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Combined models

Adsorption. In the design of the adsorption step of gas-phase processes, two phenomena must be considered, equiUbrium and mass transfer. Sometimes adsorption equiUbrium can be regarded as that of a single component, but mote often several components and their interactions must be accounted for. Design techniques for each phenomenon exist as well as some combined models for dynamic performance. [Pg.285]

Combined Models, Transfer Functions The transfer function relation is... [Pg.2085]

Identify the flow pattern of the prototype system by subjecting it to an impulse, step, or sinusoidal disturbance by injection of a tracer material as reviewed in Chapter 8. The result is classified as either complete mixing, plug flow, and an option between a dispersion, cascade, or combined model. [Pg.1035]

Overview of combined modeling of heat transport and air movement, AIVC Technical Note TN 40. Coventry Air Infiltration and Ventilation Centre, 1993. [Pg.1104]

Dear, J.P. Combined Modeling and Experimental Studies of Rubber Toughening in Polymers, J. Mater. Set 38, 891-900, 2004. [Pg.349]

The application of a combined modelling and simulation approach leads to the following advantages ... [Pg.5]

The maximum value for the tortousity was 30 and the value for the tortusity of each sample was estimated from the formation factor. The formation factor was taken either from resistivity measurents or estimated from NMR measurements and the Myers pore-combination model [37]. A comparison of the estimated permeability correlations is given in Figure 3.6.9. The SDR model overestimates the permeability of low permeability samples and the Chang model underestimates the permeability of high permeability samples. The modified Chang model, Eq. (3.6.9), improves the estimate of permeability for both low and high permeability samples. [Pg.334]

M. T. Myers 1991, Pore Combination Modeling A Technique for Modeling the Permeability and Resistivity Properties of Complex Pore Systems, paper SPE 22662 presented at the 1991 SPE ATC E, Dallas, TX, 6-9 October, 1991. [Pg.339]

Stern HA, Kaminski GA, Banks JL, Zhou RH, Berne BJ, Friesner RA (1999) Huctuating charge, polarizable dipole, and combined models parameterization from ab initio quantum chemistry. J Phys Chem B 103(22) 4730 t737... [Pg.253]

Although this section has emphasized possible errors in the observed data, the above considerations should not be used as a crutch to support an invalid or inaccurate model. In truth, in most circumstances the observed data are our best real indication of system behavior. Combining model simulations with an informed skepticism of both model and the observed data can lead to a better overall understanding of modeling natural systems. [Pg.163]

An alternative approach is to combine models with field measurements to assist in developing carbon budgets (Huggins et al. 1998). Clay et al. (2005) used first-order models to calculate the amount of residue returned to the soil from C3 and C4 plants over an 8-year period. Based on the mineralization rates and when the C3 and C4 residues were returned, the 813C signature of non-harvested biomass was determined. Based on the rates, carbon turnover, the amount of SOC mineralized, and the amount of fresh biomass incorporated into the SOC over an 8-year period were determined. [Pg.209]

Make a single combined model of a component, prior to implementing it. [Pg.630]

Ham H, Kim TJ, Boyce D (2005) Implementation and estimation of a combined model of interregional, multimodal commodity shipments and transportation network flows. Transportation Research Part B (39) 65-79... [Pg.267]

Jang Y, Jang S, Chang B, Park J (2002) A combined model of network design and production/distribution planning for a supply network. Computers Industrial Engineering 43 (1-2) 263-281... [Pg.268]

A reciprocal proportionality exists between the square root of the characteristic flow rate, t/A, and the thickness of the effective hydrodynamic boundary layer, <5Hl- Moreover, f)HL depends on the diffusion coefficient D, characteristic length L, and kinematic viscosity v of the fluid. Based on Levich s convective diffusion theory the combination model ( Kombi-nations-Modell ) was derived to describe the dissolution of particles and solid formulations exposed to agitated systems [(10), Chapter 5.2]. In contrast to the rotating disc method, the combination model is intended to serve as an approximation describing the dissolution in hydrodynamic systems where the solid solvendum is not necessarily fixed but is likely to move within the dissolution medium. Introducing the term... [Pg.140]

