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Oxygen electrolyte concentration

Gas and liquid systems are explained by solubility. The solubility of oxygen at room temperature is about 10 ppm therefore the concentration of oxygen is 10 ppm (oxygen flux, Na). The solubility of oxygen at 0 °C is double that at 35 °C. Also, the solubility decreases if the electrolyte concentration is increased. The concentrations of oxygen in the gas phase and liquid phase are related to each other by the Raoult-Dalton equilibrium law. [Pg.30]

The electrolyte concentration is very important when it comes to discussing mechanisms of ion transport. Molar conductivity-concentration data show conductivity behaviour characteristic of ion association, even at very low salt concentrations (0.01 mol dm ). Vibrational spectra show that by increasing the salt concentration, there is a change in the environment of the ions due to coulomb interactions. In fact, many polymer electrolyte systems are studied at concentrations greatly in excess of 1.0 mol dm (corresponding to ether oxygen to cation ratios of less than 20 1) and charge transport in such systems may have more in common with that of molten salt hydrates or coulomb fluids. However, it is unlikely that any of the models discussed here will offer a unique description of ion transport in a dynamic polymer electrolyte host. Models which have been used or developed to describe ion transport in polymer electrolytes are outlined below. [Pg.129]

Figure 26. Predictions of the Adler model shown in Figure 25 assuming interfacial electrochemical kinetics are fast, (a) Predicted steady-state profile of the oxygen vacancy concentration ( ) in the mixed conductor as a function of distance from the electrode/electrolyte interface, (b) Predicted impedance, (c) Measured impedance of Lao.6Cao.4Feo.8-Coo.203-(5 electrodes on SDC at 700 °C in air, fit to the model shown in b using nonlinear complex least squares. Data are from ref 171. Figure 26. Predictions of the Adler model shown in Figure 25 assuming interfacial electrochemical kinetics are fast, (a) Predicted steady-state profile of the oxygen vacancy concentration ( ) in the mixed conductor as a function of distance from the electrode/electrolyte interface, (b) Predicted impedance, (c) Measured impedance of Lao.6Cao.4Feo.8-Coo.203-(5 electrodes on SDC at 700 °C in air, fit to the model shown in b using nonlinear complex least squares. Data are from ref 171.
The fluorescence properties of two fulvic acids, one derived from the soil and the other from river water, were studied. The maximum emission intensity occurred at 445-450 nm upon excitation at 350 nm, and the intensity varied with pH, reaching a maximum at pH 5.0 and decreasing rapidly as the pH dropped below 4. Neither oxygen nor electrolyte concentration affected the fluorescence of the fulvic acid derived from the soil. Complexes of fulvic acid with copper, lead, cobalt, nickel and manganese were examined and it was found that bound copper II ions quench fulvic acid fluorescence. Ion-selective electrode potentiometry was used to demonstrate the close relationship between fluorescence quenching and fulvic acid complexation of cupric ions. It is suggested that fluorescence and ion-selective electrode analysis may not be measuring the same complexation phenomenon in the cases of nickel and cobalt complexes with fulvic acid. [Pg.113]

Ion Electrolyte Concentration (molarity) Ion-oxygen distance i io (A) Coordination Method"/ reference... [Pg.214]

This is because the apparent activation energies for the interfacial processes are, in general, higher than those for oxygen ionic transport in solid electrolytes (Yamamoto, 2000). The reduction of the working temperature results in a lower oxygen vacancy concentration with concomitant increase of the role of ionic conductivity of electrode material. [Pg.240]

Many X-ray diffraction studies of electrolyte solutions have been carried out in aqueous solutions [Gl, 4, 5]. Values of the most probable distance, between the oxygen atom in water and a number of monoatomic ions are summarized in table 5.1. In the case of the cations, this distance reflects the radius of the cation plus the effective radius of the water molecule measured in the direction of the lone pairs on oxygen. In the case of alkali metals, the effective radius of water increases from 122 pm for Li" " to 131 pm for Cs when the Shannon and Prewitt radii are assumed for the cations (see section 3.2), the average value being 127 pm. This result can be attributed to the observation that the coordination number for water molecules around an alkali metal or alkaline metal earth cation changes with cation size and electrolyte concentration. In the case of the Li" " ion, this number decreases from six in very dilute solutions to four in concentrated solutions [5]. Because of the electrostatic character of the interaction between the cation and water molecules, these molecules exchange rapidly with other water molecules in their vicinity. For this reason, the solvation coordination number should be considered as an average. [Pg.209]

Soil has long been considered as a chemical system due to its semipermeability to chemicals, bioactivity, interactions with chemicals, and so on. As a result, soil has been idealized as a leaky semipermeable membrane in chemical osmosis to explain various abnormal transport phenomena of water and chemicals in soil (Hanshaw, 1972 Marine and Fritz, 1981 Fritz and Marine, 1983 Yeung, 1990 Keijzer, Kleingeld, and Loch, 1999) as a Donnan membrane (Donnan, 1924) to examine the influences of soil type, water content, electrolyte concentration, and the cation and anion distribution in pore fluid on electroosmotic flow of fluid in soil (Gray and Mitchell, 1967) as a bioreactor to evaluate the impact of oxygen transfer on efficiency of bioremediation (Woo and Park, 1997) and so on. [Pg.67]

Under conditions of oxygen or electrolyte concentration gradients, or due to heterogeneities of the metallic substrate, the cathodic and anodic sites may be separated. For each of the two electrodes, the equilibrium potential for their actual conditions can be determined by the Nemst equation. The electromotive force (EMF) for the corrosion process to occur is the difference between the two equilibrium potentials. When the cathode and the anode are short-circuited, a mixed potential results, known as corrosion potential, f corr- The value of corr lies between the two separate electrode potentials, although shifted towards the equilibrium potential of the faster reaction. This situation can be easily visualized with the help of the... [Pg.510]

Identical metab in contact with solutions of different concentrations The metal dissolves from the electrode immersed in a dilute solution, and is deposited on the electrode that is immersed in a more concentrated solution. The corrosion stops when the electrolyte concentration is homogeneous at the interfaces of both of electrodes. The other type of electrochemical concentration cell is known as a differential aeration cell. The electrode potential difference in this case results from different oxygen aeration of the electrodes. This type of corrosion initiates crevice corrosion in aluminum or stainless steel when exposed to a chloride environment. [Pg.32]


See other pages where Oxygen electrolyte concentration is mentioned: [Pg.214]    [Pg.183]    [Pg.430]    [Pg.81]    [Pg.282]    [Pg.306]    [Pg.109]    [Pg.190]    [Pg.35]    [Pg.123]    [Pg.212]    [Pg.494]    [Pg.23]    [Pg.815]    [Pg.249]    [Pg.408]    [Pg.74]    [Pg.397]    [Pg.567]    [Pg.618]    [Pg.432]    [Pg.46]    [Pg.59]    [Pg.216]    [Pg.125]    [Pg.491]    [Pg.233]    [Pg.5076]    [Pg.16]    [Pg.150]    [Pg.322]    [Pg.58]    [Pg.39]    [Pg.2727]    [Pg.432]    [Pg.1465]    [Pg.95]    [Pg.116]    [Pg.288]    [Pg.122]   


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