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Mass electrolytes

PZC/IEP of Chitosan-Polymethacrylic Acid Composites chitosan (Mass%) Electrolyte T Method Instrument... [Pg.858]

Typical purities of the elements employed for sample preparation were iodide zirconium (99.96 mass%), electrolytic iron and chromium (99.96 mass%). In a few cases metal purities were not indicated, while in a few others N, O, Si and selected metal impurities were analyzed and reported. Alloys were generally prepared by arc melting. [Pg.412]

Figure 23-1. Acceleration of the bromoacetate-thiosulfate reaction at 25 C by various low-molar-mass and high-molar-mass electrolytes as a function of the molar concentration (El) with respect to catalytically effective groups. PEI nHCl, Poly (ethylene imine hydrochloride) TP 5HC . tetraethylene pentamine hydrochloride DT-3HC1, diethylene triamine hydrochloride. The bromoacetate and thiosulfate concentrations were, in each case, 0.01 mol liter unless otherwise noted. (After N. Ise and F. Matsui.)... Figure 23-1. Acceleration of the bromoacetate-thiosulfate reaction at 25 C by various low-molar-mass and high-molar-mass electrolytes as a function of the molar concentration (El) with respect to catalytically effective groups. PEI nHCl, Poly (ethylene imine hydrochloride) TP 5HC . tetraethylene pentamine hydrochloride DT-3HC1, diethylene triamine hydrochloride. The bromoacetate and thiosulfate concentrations were, in each case, 0.01 mol liter unless otherwise noted. (After N. Ise and F. Matsui.)...
The Electrolyte Environment. The electrolyte environment also needs to be described to characterize a polyelectrolyte system. Polyelectrolytes dissolved or swollen in a solvent are bathed in a dielectric medium that typically includes, in addition to other polymer chains and liberated counterions, some level of added or ambient low molar mass electrolyte. A full system description therefore includes information about the solvent medium and any added electrolyte. [Pg.6018]

The rates of the self-discharge reactions also depend on temperature, additives to the active mass, electrolyte formulation, and grid alloy composition. As the surface of the electrodes is covered by PbS04 (the product of the self-discharge reactions), the state of charge of the electrodes begins to affect the rate of the self-discharge process. [Pg.13]

The modification of the dependence implies that the Coulomb force originating from a kation practically disappears at distances r above the Debye screening length d- The effect was explained for the first time in 1923 in the famous theory developed by Debye and Hiickel, and we briefly sketch its content. The explanation refers at first to low molar mass electrolytes, but the results can be transferred to polyelectrolyte solutions. [Pg.93]

Ion chemistry is a product of the 20th century. J J Thomson discovered the electron in 1897 and identified it as a constituent of all matter. Free positive ions (as distinct from ions deduced to exist in solids or electrolytes) were first produced by Thomson just before the turn of the century. He produced beams of light ions, and measured their mass-to-charge ratios, in the early 1900s, culminating in the discovery of two isotopes of neon in 1912 [1]. This year also marked Thomson s discovery of which turns out to be the... [Pg.798]

It is conventional to use molality—moles of solute per kilogram of solvent (symbol m)—as the concentration unit in electrolyte thermodynamics. Accordingly, we shall represent the concentrations of both the indifferent electrolyte and the polymer in these units in this section m3 and m2, respectively. In the same dilute (with respect to polymer) approximation that we have used elsewhere in this chapter, m2 is related to the mass volume system of units C2 by... [Pg.570]

Other methods attempt to probe the stmcture of the foam indirectly, without directly imaging it. Eor example, since the Hquid portion of the foam typically contains electrolytes, it conducts electrical current, and much work has been done on relating the electrical conductivity of a foam to its Hquid content, both experimentally (15) and theoretically (16). The value of the conductivity depends in a very complex fashion on not only the Hquid content and its distribution between films and borders, but the geometrical stmcture of the bubble packing arrangement. Thus electrical measurements offer only a rather cmde probe of the gas Hquid ratio, a quantity that can be accurately estimated from the foam s mass density. [Pg.429]

The manufacture of metal in powder form is a complex and highly engineered operation. It is dominated by the variables of the powder, namely those that are closely connected with an individual powder particle, those that refer to the mass of particles which form the powder, and those that refer to the voids in the particles themselves. In a mass of loosely piled powder, >60% of the volume consists of voids. The primary methods for the manufacture of metal powders are atomization, the reduction of metal oxides, and electrolytic deposition (15,16). Typical metal powder particle shapes are shown in Figure 5. [Pg.181]

In atomization, a stream of molten metal is stmck with air or water jets. The particles formed are collected, sieved, and aimealed. This is the most common commercial method in use for all powders. Reduction of iron oxides or other compounds in soHd or gaseous media gives sponge iron or hydrogen-reduced mill scale. Decomposition of Hquid or gaseous metal carbonyls (qv) (iron or nickel) yields a fine powder (see Nickel and nickel alloys). Electrolytic deposition from molten salts or solutions either gives powder direcdy, or an adherent mass that has to be mechanically comminuted. [Pg.182]

The standard potential for the anodic reaction is 1.19 V, close to that of 1.228 V for water oxidation. In order to minimize the oxygen production from water oxidation, the cell is operated at a high potential that requires either platinum-coated or lead dioxide anodes. Various mechanisms have been proposed for the formation of perchlorates at the anode, including the discharge of chlorate ion to chlorate radical (87—89), the formation of active oxygen and subsequent formation of perchlorate (90), and the mass-transfer-controUed reaction of chlorate with adsorbed oxygen at the anode (91—93). Sodium dichromate is added to the electrolyte ia platinum anode cells to inhibit the reduction of perchlorates at the cathode. Sodium fluoride is used in the lead dioxide anode cells to improve current efficiency. [Pg.67]

Electrochemical Microsensors. The most successful chemical microsensor in use as of the mid-1990s is the oxygen sensor found in the exhaust system of almost all modem automobiles (see Exhaust control, automotive). It is an electrochemical sensor that uses a soHd electrolyte, often doped Zr02, as an oxygen ion conductor. The sensor exemplifies many of the properties considered desirable for all chemical microsensors. It works in a process-control situation and has very fast (- 100 ms) response time for feedback control. It is relatively inexpensive because it is designed specifically for one task and is mass-produced. It is relatively immune to other chemical species found in exhaust that could act as interferants. It performs in a very hostile environment and is reHable over a long period of time (36). [Pg.392]

Most battery electrodes are porous stmctures in which an interconnected matrix of soHd particles, consisting of both nonconductive and electronically conductive materials, is filled with electrolyte. When the active mass is nonconducting, conductive materials, usually carbon or metallic powders, are added to provide electronic contact to the active mass. The soHds occupy 50% to 70% of the volume of a typical porous battery electrode. Most battery electrode stmctures do not have a well defined planar surface but have a complex surface extending throughout the volume of the porous electrode. MacroscopicaHy, the porous electrode behaves as a homogeneous unit. [Pg.514]

Eor the negative electrolyte, cadmium nitrate solution (density 1.8 g/mL) is used in the procedure described above. Because a small (3 —4 g/L) amount of free nitric acid is desirable in the impregnation solution, the addition of a corrosion inhibitor prevents excessive contamination of the solution with nickel from the sintered mass (see Corrosion and corrosion inhibitorsCorrosion and corrosion control). In most appHcations for sintered nickel electrodes the optimum positive electrode performance is achieved when one-third to one-half of the pore volume is filled with active material. The negative electrode optimum has one-half of its pore volume filled with active material. [Pg.548]


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See also in sourсe #XX -- [ Pg.597 , Pg.604 ]




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