Fluid velocities using the basket method were determined to range between 0.3 and 5 cm/sec [25-200 rpm], and for the paddle method, between 1.8 and 37 cm/sec [25— 200 rpm]. Possible applications of these fluid velocity data may include their use to forecast in vitro dissolution rates and profiles of pure drug compounds for the paddle test employing an appropriate mathematical scenario/formula like the combination model. [Pg.153]

As mentioned earlier, Reynolds numbers determined for the bulk flow have to be discerned from Reynolds numbers characterizing a particle-liquid dissolution system. The latter were calculated for drug particles of different sizes using the Reynolds term according to the combination model. The kinematic viscosity of the dissolution medium at 37°C is about 7 x 10-03 cm2/sec. The fluid velocities (Ua) employing the paddle method at stirring rates of 50-150 rpm can be taken from the literature and may arbitrarily be used as the slip velocities at the particle surfaces. [Pg.160]

While Eq. (2) models submonolayer order-disorder transitions and Eq. (60) model multilayer adsorption, it is of course possible to formulate a combined model which considers the competition between order-disorder phenomena in the first layer and adsorption of further layers . Then instead of Eqs. (2), (60) we write, for the simple cubic lattice,... [Pg.134]

The first edition of this book appeared over fifteen years ago. It was the first ehemieal engineering textbook to combine modeling, simulation, and control. It also was the first chemical engineering book to present sampled-data control. This choice of subjects proved to he popular with both students and teachers and of eonsiderable practieal utihty. [Pg.746]

Hales, C. H.. A. M. Rollinson, and F. H. Shair. Experimental verification of linear combination model for relating indoor-outdoor pollutant concentrations. Environ. Sci. Technol. 8 452-453, 1974. [Pg.192]

Eikerling et al. ° used a similar approach except that they focus mainly on convective transport. As mentioned above, they use a pore-size distribution for Nafion and percolation phenomena to describe water flow through two different pore types in the membrane. Their model is also more microscopic and statistically rigorous than that of Weber and Newman. Overall, only through combination models can a physically based description of transport in membranes be accomplished that takes into account all of the experimental findings. [Pg.456]

If we were to continue this scheme of two-factor substitutions, we would accumulate a total of twelve different models, one for each factor combination in the study. However, it is possible to combine all twelve of these separate models in a single model through the use of dummy variables . These dummy variables can be used to turn on or turn off various terms in the combined model in such a way that the twelve separate models result. [Pg.382]

In Fig.la a lower slope ((j)=2.25) and higher Intercept (g=1.32) Is obtained for the low pressure region as compared to the slope (((>=2.60) and Intercept (g=1.09) for high pressure region. Since from Eq(13), a value of g close to 1 implies adherence to the solution-diffusion model. It appears that at low pressures where g = 1.32>1.0, a combined model of viscous and diffusive flow Is operative. This correlates with previous SEM studies In our laboratory (unpublished), where mlcro-pln holes were postulated to exist In the skin. The presence of such m-LcAO-p-Ln hoZ 6 In the surface can be used to explain the high g-value. Above 10 atm, the DDS-990 membrane Is compressed or compacted and the mlcro-pln holes filled. Thus g = l.O l.O implies adherence to the solution-diffusion model. [Pg.151]

Figure 8. Schematic illustration of bed cross section for the combination model. See text for explanation of nomenclature. Figure 8. Schematic illustration of bed cross section for the combination model. See text for explanation of nomenclature.

See other pages where Combined models is mentioned: [Pg.134]    [Pg.2067]    [Pg.28]    [Pg.1104]    [Pg.184]    [Pg.719]    [Pg.715]    [Pg.86]    [Pg.249]    [Pg.500]    [Pg.507]    [Pg.656]    [Pg.302]    [Pg.347]    [Pg.490]    [Pg.381]    [Pg.389]    [Pg.392]    [Pg.150]    [Pg.140]    [Pg.141]    [Pg.141]    [Pg.197]    [Pg.440]    [Pg.456]    [Pg.114]   
See also in sourсe #XX -- [ Pg.546 ]




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