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Equilibrium analysis

The foregoing is an equilibrium analysis, yet some transient effects are probably important to film resilience. Rayleigh [182] noted that surface freshly formed by some insult to the film would have a greater than equilibrium surface tension (note Fig. 11-15). A recent analysis [222] of the effect of surface elasticity on foam stability relates the nonequilibrium surfactant surface coverage to the foam retention time or time for a bubble to pass through a wet foam. The adsorption process is important in a new means of obtaining a foam by supplying vapor phase surfactants [223]. [Pg.524]

When the kinetics are unknown, still-useful information can be obtained by finding equilibrium compositions at fixed temperature or adiabatically, or at some specified approach to the adiabatic temperature, say within 25°C (45°F) of it. Such calculations require only an input of the components of the feed and produc ts and their thermodynamic properties, not their stoichiometric relations, and are based on Gibbs energy minimization. Computer programs appear, for instance, in Smith and Missen Chemical Reaction Equilibrium Analysis Theory and Algorithms, Wiley, 1982), but the problem often is laborious enough to warrant use of one of the several available commercial services and their data banks. Several simpler cases with specified stoichiometries are solved by Walas Phase Equilibiia in Chemical Engineering, Butterworths, 1985). [Pg.2077]

To find the best a priori conditions of analysis, the equilibrium analysis, based on material balances and all physicochemical knowledge involved with an electrolytic system, has been done with use of iterative computer programs. The effects resulting from (a) a buffer chosen, (b) its concentration and (c) complexing properties, (d) pH value established were considered in simulated and experimental titrations. Further effects tested were tolerances in (e) volumes of titrants added in aliquots, (f) pre-assumed pH values on precision and accuracy of concentration measured from intersection of two segments obtained in such titrations. [Pg.83]

W.R. Smith and R.W. MIssen. Chemical Reaction Equilibrium Analysis. J. Wiley and Sons. New York (1982). [Pg.117]

The values of stress may be checked by simple equilibrium analysis. [Pg.220]

Ammonium carbamate solid (NH4C02NH2) decomposes at 313 K into ammonia and carbon dioxide gases. At equilibrium, analysis shows that there are 0.0451 atm of C02,0.0961 atm of ammonia, and 0.159 g of ammonium carbamate. [Pg.346]

This aqueous solution is 5.0 x 10 M HCIO4, so [ H3 O ] = [CIO4 ] = 5.0 x 10 M. The final concentrations are found using an equilibrium analysis. Set up a concentration table for the water dissociation equilibrium, and define the change in hydronium ion concentration as x ... [Pg.1211]

Titrations are treated like any other equilibrium analysis, but we must pay special attention to the major species present in the solution, because these change during the titration. The most common titrations are analysis of a weak acid using a solution of strong base and analysis of a weak base using a solution of strong acid. [Pg.1290]

After the addition of the non-radioactive material, the labeled material is added to the mixture and the mixture allowed to proceed toward equilibriim. In equilibrium analysis the order of addition of reagents is not critical as long as sufficient time is allowed for establishing equilibrium of the complete mixture (3,4). [Pg.59]

The role of the distribution of species in solution in determining the CdS film composition and structure was studied by Rieke and Bentjen [244], who performed equilibrium analysis of the cadmium-amine-hydroxide system to predict the spe-ciation in solution. The focus was on the formation of Cd(OH)2 and Cd(NH3) species due to their importance in film growfh. If was concluded fhat for deposition of high-quality, adherent, phase-pure CdS films, a surface cafalytically active toward thiourea decomposition is desirable. The Cd(OH)2 film was thought to be responsible for this effect. [Pg.134]

Time-resolved IR spectra of similar peptides following a laser-excited temperature jump showed two relaxation times, unfolding 160 ns and faster components <10 ns (Williams et al., 1996). These times are very sensitive to the length, sequence, and environment of these peptides, but do show that the fundamental helix unfolding process is quite fast. These fast IR data have been contrasted with Raman and fluorescence-based T-jump experiments (Thompson et al., 1997). Raman experiments at various temperatures have suggested a folding in 1 /xs, based on an equilibrium analysis (Lednev et al., 2001). But all agree that the mechanism of helix formation is very fast. [Pg.158]

