction steps, or which should be avoided because they catalyze side reactions. [Pg.267]

Table II gives an example of the fixed parameters used in calculating the model-predicted values of conversion for the a-methylstyrene-hexane solvent system and 0.5% Pd catalyst. These, along with the experimental conversion versus liquid superficial velocity data, were input to a computer program for data reduction. Similar data files were developed for each series of experiments and reduced in a similar fashion. Table II gives an example of the fixed parameters used in calculating the model-predicted values of conversion for the a-methylstyrene-hexane solvent system and 0.5% Pd catalyst. These, along with the experimental conversion versus liquid superficial velocity data, were input to a computer program for data reduction. Similar data files were developed for each series of experiments and reduced in a similar fashion.
To calculate the amount of catalyst for a particular case, mass and heat balance have to be considered they can be described by two differential equations one gives the differential CO conversion for a differential mass of catalyst, and the other the associated differential temperature increase. As analytical integration is not possible, numerical methods have to be used for which today a number of computer programs are available with which the calculations can be performed on a powerful PC in the case of shift conversion. Thus the elaborate stepwise and graphical evaluation by hand [592], [609] is history. For the reaction rate r in these equations one of the kinetic expressions discussed above (for example, Eq. 83) together with the function of the temperature dependence of the rate constant has to be used. [Pg.116]

The computer program PROG38 calculates the pressure drop in a 1.610-inch I.D. packed bed for varying length of catalyst pellets. For air at 260°C and 10 atm, the physical properties are ... [Pg.204]

Using chc constants in a computer program to solve for W.wc get W c 18450 kg catalyst. Note that the 18450 is wrong due to complete error. Also, the D s in Qs Qa should be switched. Thus ... [Pg.781]

Selection and Testing Statistical Test Planning with a Computer Program... [Pg.379]

Catalyst preparation, characterization and testing that includes robotic and computer-programmed instruments... [Pg.437]

This particular strategy suffers from gaps in the ability to predict protein structure accurately and correlate this ideal structure with enzymatic activity. For example, two enzymes (retro-aldol enzyme and a Kemp elimination catalyst) were built completely from scratch by using computer programs. However, both enzymes required further optimization by directed evolution to achieve maximum activity. [Pg.706]


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Catalyst program

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