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Integrate after separation

In kinetic studies it is not necessary to use rates for determination of the rate parameters. In eqs 2-4 r represents the rate expression for the reaction under consideration, whatever its mathematical form. This can be inserted in eq 2, and subsequently integrated after separation of variables, leading to eq 5. The result may be an implicit expression, containing the rate parameters, describing the relationship between space-time and conversion. It will be shown later that this relationship can also be used for parameter determination. [Pg.306]

Solution by Direct Indefinite Integration after Separation... [Pg.127]

The future leaching plant is based, as is the present installation, on the jarosite process. The project contemplates two separate circuits one to treat concentrates with high silver content and another one to treat the concentrates with low silver content. Both circuits are integrated after separation of the Pb/Ag residue. [Pg.558]

Fig. 22. XPS and UPS (/iV=120eV) ectra for YbAlj taken at 7 = 20K to determine any differences in signal due to escape depth. Values of f were obtained by dnect integration after separating out the background and surface features as shown. Nearly identical values were obtained thus confirming the bulk nature of the divalent peaks in UPS. Fig. 22. XPS and UPS (/iV=120eV) ectra for YbAlj taken at 7 = 20K to determine any differences in signal due to escape depth. Values of f were obtained by dnect integration after separating out the background and surface features as shown. Nearly identical values were obtained thus confirming the bulk nature of the divalent peaks in UPS.
After separation of variables, Eq. (3-3) is integrated to give Eq. (3-4) as the integrated rate equation. [Pg.60]

After separating the variables, (3.14.3.1) was solved by integration and the initial conditions were implemented (/0 = 0, S = S0). The resulting expression is... [Pg.56]

Equation (8.7.4.3) is a linear first-order differential equation for concentration and reactor length. After separation of variables, the equation can be integrated as... [Pg.226]

After separating the variables, this equation can be solved by integration between the limits (fo = 0, [A]0) and (t, [A],). The integrated expression is... [Pg.15]

The principles of fluidisation, discussed in Chapter 6, are applied in this type of dryer, shown typically in Figure 16.25. Heated air, or hot gas from a burner, is passed by way of a plenum chamber and a diffuser plate, fitted with suitable nozzles to prevent any back-flow of solids, into the fluidised bed of material, from which it passes to a dust separator. Wet material is fed continuously into the bed through a rotary valve, and this mixes immediately with the dry charge. Dry material overflows through a downcomer to an integral after-cooler. An alternative design of this type of dryer is one in which a thin bed is used. [Pg.946]

By integrating the second equation first, we get [R] = [R]initiaie 2 thus, we may substitute this expression for [R] into the first differential equation to obtain the rate law that allows for enzyme inactivation by a reagent which itself is undergoing deactivation. After separating variables and integrating the combined expression, we obtain... [Pg.695]

Sensors based on integrated dialysis, reaction and detection differ from those described in Section 4.3.1 in the fact that a (bio)chemical reaction takes place after separation (simultaneously with detection). They thus fit the generic configuration depicted in Fig. 5.1. A. Some of the ingredients of such a reaction may be immobilized at the sensing microzone, even though the reaction may also take place in the solution passed through it. [Pg.274]

If we now write the equation for a batch reactor (Chapter 5, Section 5.2.2) with deactivating enzyme over time, we obtain Eq. (17.20), or after separation of variables Eq. (17.21), and after integration Eq. (17.22). [Pg.495]

Eqns (16), (20) and (22) were integrated numerically to obtain the separation performance of the one- and two-column processes The GEAR package (13) was used for the integration after determining that it was faster than, say, Runge-Kutta methods For all calculations N 50 and e - 0.40 Dimensionless parameters varied were 8, ph pL Yf and, for the two-column process, H. Combinations of the parameters of 6 and Pr/Pl were chosen to correspond to the me thane-helium system on BPL carbon Adsorption isotherm data for methane at 25°C (14) were represented by... [Pg.207]

Assembly of Proteins into Cell Membranes. The individual components of a biological membrane, after separation in the presence of a high concentration of detergent, still are able to associate into a membrane when the detergent is removed. However, such self-assembly of the normal constituents of a membrane fail to show asymmetry. This might be the result of a random insertion of integral proteins as the lipid... [Pg.86]

When TiC>2 is used as a powder, a separation step must be integrated after pollutant treatment. [Pg.251]

Assume that the filtration is conducted at constant pressure. Then, after separating variables and integrating from 0 to tp and 0 and Vp, we obtain... [Pg.320]

After separating the variables and integrating within the limits ... [Pg.316]

Since the early 1980s, EniChem has been a pioneer in the development of the process, holding a portfolio of patents [10c,dj. The integration of HP synthesis by means of alkylanthraquinone/alkylanthrahydroquinone (RAQ/RAHQ) cycle technology, with PO production, by means of propene epoxidation with H P, is possible because of the peculiar properties of the TS-1 catalyst (Scheme 6.5). TS-1 can selectively epoxidize propene using diluted HP [12]. A water- methanol mixture is the solvent for the epoxidation the alcohol is necessary to obtain a sufficient reaction rate. Therefore, a cost-saving feature in this process is the fact that the crude H P produced can be used directly in the epoxidation of propene. Moreover, integration of the two processes is also allowed by the easily accomplished separation of propene and PO from the water-methanol mixture. Methanol, after separation and purification, can be recycled to the epoxidation step. [Pg.330]

We also assume that AHm is equal to a constant. After separation of variables and integration, we obtain the Clausius-Clapeyron equation... [Pg.337]

As required, all the molecular integrals can be evaluated analytically in terms of standard functions after separation into products of integrals of single variables. [Pg.120]

For upward flow (a = -g, where g is the acceleration due to gravity and the height h = x), after separation of the variables and integration, this equation leads to the well-known Bernoulli" equation (Equations 2.4-5 and 2.4-6 Figure 2.4-1) ... [Pg.173]


See other pages where Integrate after separation is mentioned: [Pg.39]    [Pg.574]    [Pg.39]    [Pg.574]    [Pg.556]    [Pg.387]    [Pg.321]    [Pg.43]    [Pg.169]    [Pg.465]    [Pg.196]    [Pg.102]    [Pg.249]    [Pg.513]    [Pg.465]    [Pg.20]    [Pg.250]    [Pg.7]    [Pg.526]    [Pg.9]    [Pg.610]    [Pg.255]    [Pg.340]    [Pg.51]    [Pg.162]    [Pg.41]    [Pg.281]   


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