The proposed mechanism of the exchange suggests that the intermolecu-lar exchange should not involve the center CH bond. On the other hand, if the exchange were random among the six hydrogen positions, one would expect about one out of three molecules to have a deuterium on the central carbon at equilibrium. Analysis by IR shows no evidence for a deuterium at this position even for the nearly equilibrated surface products. Thus, this result also conforms to expectations based on the proposed mechanism. [Pg.40]

Like all formulations of the multicomponent equilibrium problem, these equations are nonlinear by nature because the unknown variables appear in product functions raised to the values of the reaction coefficients. (Nonlinearity also enters the problem because of variation in the activity coefficients.) Such nonlinearity, which is an unfortunate fact of life in equilibrium analysis, arises from the differing forms of the mass action equations, which are product functions, and the mass balance equations, which appear as summations. The equations, however, occur in a straightforward form that can be evaluated numerically, as discussed in Chapter 4. [Pg.44]

Smith, W. R. and R. W. Missen, 1982, Chemical Reaction Equilibrium Analysis Theory and Algorithms. Wiley, New York. [Pg.530]

Smith, W.R., and R.W. Missen (1991), Chemical Reaction Equilibrium Analysis, Krieger, Malabar, FL. [Pg.655]

RONALD W. MISSEN is Professor Emeritus (Chemical Engineering) at the University of Toronto. He received his B.Sc, and M.Sc. in chemical engineering from Queen s University, Kingston, Ontario, and his Ph.D. in physical chemistry from the University of Cambridge, England. He is the co-author of CHEMICAL REACTION EQUILIBRIUM ANALYSIS, and has authored or co-authored about f 50 research articles. He is a fellow of the Chemical Institute of Canada and the... [Pg.674]

High-pressure experiments promise to provide insight into chemical reactivity under extreme conditions. For instance, chemical equilibrium analysis of shocked hydrocarbons predicts the formation of condensed carbon and molecular hydrogen.17 Similar mechanisms are at play when detonating energetic materials form condensed carbon.10 Diamond anvil cell experiments have been used to determine the equation of state of methanol under high pressures.18 We can then use a thermodynamic model to estimate the amount of methanol formed under detonation conditions.19... [Pg.162]

The general equilibrium structure of these models is based on Arrow and Debreu (1954). An introduction to applied general equilibrium analysis can be found in Shoven and Whalley (1984). CGE models are used in almost all economic fields to quantify the impact of various policy reforms. For an overview of these studies, see, e.g., Bhattacharyya (1996), Conrad (2002), Gottfried et al. (1990), or Gunning and Keyzer (1995). [Pg.544]

FIGURE 9.23 Adiabatic flame temperature for stoichiometric combustion of methane in mixtures of oxygen with nitrogen and oxygen with carbon dioxide, computed using NASA s Chemical Equilibrium Analysis (CEA) program [52]. [Pg.545]

STANJAN The Element Potential Method for Chemical Equilibrium Analysis Implementation in the Interactive Program STANJAN, W.C. Reynolds, Thermosciences Division, Department of Mechanical Engineering, Stanford University, Stanford, CA, 1986. A computer program for IBM PC and compatibles for making chemical equilibrium calculations in an interactive environment. The equilibrium calculations use a version of the method of element potentials in which exact equations for the gas-phase mole fractions are derived in terms of Lagrange multipliers associated with the atomic constraints. The Lagrange multipliers (the element potentials ) and the total number of moles are adjusted to meet the constraints and to render the sum of mole fractions unity. If condensed phases are present, their populations also are adjusted to achieve phase equilibrium. However, the condensed-phase species need not be present in the gas-phase, and this enables the method to deal with problems in which the gas-phase mole fraction of a condensed-phase species is extremely low, as with the formation of carbon particulates. [Pg.751]

Haas, A. L. and Rose, 1. A. The mechanism of ubiquitin activating enzyme. A kinetic and equilibrium analysis, J Biol Chem 1982, 257, 10329-10337. [Pg.41]

F. Van Zeggeten and S. H. Storey, The Computation of Chemical Equilibria, Cambridge University Press, Cambridge, UK, 1970 W. R. Smith and R. W. Missen, Chemical Reaction Equilibrium Analysis Theory and Algorithms, Wiley-Interscience, New York, 1982 W. J. Lyman, W. F. Reehl, and D. H. Rosenblatt, eds.. Handbook of Chemical Property Estimation Methods, McGraw-HiU, New York, 1982 C. M. Wal and S. G. Hutchison, J. Chem. Educ. 66, 546 (1989) F. G. Heherich, Chemical Engineering Education, 1989. [Pg.525]

