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Equilibrium constants Conductivity, molar

Methods. Adsorption isotherms were run at constant feed molar ratio of C oS0 /Ci3eS0.. The feed solutions had a pH of 4.25 and a NaCl concentration of 0.15 M. Ten ml of feed solution was added to 0.5 g alumina in a screw top centrifuge tube and centrifuged at 700 RPM for 45 minutes at room temperature. The tube was then placed in a water bath at 30°C for four days, the liquid decanted from the mineral and analyzed. The surfactant concentrations were analyzed using high performance liquid chromatography with a conductivity detector. The solution pH after equilibration was determined using pH electrodes. The equilibrium pH increased to 6.8 at equilibrium because the PZC of alumina is approximately 9. [Pg.203]

Figures 1 to 3 present calculated equilibrium molar ratios of products to reactants as a function of temperature and total pressure of 1 and 100 atm. for the gas-carbon reactions (4), (7), and (5), (6), (4), (7), respectively. Up to 100 atm. over the temperature range involved, the fugacity coefficients of the gases are close to 1 therefore, pressures can be calculated directly from the equilibrium constant. From Fig. 1, it is seen that at temperatures above 1200°K. and at atmospheric pressure, the conversion of carbon dioxide to carbon monoxide by the reaction C - - COj 2CO essentially is unrestricted by equilibrium considerations. At elevated pressures, the possible conversion markedly decreases hence, high pressure has little utility for this reaction, since increased reaction rate can easily be obtained by increasing reaction temperature. On the other hand, for the reaction C -t- 2H2 CH4, the production of methane is seriously limited at one atmosphere pressure and practical operating temperatures, as seen in Fig. 2. Obviously, this reaction must be conducted at elevated pressures to realize a satisfactory yield of methane. For the carbon-steam reaction. Figures 1 to 3 present calculated equilibrium molar ratios of products to reactants as a function of temperature and total pressure of 1 and 100 atm. for the gas-carbon reactions (4), (7), and (5), (6), (4), (7), respectively. Up to 100 atm. over the temperature range involved, the fugacity coefficients of the gases are close to 1 therefore, pressures can be calculated directly from the equilibrium constant. From Fig. 1, it is seen that at temperatures above 1200°K. and at atmospheric pressure, the conversion of carbon dioxide to carbon monoxide by the reaction C - - COj 2CO essentially is unrestricted by equilibrium considerations. At elevated pressures, the possible conversion markedly decreases hence, high pressure has little utility for this reaction, since increased reaction rate can easily be obtained by increasing reaction temperature. On the other hand, for the reaction C -t- 2H2 CH4, the production of methane is seriously limited at one atmosphere pressure and practical operating temperatures, as seen in Fig. 2. Obviously, this reaction must be conducted at elevated pressures to realize a satisfactory yield of methane. For the carbon-steam reaction.
The way in which dissociation constants are obtained from experimental data is illustrated in Table 1.7, in which the dissociation equilibrium constant of acetic acid is computed from molar conductivities. The average value... [Pg.34]

Table 1.7 Calculation of the dissociation equilibrium constant of acetic acid from measured values of molar conductivity... Table 1.7 Calculation of the dissociation equilibrium constant of acetic acid from measured values of molar conductivity...
Ostwald s dilution law gives the relationship between the equilibrium constant K for a dissociation reaction and the molar conductivity A of the resulting solution of concentration c, which is... [Pg.128]

Ni(PEX)Br2 is intermediate in properties and behavior. In nonpolar solvents, such as dichloroethane, the compound exists as a neutral, molecular, 6-coordinate species having a normal, triplet, ground state, as inferred from molecular weight, magnetic moment, and electronic spectra. However, in nitromethane, at room temperature, the substance exhibits intermediate values for molar conductance (58 ohm at 10 M) and magnetic moment (2.65 BM at 9.44 x 10 M). Dilution experiments yield values for the molar conductance that are consistent with an equilibrium constant of 1.66 X 10 3 (T = 25°C.) for the process given in Equation 8. [Pg.626]

It is clear that from the integrated form of Equation (4) the volume of reaction can be obtained if the equilibrium constant can be determined over a range of pressure. If the volume of activation is not experimentally accessible for one of the directions of the reaction, A V can be used to calculate its value. Under certain conditions and with suitable properties of reactants and/or products it may be possible to determine their partial molar volumes, hence allowing development of a volume profile on an absolute volume basis, as noted above. Even if A V can be determined either from the pressure dependence of the equilibrium constant and/or from use of Equation (5), it may be possible to confirm its value by determination of the partial molar volumes from density measurements. The conditions for conducting successful determinations of partial molar volumes are rather stringent and will be described in Section 2. The method depends on measuring the density, d, of several solutions of different concentrations of the reactant or product. The following equation is used to obtain... [Pg.4]

