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Limiting conductances

At 40 mg/kg FW hardness, the upper conductivity limit should be further reduced to 4,000 p,S/cm. [Pg.585]

Some efforts have been undertaken to study propellant dilatation in multiaxial stress fields and even in small motor configurations. Farris (25) has conducted limited investigations along this line and has made approximate correlations between uniaxial and multiaxial tests. [Pg.210]

For boilers with operating pressures Over 1000 psi (68 atm) cation conductivity of the condensate should normally run between 0.2 and 0.5 micromhos. A reading above this limit indicates the presence of condenser leakage or contamination from some other source. The source of the contamination should be investigated and remedied at the first opportunity. However, when a cation conductivity limit of 1.0 is readied, the internal water treatment and blowdown must be changed appropriately. [Pg.1745]

Conductance Limit Orifice in a metal plate separating the two... [Pg.193]

Foods. The FDA has conducted limited analyses for the higher chlorinated CDDs (HxCDD, HpCDD, and OCDD) in market-basket samples collected from 1979 to 1984 under the FDA s Total Diet Program (Firestone et al. 1986). Food samples found to contain PCP residues >0.05 g/g (ppm) were analyzed for... [Pg.472]

Three dimensional electrode structures are used in several applications, where high current densities are required at relatively low electrode and cell polarisations, e g. water electrolysis and fuel cells. In these applications it is desirable to fully utilize all of the available electrode area in supporting high current densities at low polarisation. However conductivity limitations of three-dimensional electrodes generally cause current and overpotential to be non-uniform in the structure. In addition the reaction rate distribution may also be non-uniform due to the influence of mass transfer.1... [Pg.221]

Figure 13 shows the potential and concentration distributions for different values of dimensionless potential under conditions when internal pore diffusion (s = 0.1) and local mass transport (y = 10) are a factor. As expected the concentration and relative overpotential decrease further away from the free electrolyte (or membrane) due to the combined effect of diffusion mass transport and the poor penetration of current into the electrode due to ionic conductivity limitations. The major difference in the data is with respect to the variation in reactant concentrations. In the case when an internal mass transport resistance occurs (y = 10) the fall in concentration, at a fixed value of electrode overpotential, is not as great as the case when no internal mass transport resistance occurs. This is due to the resistance causing a reduction in the consumption of reactant locally, and thereby increasing available reactant concentration the effect of which is more significant at higher electrode overpotentials. [Pg.267]

Keith Scott and Yan-Ping Sun review and discuss three dimensional electrode structures and mathematical models of three dimensional electrode structures in chapter four. Conductivity limitations of these three-dimensional electrodes can cause the current overpotential to be non-uniform in structure. Adomian s Decomposition Method is used to solve model equations and approximate analytical models are obtained. The first three to seven terms of the series in terms of the nonlinearities of the model are generally sufficient to meet the accuracy required in engineering applications. [Pg.315]

It will be seen from Fig. 10.29 that for small Raw, when the convective motion is weak, the Nusselt number tends to the conduction limit value of 1. However, when Raw is large, the flow will consist mainly of a boundary layer flow up the hot wall and a boundary layer flow down the cold wall. It is to be expected, therefore, that in... [Pg.537]

Time Limits Unless otherwise specified, allow 5 min for a reaction to take place when conducting limit tests for trace impurities such as chloride or iron. [Pg.6]

Poor thermal conductivity limits sliding speed. [Pg.315]

Heating. II Conduction Limit. Combust, Sci. Technol, in press. [Pg.52]


See other pages where Limiting conductances is mentioned: [Pg.585]    [Pg.471]    [Pg.427]    [Pg.1648]    [Pg.311]    [Pg.161]    [Pg.216]    [Pg.129]    [Pg.1694]    [Pg.8]    [Pg.502]    [Pg.1663]    [Pg.293]    [Pg.10]    [Pg.73]    [Pg.121]    [Pg.177]    [Pg.299]    [Pg.358]    [Pg.582]    [Pg.228]    [Pg.266]    [Pg.226]    [Pg.531]    [Pg.28]    [Pg.425]    [Pg.425]    [Pg.425]    [Pg.425]    [Pg.339]   
See also in sourсe #XX -- [ Pg.216 , Pg.225 ]




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Additivity of Electrolyte Limiting Conductivity

Conduction limited, boiling

Conduction-controlled limiting case

Conductivity limiting, molar

Conventional polymer electrolytes conductivity limit

Electrical conductivity limiting

Equivalent ionic conductances, limiting

Formic Acid limiting conductances

Growth Limited by Heat Conduction and Mass Diffusion Simultaneously

Heat Conduction-Limited Growth

Ionic molar conductivity, limiting

Kohlrauschs Law and Limiting Conductivity

Limiting conductance of lanthanum trichloride

Limiting conductance of univalent chlorides

Limiting equivalent conductances

Limiting equivalent conductivities

Limiting gas conductance

Limiting ionic conductivities

Limiting molar conductance

Limits of Conducted EMI

Methanol— 568 limiting conductances

OLEDs injection-limited conduction

OLEDs transport-limited conduction

Organic ions, limiting equivalent conductances

Polymers, electronically conducting organic limitations

Proton limiting conductances

Solvate ions limiting conductances

Space-charge-limited conductivity

The Conducted Emission Limits

The limiting molar conductivity

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