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Dimensionless numbers method

TT-theorem) or from the governing equations of the flow. The latter is to be preferred because this method will give a sufficient amount of dimensionless numbers. Furthermore, it will connect the numbers to the physical process via the equations and give important information in cases where it is necessary to make approximations. [Pg.1177]

Since the process is more complex, the proposed method may not be valid for scale-up calculation. The combination of power and Reynolds number was the next step for correlating power and fluid-flow dimensionless number, which was to define power number as a function of the Reynolds number. In fact, the study by Rushton summarised various geometries of impellers, as his findings were plotted as dimensionless power input versus impeller... [Pg.291]

The dynamical regimes that may be explored using this method have been described by considering the range of dimensionless numbers, such as the Reynolds number, Schmidt number, Peclet number, and the dimensionless mean free path, which are accessible in simulations. With such knowledge one may map MPC dynamics onto the dynamics of real systems or explore systems with similar characteristics. The applications of MPC dynamics to studies of fluid flow and polymeric, colloidal, and reacting systems have confirmed its utility. [Pg.139]

From an analysis of the electrochemical mass-transfer process in well-supported solutions (N8a), it becomes evident that the use of the molecular diffusivity, for example, of CuS04, is not appropriate in investigations of mass transfer by the limiting-current method if use is made of the copper deposition reaction in acidified solution. To correlate the results in terms of the dimensionless numbers, Sc, Gr, and Sh, the diffusivity of the reacting ion must be used. [Pg.233]

Our task now is to come up with a way to quantifying the amount of nonlinearity the data exhibits, independent of the scale (i.e., units) of either variable, and even independent of the data itself. Our method of addressing this task is not unique, there are other ways to reach the goal. But we will base our solution on the methodology we have already developed. We do this by noting that the first condition is met by converting the nonlinear component of the data to a dimensionless number (i.e., a statistic), akin to but different than the correlation coefficient, as we showed in our previous chapter first published as [5],... [Pg.459]

As a rule, more than two dimensionless numbers will be necessary to describe a physicotechnological problem and therefore they cannot be derived by the method described above. In this case, the easy and transparent matrix calculation introduced by Pawlowski (6) is increasingly used. It will be demonstrated by the following example. It treats an important problem in industrial chemistry and biotechnology because the gas liquid-contact in mixing vessels belongs to frequently used mixing operations (Fig. 2). [Pg.8]

The second method uses dimensionless numbers to predict scale-up parameters. The use of dimensionless numbers simplifies design calculations by reducing the number of variables to consider. The dimensionless number approach has been used with good success in heat transfer calculations and to some extent in gas dispersion (mass transfer) for mixer scale-up. Usually, the primary independent variable in a dimensionless number correlation is Reynolds number ... [Pg.74]

Both methods yield dimensionless groups, which correspond to dimensionless numbers (1), e.g.. Re, Reynolds number Fr, Froude number Nu, Nusselt number Sh, Sherwood number Sc, Schmidt number etc. (2). The classical principle of similarity can then be expressed by an equation of the form ... [Pg.200]

Dimensional analysis is a method for producing dimensionless numbers that completely characterize the process. The analysis can be applied even when the equations governing the process are not known. According to the theory of models, two processes may be considered completely similar if they take place in similar geometrical space and if all the dimensionless numbers necessary to describe the process have the same numerical value (2). [Pg.556]

Where no complete mathematical description of the process and no dimensionless-numbers equations are available, modeling based on individual ratios can be employed. This is the most characteristic case for a number of industrial processes, especially in the field of organic-chemicals technology. This method is referred to as scale-up modeling (Mukhyonov et al., 1979). In such cases, individual ratios for the model and the object, which should have a constant value, are employed. For instance, there should be a constant ratio between the space velocity of the reacting mixture in the model and the industrial object. Some of the dimensionless numbers mentioned in physical modeling are also employed in this case. [Pg.528]

Both methods yield dimensionless groups, which correspond to dimensionless numbers [1], e.g. ... [Pg.152]

