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Region II

Reduction of Adsorbed water Hydrolysis of PC Hoffman eltmlnallQr ofTEMA- [Pg.346]


Estimate the slopes in region II of the isotherms in Fig. XI-13. Derive adsorption laws from these estimates and discuss the differences in the two systems responsible for the different isotherms. [Pg.421]

This Scln-ddinger equation has a particularly simple solution for a finite energy well V(x) = - V for 0 [Pg.101]

Escaped radicals diffiise to region II, where J is negligible, and may undergo. S-Jq mixmg as described previously. From region II, the radicals may follow any of tliree different pathways. [Pg.1596]

The feed compositions and products of each of these strategic separations remain ill-defined. The unspecified 2-propanol—water mixture, the input to each strategic separation, could be but is not necessarily the original feed composition. The MSA composition (pure hexane in this case) is such that one of the products of the strategic separation is in region II, ie, the strategic separation crosses the distillation boundary. Two opportunistic distillations from... [Pg.455]

Mixer 6 undefined mixture in region II B5 = water (target product) M6 = mixture in region III... [Pg.456]

Sulfur oxides resulting from fuel sulfur combustion often inhibit catalyst performance in Regions II, III, and a portion of Region IV (see Fig. 7) depending on the precious metals employed in the catalyst and on the air/fuel ratio. Monolithic catalysts generally recover performance when lower sulfur gasoline is used so the inhibition is temporary. Pd is more susceptible than Rh or Pt. The last is the most resistant. Pd-containing catalysts located in hotter exhaust stream locations, ie, close to the exhaust manifold, function with Httie sulfur inhibition (72—74). [Pg.489]

In Region II, the high- and low-boihng nodes are MIPK and the MEK-water azeotrope, respectively. The more complicated cyclo-hexane-ethanol-water system (Fig. 13-58c) has three separatrices and three regions, all of which share the ternaiy azeotrope as the low-boiling node. [Pg.1296]

Region II, 0.02 < P < 2. Most of the reaction occurs in the bulk of the liquid. Both interfacial area and holdup of liquid should be high. Stirred tanks or bubble columns will be suitable. [Pg.2109]

Electrolytic corrosion occurs in regions I and IV with the formation of soluble iron ions. Solid corrosion products which can have a protective effect are formed in region II. This is the region of surface film passivity. Certain corrosive sub-... [Pg.39]

A non-ideal MSMPR model was developed to account for the gas-liquid mass transfer resistance (Yagi, 1986). The reactor is divided into two regions the level of supersaturation in the gas-liquid interfacial region (region I) is higher than that in the main body of bulk liquid (region II), as shown in Figure 8.12. [Pg.236]

A steady-state population density of crystals in the region II is... [Pg.236]

Note that we do not use any dielectric constant here since all interactions are considered explicitly. UQti is the interaction between the charges in region I and the protein residual charges in region II and is given by... [Pg.125]


See other pages where Region II is mentioned: [Pg.415]    [Pg.102]    [Pg.102]    [Pg.102]    [Pg.1595]    [Pg.1822]    [Pg.79]    [Pg.640]    [Pg.641]    [Pg.202]    [Pg.456]    [Pg.456]    [Pg.456]    [Pg.456]    [Pg.456]    [Pg.456]    [Pg.195]    [Pg.486]    [Pg.487]    [Pg.1302]    [Pg.1302]    [Pg.1312]    [Pg.2041]    [Pg.40]    [Pg.237]    [Pg.352]    [Pg.353]    [Pg.234]    [Pg.216]    [Pg.303]    [Pg.304]    [Pg.403]    [Pg.201]    [Pg.202]    [Pg.591]    [Pg.132]    [Pg.134]    [Pg.54]    [Pg.125]   


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Amide II region

H II region

Region II Ohmic Polarization

Rheology in Region II The Effect of Texture Elasticity

Switch II region

Winsor II Region

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