In this table, all units are based on the molar scale and was obtained from the temperature dependence of the overall formation constant Based on the differences in these quantities with the two supporting electrolytes, the ion-association constant for LiCl was estimated as 10 -, which is in good agreement with the value 10 obtained from conductivity data. In PC-H2O mixtures up to [H2O] = 3.57 molar, the various equilibrium constants are given by... [Pg.177]

Conversely, Eq. (21.42) can be used to determine the degree of dissociation a of a weak electrolyte at a given concentration c by measuring the molar conductivity. Moreover, with the help of Eq. (21.41), the equilibrium constant of the substance becomes accessible. However, for these calculations we need the limiting molar conductivity A . This quantity is very difficult to find experimentally because the steep rise of the A at low concentrations makes an extrapolation to infinite dilution very uncertain. The law of independent migration of ions [Eq. (21.35)] offers a way out. hi the case of infinite dilution, the limiting molar conductivity of acetic acid is the sum of the contributions of cation and anion ... [Pg.511]

This handbook contains extensive tables of data for the more common Inorganic and organic aqueous electrolyte solutions. Properties covered include dielectric constants, activity coefficients, relative partial molar enthalpies, equilibrium constants, solubility products, conductivities, electrochemical potentials, Gibbs energies and enthalpies of formation, entropies, heat capacities, viscosities, and diffusion coefficients. Unfortunately, only a few of the tables contain references to the sources of the data. [Pg.787]

This shows how one may obtain the molar entropy of the adsorbed phase from an observation of the variation of in P with T, where P is the pressure of the gas in equilibrium with the adsorbate. The problem here is that one cannot readily devise an experiment in which the variation of in P with T is carried out at constant 4 It is much simpler to conduct experiments under conditions where As or T remains constant. [Pg.466]

Osmotic pressure (IT) - The excess pressure necessary to maintain osmotie equilibrium between a solution and the pure solvent separated by a membrane permeable only to the solvent. In an ideal dilute solution n = c RT, where Cb is the amount-of-substance concentration of the solute, is the molar gas constant, and T the temperature. [1,2] Ostwald dilution law - A relation forthe concentration dependence ofthe molar conductivity A of an electrolyte solution, viz.,... [Pg.112]

This book (about 800 pp.) is a treatise on the physical chemistry of electrolytic solutions with coverage of both equilibrium and non-equilibrium properties. The book includes tables of values of the equivalent conductance, dissociation constants, transference numbers, diffusion coefficients, relative apparent molar heat contents, activity coefficient, pH values, densities, and activity coefficients for many of the more common inorganic and organic electrolyte solutions. [Pg.761]

H-H ) - molar enthalpy departure frm the ideal gas state AHmix molar liquid heat of solution k - liquid thermal conductivity K - vapor-liquid equilibrium ratio P - absolute pressure Pref reference pressure R - gas constant T - absolute temperature - liquid molar volume - liquid partial molar volume X - mole fraction in liquid phase y - mole fraction in vapor phase relative volatility Y - liquid activity coefficient liquid viscosity... [Pg.85]

A completely dissociated electrolyte should obey the Debye-Hiickel equation and Onsager s equation (q.v.) in sufficiently dilute solutions. Many salts in water conform with this expectation, but some uniunivalent and unidivalent salts, and most of those of higher valence type, show abnormally low molar conductivities and activities. The deviations can be explained by association between cation and anion to form ion-pairs, and the equilibrium between free ions and ion-pairs can be formulated, in the same way as for a weak electrolyte, by writing Kd= 7c7Aa m/(l-a), where the 7s are the activity coefficients of cation and anion, a is the fraction of electrolyte present as free ions and Kd is the dissociation constant. The reciprocal of this, Ka, the association or stability constant, is also used, and it will be seen that pKa = pKd. The ion-pair itself may carry a net charge, e.g. [Pg.148]


See other pages where Equilibrium constants Conductivity, molar is mentioned: [Pg.219]    [Pg.52]    [Pg.341]    [Pg.286]    [Pg.289]    [Pg.6]    [Pg.475]    [Pg.57]    [Pg.129]    [Pg.84]    [Pg.227]    [Pg.144]    [Pg.66]    [Pg.4358]    [Pg.129]    [Pg.63]    [Pg.97]    [Pg.244]    [Pg.261]    [Pg.4357]    [Pg.316]    [Pg.419]   


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Conductance molar

Conductivity constant

Equilibrium conductance

Equilibrium conductivity

Molar conductivity

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