Dimensionless parameter estimation The model s equations were solved using a fourth-order Runge-Kutta method. The dimensionless parameters estimation (Table I) was made as follows Only two of the dimensionless numbers Ai, Af, A2, A3, Ai and A5 are known directly. The parameter Ai can be estimated with reasonable accuracy since the catalyst surface area was measured independently ... [Pg.174]

As a rule, more than two dimensionless numbers are necessary to describe a phys-ico-technological problem they cannot be produced as shown in the first three examples. The classical method to approach this problem involved a solution of a system of linear algebraic equations. They were formed separately for each of the base dimensions by exponents with which they appeared in the physical quantities. J. Pawlowski [5] replaced this relatively awkward and involved method by a simple and transparent matrix transformation ( equivalence transformation ) which will be presented in detail in the next example. [Pg.16]

This method of compiling a complete set of dimensionless numbers makes it clear that the numbers formed in this way cannot contain numerical values or any other constant. These appear in dimensionless groups only when they are established and interpreted as ratios on the basis of known physical interrelations. Examples ... [Pg.19]

In the above-mentioned case of the pressure drop of the volume flow in a straight pipe, this method of compiling a complete set of dimensionless numbers produces the relationship... [Pg.19]

Tlie physical properties appearing in the dimensionless numbers Nu, Re, Pr, and Or all are evaluated at the bulk fluid temperature T. The values of the empirical con.slanls a, b, and c in Eq. 8-83 depend on the inlet configuration and are given in Table 8-7. The viscosity ratio accounts for the temperature effect on the process. Tlte range of application of the heat transfer method based on their database of 1290 points (441 points for re-entrant... [Pg.504]

The derivation method of the adiabatic temperature increase equation, which is introduced in the preceding section, is very difficult to understand. First of all, wc cannot understand very well the reason why dimensionless numbers, such as 0, 6 and T, are needed to derive the equation. Fortunately, however, we have an alternative method to derive, though qualitatively, the equation in a far simpler manner. [Pg.33]

The determination of heat transfer coefficients with the assistance of dimensionless numbers has already been explained in section 1.1.4. This method can also be used for mass transfer, and as an example we will take the mean Nusselt number Num = amL/ in forced flow, which can be represented by an expression of the form... [Pg.84]

Two methods have proved themselves in the reproduction of heat transfer measurements. One starts from empirical correlations for the pure substances. These correlations normally contain dimensionless numbers, that now have to be formed with the properties of the binary mixture. The reduction in heat transfer because of inhibited bubble growth caused by diffusion is taken into account by the introduction of an extra term. This type of equation has been presented by... [Pg.498]

This is to an extent laughable, because dimensional analysis is a method for producing dimensionless numbers and is not an aid, which replaces the thinking of the researcher or can take away the decision over which quantities should be considered relevant and incorporated into the relevance list and which not ... [Pg.230]

This result only gives you the fact that Oi can be written as a function of the other fls. Normally, the exact functional form comes from data correlation or rearrangement of analytical solutions. Correlating data using the dimensionless numbers formed by this method typically allows one to obtain graphical plots which are simpler to use and/or equations which fit to the data. If the dimensionless terms are properly grouped, they represent ratios of various effects and one can ascertain the relative importance of these effects for a given set of conditions. [Pg.276]

This illustrates an important point. With this method, we can obtain dimensionless numbers but they may not be in the best (or most recognizable) form. So the final form that is normally used is ... [Pg.278]

Dimensionless numbers obtained by this method are usually called fl s. [Pg.266]


See other pages where Dimensionless numbers method is mentioned: [Pg.74]    [Pg.45]    [Pg.74]    [Pg.45]    [Pg.62]    [Pg.97]    [Pg.55]    [Pg.113]    [Pg.209]    [Pg.182]    [Pg.226]    [Pg.50]    [Pg.299]    [Pg.11]    [Pg.266]    [Pg.61]    [Pg.436]   
See also in sourсe #XX -- [ Pg.74 , Pg.75 ]




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