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Effects of Mixing

Isobutane is almost insoluble in the liquid acid catalysts used in refinery alkylation. Therefore, intense mixing is necessary to make sure that at least this low isobutene equilibrium concentration is maintained throughout the readion in the acid phase to allow the reaction to proceed properly. As the alkylation readion occurs at or near [Pg.656]


The enthalpy of a vapor mixture is obtained first, from zero-pressure heat capacities of the pure components and second, from corrections for the effects of mixing and pressure. [Pg.83]

The perturbations in this case are between a singlet and a triplet state. The perturbation Hamiltonian, H, of the second-order perturbation theory is spin-orbital coupling, which has the effect of mixing singlet and triplet states. [Pg.1142]

Concentrations of moderator at or above that which causes the surface of a stationary phase to be completely covered can only govern the interactions that take place in the mobile phase. It follows that retention can be modified by using different mixtures of solvents as the mobile phase, or in GC by using mixed stationary phases. The theory behind solute retention by mixed stationary phases was first examined by Purnell and, at the time, his discoveries were met with considerable criticism and disbelief. Purnell et al. [5], Laub and Purnell [6] and Laub [7], examined the effect of mixed phases on solute retention and concluded that, for a wide range of binary mixtures, the corrected retention volume of a solute was linearly related to the volume fraction of either one of the two phases. This was quite an unexpected relationship, as at that time it was tentatively (although not rationally) assumed that the retention volume would be some form of the exponent of the stationary phase composition. It was also found that certain mixtures did not obey this rule and these will be discussed later. In terms of an expression for solute retention, the results of Purnell and his co-workers can be given as follows,... [Pg.106]

In contrast molecular interaction kinetic studies can explain and predict changes that are brought about by modifying the composition of either or both phases and, thus, could be used to optimize separations from basic retention data. Interaction kinetics can also take into account molecular association, either between components or with themselves, and contained in one or both the phases. Nevertheless, to use volume fraction data to predict retention, values for the distribution coefficients of each solute between the pure phases themselves are required. At this time, the interaction kinetic theory is as useless as thermodynamics for predicting specific distribution coefficients and absolute values for retention. Nevertheless, it does provide a rational basis on which to explain the effect of mixed solvents on solute retention. [Pg.140]

The theory of losses is very complex. The effect of mixing on the total pressure has been investigated. The calculated results qualitatively match the measured results. Friction in impeller channel and casing decreases the total pressure. [Pg.757]

Lee, Y.-M. and Lee, L.J., 1987. Effect of mixing and reaction on a fast step growth polymerization. International Polymer Processing, 1, 144-152. [Pg.313]

Tosuii, G., 1988. All experimental study of the effect of mixing on the particle size distribution in BaS04 precipitation reaction. 6th European Conference on Mixing, Pavia, pp. 161-170. [Pg.325]

B. Effect of Mixed Solvent-Water Systems on Grafting... [Pg.538]

From Figure 8-31 the effect of mixed and unmixed pools of liquid can be noted. For a completely mixed tray, there is no concentration gradient from inlet to outlet, and therefore the entire tray has a uniform composition. The degree of mixing across the tray as determined by the number of discrete mixing pools on the tray has an effect on the relationship between Eqg E y as a function of X. [Pg.45]

A change in the agitation intensity or gas flow rate will change 0. As a result, b, c0, and the total mass-transfer rate are affected. Thus, the effect of mixing in the vessel is considered by indirect mechanisms. [Pg.355]

Figure 5.22 reveals the ability of solid state electrochemistry to create new types of adsorption on metal catalyst electrodes. Here oxygen has been supplied not from the gas phase but electrochemically, as 02 via current application for a time, denoted tj, of 1=15 pA at 673 K, i.e. at the same temperature used for gaseous O2 adsorption (Fig. 5.21). Figure 5.23 shows the effect of mixed gaseous-electrochemical adsorption. The Pt surface has been initially exposed to po2 =4x1 O 6 Torr for 1800 s (7.2 kL) followed by electrochemical O2 supply (1=15 pA) for various time periods ti shown on the figure, in order to simulate NEMCA conditions. [Pg.228]

Reactor Conditions for Experimental Runs. Operating conditions for the continuous, stirred tank reactor runs were chosen to study the effects of mixing speed on the monomer conversion and molecular weight distribution at different values for the number average degree of polymerization of the product polymer. [Pg.309]