The first term is in fact important only at very low ionic strengths thus for cases used in equilibrium analysis one has... [Pg.274]

In equilibrium analysis studies carried out in the presence of an inert salt (medium salt NX) and small (trace) concentrations of the reactants, only the terms involving have to be considered in Eq. (6.33), while those involving can be neglected. Nevertheless, as the main difficulty... [Pg.274]

Binding of heme by isolated N-domain causes a change in sedimentation coefficient consistent with a more compact conformation and leads to the more avid association with the C-domain (125). Sedimentation equilibrium analysis showed that the Kd decreases from 55 pM to 0.8 pM (Fig. 5) (106). In addition, the calorimetric AH (-1-11 kcal/mol) and AS (-1-65 kcal/mol K) for the heme-N-domain-C-domain interaction and the AH (-3.6 kcal/mol) and AS (-1-8.1 kcal/mol K) derived from van t Hoff analysis of ultracentrifuge data for the interaction in the absence of heme indicate that hydrophobic interactions predominate in the presence of heme and a mix (e.g., hydrophobic and van der Waals forces) drives the interaction in the absence of heme. However, FTIR spectra (Fig. 6) indicate that little change in the secondary structure of domains or intact hemopexin occurs upon heme binding (104). [Pg.215]

Fig. 5. Sedimentation equilibrium analysis of hemopexin domain interactions. Mixtures of N- and C-domain were centrifuged to equilibrium at 25 C in the absence (upper panels) and presence (lower panels) of heme. Nonlinear fitting procedures were performed to obtain apparent values, and residuals of the fits are shown in the top portion of each panel (106). Fig. 5. Sedimentation equilibrium analysis of hemopexin domain interactions. Mixtures of N- and C-domain were centrifuged to equilibrium at 25 C in the absence (upper panels) and presence (lower panels) of heme. Nonlinear fitting procedures were performed to obtain apparent values, and residuals of the fits are shown in the top portion of each panel (106).
STEP FLUCTUATIONS FROM EQUILIBRIUM ANALYSIS TO STEP UNBUNCHING AND CLUSTER DIFFUSION IN A UNIFIED PICTURE... [Pg.83]

An equilibrium analysis of the composition of the reformate as a function of temperature, at 1 atm absolute pressure, is shown in Figure 25. [Pg.230]

The determination that the low MW, acetylated aspen lignins examined actually fit universal calibration, however, must be deferred to future studies comparing these data to results from LALLS and sedimentation equilibrium analysis (if possible). [Pg.105]

Kinetics and equilibrium analysis To use Patterson s model (eq. (4.52)), we first need the parameter w, and thus the equilibrium liquid-phase concentration Ce. The maximum loading of the zeolite particles for the specific initial concentration can be calculated by means of the equilibrium relationship (eq. (4.5)) ... [Pg.298]


See other pages where Equilibrium analysis is mentioned: [Pg.450]    [Pg.176]    [Pg.286]    [Pg.377]    [Pg.103]    [Pg.78]    [Pg.162]    [Pg.163]    [Pg.39]    [Pg.308]    [Pg.308]    [Pg.344]    [Pg.334]   
See also in sourсe #XX -- [ Pg.38 ]

See also in sourсe #XX -- [ Pg.38 ]




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Analysis of Solution Equilibria

Analysis of complex equilibria

Asymptotic analysis equilibrium approach

Binding equilibrium, analysis

Electrochemical equilibria analysis

Equilibrium catalyst analysis

Equilibrium constants frontal analysis

Equilibrium potential analysis

Equilibrium stages McCabe-Thiele analysis

Equilibrium techniques in saturation analysis

Equilibrium-limited analysis

Frontal Analysis, Displacement and the Equilibrium-Dispersive Model

Graphical Analysis of Equilibrium-Limited Adiabatic Reactors

Numerical Analysis of the Equilibrium-Dispersive Model

Sedimentation Equilibrium Analysis

Solubility equilibria analysis

Vapor-liquid equilibrium analysis simulation

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