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Second threshold value

Figure 8 Schematic representation of the processes leading to birefringence (and turbidity) in a W/O microemulsion, in relation to an applied electric square pulse E. Below a (second) threshold value of the field strength and far from critical conditions, or under any conditions if the pulse is terminated at a time indicated by the dashed line, only birefringence is observed due to the formation of AJ, and Above the threshold of the field strength, close to critical conditions, and with a sufficiently long square pulse, turbidity contributes to the signal due to phase separation or/and percolation. The double wall of the particles symbolizes the water/oil interface. Symbols A, surfactant monomer An, microemulsion droplet (An), cluster LCmp, liquid-crystalline microphase or/and percolation structure. Primed symbols stand for polarized structures oriented parallel to E (- ) reversible step with respect to turning the field on or off (->) irreversible step. (Reprinted with permission from Refs. 6 and 41. Copyright 1989 and 1994 American Chemical Society.)... Figure 8 Schematic representation of the processes leading to birefringence (and turbidity) in a W/O microemulsion, in relation to an applied electric square pulse E. Below a (second) threshold value of the field strength and far from critical conditions, or under any conditions if the pulse is terminated at a time indicated by the dashed line, only birefringence is observed due to the formation of AJ, and Above the threshold of the field strength, close to critical conditions, and with a sufficiently long square pulse, turbidity contributes to the signal due to phase separation or/and percolation. The double wall of the particles symbolizes the water/oil interface. Symbols A, surfactant monomer An, microemulsion droplet (An), cluster LCmp, liquid-crystalline microphase or/and percolation structure. Primed symbols stand for polarized structures oriented parallel to E (- ) reversible step with respect to turning the field on or off (->) irreversible step. (Reprinted with permission from Refs. 6 and 41. Copyright 1989 and 1994 American Chemical Society.)...
Onc-Factor-at-a-Timc Optimization One approach to optimizing the quantitative method for vanadium described earlier is to select initial concentrations for ITiOz and 1T2S04 and measure the absorbance. We then increase or decrease the concentration of one reagent in steps, while the second reagent s concentration remains constant, until the absorbance decreases in value. The concentration of the second reagent is then adjusted until a decrease in absorbance is again observed. This process can be stopped after one cycle or repeated until the absorbance reaches a maximum value or exceeds an acceptable threshold value. [Pg.669]

Fatty alcohol- (or alkyl-)ethoxylates, CoE, are considered to be better candidates for LLE based on their ability to induce rapid phase separation for Winsor II and III systems. (Winsor III systems consist of excess aqueous and organic phases, and a middle phase containing bicontinuous microemulsions.) However, C,E,-type surfactants alone cannot extract biomolecules, presumably because they have no net negative charge, in contrast to sorbitan esters [24,26,30,31]. But, when combined with an additional anionic surfactant such as AOT or sodium benzene dodecyl sulfonate (SDBS), or affinity surfactant, extraction readily occurs [30,31]. The second surfactant must be present beyond a minimum threshold value so that its interfacial concentration is sufficiently large to be seen by... [Pg.482]

Inset a) refers to the starting configuration, t=0 fs, with the 5 water molecules in the first hydration shell. Inset b) refers to t=70 fs some rearrangement starts to occur, especially for the left most water molecule. At t=l 10 fs (inset c)) one ion-water distance is above the threshold value, the water starts to leave the first hydration shell. Finally, at t=210 fs, one water molecule is in the second hydration shell and the remaining four... [Pg.201]

The second RPT criterion relates to the temperature of the hot liquid. That is, this temperature must exceed a threshold value before an RPT is possible. From one theory of RPTs, the superheated-liquid model (described later), this criterion arises naturally, and the threshold hot-liquid temperature is then equal to the homogeneous nucleation temperature of the colder liquid T. This temperature is a characteristic value for any pure liquid or liquid mixture and can be measured in independent experiments or estimated from theory. From alternate RPT theories, the threshold temperature may be equated, approximately, to the hot fluid temperature at the onset of stable film boiling. [Pg.107]

After the second layer the time courses of A, (t) are filtrated by the threshold value UiH and gradually settled to a two-state, having the values 0 and 1.0 only, and having a higher signal-to-noise ratio. [Pg.17]

However, although this equation was effective in modelling the odour thresholds of the disubstituted pyrazines, two main weaknesses have been identified (72) the first was that it was difficult to dmw physical meaning from the descriptor AA J, since it was not clear which aspects of die molecular structure determined the odour threshold. The second we ess was discovered when pyrazine itself and thirteen mono-substituted pyrazines were added to the original set. The calculated and observed odour threshold values were no longer in agreement. This result indicated diat the model was insufficient for more heterogeneous data sets. [Pg.102]

Of the few known terpene compounds that contain heteroatoms such as nitrogen or sulfur, the thiol 8-mercapto-p-menthan-3-one described below has qualitatively important applications as a fragrance and flavor substance. The second thiol, -p-menthene-8-thiol, is described because its odor threshold value is far lower than that of most other fragrance and flavor materials. [Pg.74]

Table VI-5 shows that the dissociation process, N02 - NO + O( D) takes place energetically below 2439 A. Usclman and Lee (985) have measured the production of O( >) as a function of incident wavelength near 2439 A. They have found that the contribution of rotational energy to dissociation is insignificant near the second threshold in contrast to the case near the first threshold at 3980 A where the contribution of rotational energy is substantial. They attribute the lack of rotational contribution to the presence of large rotational barriers at high J values in the excited state (987). The quantum yield of O( D) production increases to a plateau of about 0.5 0.1 towards shorter wavelengths, indicating that at least two processes, (VI-59) and (V1-60). occur concurrently below the second threshold wavelength. Table VI-5 shows that the dissociation process, N02 - NO + O( D) takes place energetically below 2439 A. Usclman and Lee (985) have measured the production of O( >) as a function of incident wavelength near 2439 A. They have found that the contribution of rotational energy to dissociation is insignificant near the second threshold in contrast to the case near the first threshold at 3980 A where the contribution of rotational energy is substantial. They attribute the lack of rotational contribution to the presence of large rotational barriers at high J values in the excited state (987). The quantum yield of O( D) production increases to a plateau of about 0.5 0.1 towards shorter wavelengths, indicating that at least two processes, (VI-59) and (V1-60). occur concurrently below the second threshold wavelength.

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See also in sourсe #XX -- [ Pg.2 , Pg.515 ]




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Second values

THRESHOLD VALUE

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