Big Chemical Encyclopedia

Chemical substances, components, reactions, process design ...

Articles Figures Tables About

Fixed phase approximation

In fact, (3.22) is the usual stationary phase approximation, performed however for an infinitedimensional path integral, which picks up the trajectories with classical action S. Further, at fixed time t we take the integral over Xi again in the stationary phase approximation, which gives... [Pg.42]

As discussed in Chapter 3, proteins and mABs distribute initially into the plasma volume and then more slowly into the interstitial fluid space. It can be seen from Table 32.11 that the initial distribution volume of interleukin-2 (IL-2) IL-12/ granulocyte colony-stimulating factor (G-CSF)/ and recombinant tissue plasminogen activator (rt-PA) approximates that of plasma volume. In contrast/ the initial distribution volume of FIX is approximately twice that of plasma volume. On the other hand/ the volumes of distribution at steady state (Vd(ss)) for IL-12/ G-CSF/ and rt-PA are considerably smaller than is the Vd(ss) of inuliii/ a marker for extracellular fluid space (ECF). When distribution volume estimates are much less than expected values for ECF/ they could reflect the slow transport of large molecules across membranes and the fact that either assay sensitivity or sampling time has been inadequate to characterize the true elimination phase of the compound. [Pg.487]

Here only a few of the highlights of the extensive study will be mentioned for the simplest case of equal A and B site hard-core diameters, and an equimolar mixture of chains of N sites each (< =i). The A chain aspect ratio is fixed at approximately 1.3, which is representative of a polymer such as polyethylene. Thus, the structural asymmetry variable = 2(rg - r )/(rg -I- F ) < 0 for most experimental polyolefin mixtures since unbranched polyethylene generally has the largest aspect ratio of the saturated hydrocarbon polymers. Figure 17 shows spinodal phase boundaries based on Eq. (4.5) for two reduced densities representative of a dense melt and concentrated solution (as studied by simulation). There are several important features. ... [Pg.50]

While it is not essential to the method, frozen Gaussians have been used in all applications to date, that is, the width is kept fixed in the equation for the phase evolution. The widths of the Gaussian functions are then a further parameter to be chosen, although it appears that the method is relatively insensitive to the choice. One possibility is to use the width taken from the harmonic approximation to the ground-state potential surface [221]. [Pg.297]

The accuracy of the CSP approximation is, as test calculations for model. systems show, typically very similar to that of the TDSCF. The reason for this is that for atomic scale masses, the classical mean potentials are very similar to the quantum mechanical ones. CSP may deviate significantly from TDSCF in cases where, e.g., the dynamics is strongly influenced by classically forbidden regions of phase space. However, for simple tunneling cases it seems not hard to fix CSP, by running the classical trajectories slightly above the barrier. In any case, for typical systems the classical estimate for the mean potential functions works extremely well. [Pg.369]

Benzene-Based Catalyst Technology. The catalyst used for the conversion of ben2ene to maleic anhydride consists of supported vanadium oxide [11099-11-9]. The support is an inert oxide such as kieselguhr, alumina [1344-28-17, or sUica, and is of low surface area (142). Supports with higher surface area adversely affect conversion of benzene to maleic anhydride. The conversion of benzene to maleic anhydride is a less complex oxidation than the conversion of butane, so higher catalyst selectivities are obtained. The vanadium oxide on the surface of the support is often modified with molybdenum oxides. There is approximately 70% vanadium oxide and 30% molybdenum oxide [11098-99-0] in the active phase for these fixed-bed catalysts (143). The molybdenum oxide is thought to form either a soUd solution or compound oxide with the vanadium oxide and result in a more active catalyst (142). [Pg.455]

Some details of this new process have been pubUshed by UOP (86). UOP claims equal or better LAB product quaUty via the fixed-bed process compared with the conventional Hquid-phase process employing HP acid catalyst. The new technology requites approximately 15% lower capital investment, mosdy the result of the elimination of safety equipment and equipment related to HP acid neutralization. [Pg.52]

Determination of Controlling Rate Factor The most important physical variables determining the controlhng dispersion factor are particle size and structure, flow rate, fluid- and solid-phase diffu-sivities, partition ratio, and fluid viscosity. When multiple resistances and axial dispersion can potentially affect the rate, the spreading of a concentration wave in a fixed bed can be represented approximately... [Pg.1516]

Parametric studies showed that mass diffusion in the gas phase could be neglected under most conditions. The calculations also show that the selection of the hypergolic combination (i.e., the gaseous oxidizer and the propellant system) fixes all of the parameters except the initial temperature and the oxidizer concentration. A general solution of the model shows that the ignition-delay time is approximately rated to the gaseous oxidizer concentration by the relation... [Pg.17]

In the semiclassical centrifugal sudden (SCS) approximation some additional simplifications were made, which permit us to estimate the scattering phase by Eq. (5.50). Therefore the accuracy of SCS has to be checked separately. Fortunately, for the Ar-N2 system some cross-sections were calculated by the BFCP method [200] as well as by the CC method [206], which is considered to be the best. Using the same potential as in [209] the SCS cross-sections were found in [191] for fixed total energy of collisions E. The results are compared in Table 5.1. [Pg.170]

The most commonly employed model is the early uptake (EU) model, where U is deemed to have been taken up sufficiently shortly after burial for the bone to approximate to a closed system. Justification for the validity of early uptake seems to have stemmed from Szabo s (1979) suggestion, later elaborated on by Rae and Ivanovich (1986), that Uranium is fixed in the bone in the U oxidation state, facilitated by the reduction of U by decay products of the organic phase of bone, collagen. Since the bulk of collagen is lost rapidly from the bone (on the U-series time-scale at least), it is assumed Uranium will be taken up rapidly, and then uptake will cease. [Pg.609]


See other pages where Fixed phase approximation is mentioned: [Pg.656]    [Pg.112]    [Pg.656]    [Pg.112]    [Pg.62]    [Pg.337]    [Pg.644]    [Pg.133]    [Pg.35]    [Pg.178]    [Pg.4]    [Pg.122]    [Pg.471]    [Pg.365]    [Pg.72]    [Pg.505]    [Pg.382]    [Pg.283]    [Pg.2377]    [Pg.779]    [Pg.160]    [Pg.198]    [Pg.109]    [Pg.497]    [Pg.143]    [Pg.397]    [Pg.143]    [Pg.137]    [Pg.288]    [Pg.159]    [Pg.131]    [Pg.207]    [Pg.102]    [Pg.298]    [Pg.33]    [Pg.302]    [Pg.319]    [Pg.542]   
See also in sourсe #XX -- [ Pg.656 ]




SEARCH



Fixed-phase approximation, Monte Carlo

Phase approximation

© 2024 chempedia.info