To differentiate between the micro-mixed reactor with dead-polymer and the by-pass reactor models in this investigation, the effect of mixing speed on the value of "( )" was observed. As illustrated in Table V, the value (j>" is not observed to increase with decreasing mixing speed as would be expected for a by-pass reactor. This rules out the possibility of a by-pass model and further substantiates the dead-polymer model. [Pg.322]

Treybig, M. N., "Effect of Mixing on Polymerization of Styrene," Master of Science Thesis, Texas A M University, College Station, Texas (1977). [Pg.326]

First-order means that we consider nothing beyond that described here. In second-order , we would include the effects of mixing between ground and excited states brought about by the magnetic field. This is briefly discussed under second-order Zeeman effects later. [Pg.84]

Since EPDM is a cheaper elastomer, it is often added to SBR to reduce cost. Zhao et al. have studied the effects of curative and accelerator concentration as well as the effect of mixing on the properties of ablend compound containing 70 parts of SBR and 30 parts of EPDM [41]. Table 11.18 gives the general formulation of the blend compounds. [Pg.327]

A few ex vivo and in vivo studies have been published claiming an antigene (and antisense) effect of mixed purine/pyrimidine sequence PNA [48, 49, 78-80]. However, as pointed out by us in recent reviews [81, 82] these studies lack fundamental controls such as the inclusion of relevant internal standards as a control for sequence-specific non-antigene/antisense effects, thus confirmatory studies are warranted. The in vivo antigene studies from Richelsoris group [79, 83] completely lack a rational basis for the claimed effects. First of all there is no evidence that... [Pg.165]

Fig. 2 shows the liquid product distributions over catalysts. Main product over ferrierite is C5 hydrocarbon, while products were distributed over mainly C,-C, over HZSM-5. Table 4 shows the effect of mixing ratio on product distribution. While HZSM-5/PP ratio does not affect product distribution, higher amount of gas is obtained with increasing ferrierite/PP ratio. This is ascribed to the increased possibility of polypropylene diffusion into pore as the amount of ferrierite is increased. [Pg.319]

Henschel, C. J. (1943). The effect of mixing surface temperatures on dental cementation. Journal of the American Dental Association, 30, 1582-9. [Pg.270]

They calculated the change in 8 0 values of hydrothermally altered volcanic rocks as a function of water to rock ratio by weight and temperature, assuming that oxygen isotopic equilibrium is attained in a closed system, and demonstrated that the increase in 8 0 values of altered andesitic rocks from the veins towards peripheral zones can be interpreted as a decrease in temperature from the vein system (Fig. 1.135). In their calculations, the effect of mixing of hydrothermal solution with groundwater was not considered. [Pg.187]

Maximum effect of mixing in different liquids is observed at different concentrations of diluted oxygen. For example, in methanol this concentration is equal to 2-tO volume % (in other solvents this value may be different). These conecentrations are called the critical concentrations and are denoted. At oxygen concentrations above the... [Pg.263]

The effect of mixing Ac for various liquids with different values of the dielectric constant e is seen from Fig. 4.26. At lower values of e of the solvent, critical concentration also decreases. Moreover, at... [Pg.263]


See other pages where Effects of Mixing is mentioned: [Pg.452]    [Pg.1058]    [Pg.1821]    [Pg.1905]    [Pg.256]    [Pg.256]    [Pg.59]    [Pg.52]    [Pg.216]    [Pg.230]    [Pg.394]    [Pg.354]    [Pg.47]    [Pg.60]    [Pg.746]    [Pg.297]    [Pg.321]    [Pg.84]    [Pg.97]    [Pg.155]    [Pg.113]    [Pg.364]    [Pg.33]    [Pg.263]    [Pg.263]    [Pg.263]   
See also in sourсe #XX -- [ Pg.468 , Pg.474 , Pg.475 ]




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Effect of Lateral Mixing

Effect of Mixing on Systems Undergoing Chemical Reactions

Effect of Orientation on Distributive Mixing - Erwins Ideal Mixer

Effect of changes in mixed layer depth

Effect of the mixing time

Effects of Doped Ions on Mixed Potential

Effects of J Mixing

Effects of Mixing on Reactor Performance

Effects of Organic Cosolvent in Mixed Aqueous Solution on the Reaction Rates

Entropy of mixing effects

Heat Effects of Mixing Processes

Heat effects of mixing

Mixed effect

Mixed solvent effect on processes of complex formation

Mixing effect

Modeling of Nonideal Flow or Mixing Effects on Reactor Performance

Reactions effect of mixing

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