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Force-temperature curves effect

On the other hand, despite the information about long chain sulfates, sulfonates, phosphates, and carboxylates that indicates stronger interaction with Ca2+ than with Mg2+ (i.e., in apparent harmony with the sequence of the Hofmeister (44) series), several difficulties remain. For example, while Miyamoto s data for DS (10) indicate the interaction sequence Mg < Ca < Sr < Ba from solubility measurements (as well as from temperature/CMC measurements if one accepts the Mg—Ca sequence of the present paper), this sequence, with the exception of the position of Mg and Ca, is the opposite of that found by Deamer et al. (33) from condensation effects on the force/area curves of ionized fatty acids. At the same time, the ion sequence obtained by these authors from phase transition temperatures of spread fatty acids (33) differs from that deduced from the above-mentioned condensation effects, and the latter depended strongly on pH. Lastly, definite differences in ion sequence effects exist for the alkaline earth metals in their interaction with long... [Pg.89]

Figure 3 shows the lateral force versus temperature curves for the PS films with M of 4.9X10 (4.9k) and 140k at a fixed scanning rate (v) of 1 pm s [26]. The thickness of the films was approximately 200 nm, which was sufficient to avoid the thinning effect on Tg [27]. The ordinate is normalized by the peak value of lateral... [Pg.6]

Fig. 6.6. Calculated time-temperature heating curves for a rotary hearth donut furnace showing the effects of delays before addition of enhanced heating burners. (Directions for calculating time-temperature curves are given in chap. 8.) The top two curves show what happens upon restart at normal tph after a delay. The bottom curve shows that loads charged after resumption will be too cold to roll, forcing a fall back to half the normal tph. Fig. 6.6. Calculated time-temperature heating curves for a rotary hearth donut furnace showing the effects of delays before addition of enhanced heating burners. (Directions for calculating time-temperature curves are given in chap. 8.) The top two curves show what happens upon restart at normal tph after a delay. The bottom curve shows that loads charged after resumption will be too cold to roll, forcing a fall back to half the normal tph.
As the Dehmelt force actually varies across the gap (decreasing toward the external electrode), it affects not only the location of the bottom of pseudopotential due to ion drift nonlinearity (which determines c). but also its profile that controls ion focusing properties and thus the peak shape and height (4.3.1). This matter remains to be explored, as well as the effect in planar gaps with uneven temperature across (4.3.9). Overall, the issue of Dehmelt force in curved gaps should become topical with ongoing efforts to reduce FAIMS pressure (4.2.6). [Pg.249]

Forced-vibration instruments drive specimens at specific frequencies and determine the response, usually over a range of temperatures. Storage and loss moduli or related parameters are determined. Series of modulus-temperature curves can be generated by making measurements at several different fi equencies. Because thermal and mechanical transitions are functions of frequency as well as temperature, data from such curves can be used to calculate activation energies of transitions. In addition, frequencies can be chosen to represent or approximate polymer processing effects and use conditions. [Pg.7122]

The results of textural evaluations of banana chips prepared under different conditions are listed in Tab. 3.5. These results are expressed in terms of the maximum force in a force-deformation curve, which is a representative of the hardness of the samples. The results are also expressed in terms of the number of peaks in the force-deformation curve, which is a representative of the crispness of the samples. It can be seen that chips prepared by VACUUM-FIR were harder than those prepared by LPSSD-FIR. The difference was due to variations in the microstructure of the chips, as illustrated in Fig. 3.19. The drying temperature and pressure nevertheless had no significant effect on the hardness of the chips. In terms of crispness, LPSSD-FIR resulted in chips with higher numbers of peaks (and hence were crispier) than did VACUUM-FIR, especially when drying was conducted at a lower temperature, such as 80 °C. This was again due to the more extensive porous structure of the chips produced by LPSSD-FIR. [Pg.114]

It is seen that all the points lie on the same straight line, irrespective of the operating temperature and, thus, the enthalpy term is close to zero and the solutes are not retained by differential molecular forces. Thus, the curve shows the effect of... [Pg.43]

A rod of polypropylene, 10 mm in diameter, is clamped between two rigid fixed supports so that there is no stress in the rod at 20°C. If the assembly is then heated quickly to 60°C estimate the initial force on the supports and the force after 1 year. The tensile creep curves should be used and the effect of temperature may be allowed for by making a 56% shift in the creep curves at short times and a 40% shift at long times. The coefficient of thermal expansion for polypropylene is 1.35 x 10 °C in this temperature range. [Pg.160]

From this relatively simple test, therefore, it is possible to obtain complete flow data on the material as shown in Fig. 5.3. Note that shear rates similar to those experienced in processing equipment can be achieved. Variations in melt temperature and hypostatic pressure also have an effect on the shear and tensile viscosities of the melt. An increase in temperature causes a decrease in viscosity and an increase in hydrostatic pressure causes an increase in viscosity. Topically, for low density polyethlyene an increase in temperature of 40°C causes a vertical shift of the viscosity curve by a factor of about 3. Since the plastic will be subjected to a temperature rise when it is forced through the die, it is usually worthwhile to check (by means of Equation 5.64) whether or not this is signiflcant. Fig. 5.2 shows the effect of temperature on the viscosity of polypropylene. [Pg.373]

It should be recognized that tensile properties would most likely vary with a change of speed of the pulling jaws and with variation in the atmospheric conditions. Figure 2-14 shows the variation in a stress-strain curve when the speed of testing is altered also shown are the effects of temperature changes on the stress-strain curves. When the speed of pulling force is increased, the material reacts like brittle material when the temperature is increased, the material reacts like ductile material. [Pg.309]

In order to establish master curves of friction or side force coefficients, the speed range has to be low in order to avoid significant temperature rises in the contact area and, if the experiments are carried out on wet tracks, also lubrication effects. [Pg.698]

Figure 2. A schematic of the free energy density of an aperiodic lattice as a function of the effective Einstein oscillator force constant a (a is also an inverse square of the locahzation length used as input in the density functional of the liquid). Specifically, the curves shown characterize the system near the dynamical transition at Ta, when a secondary, metastable minimum in F a) begins to appear as the temperature is lowered. Taken from Ref. [47] with permission. Figure 2. A schematic of the free energy density of an aperiodic lattice as a function of the effective Einstein oscillator force constant a (a is also an inverse square of the locahzation length used as input in the density functional of the liquid). Specifically, the curves shown characterize the system near the dynamical transition at Ta, when a secondary, metastable minimum in F a) begins to appear as the temperature is lowered. Taken from Ref. [47] with permission.
The amount of heat actually taken up by the particles was an important quantity, as tubes operate under heat transfer limited conditions near the tube inlet. Fig. 30 shows a plot of Q against r, where Q was the total energy flow into the solid particles, for the entire segment. For inlet conditions, Q varied strongly at lower r, but was almost constant at higher values. As rcut/rp decreased from 0.95 to 0.0 and the effectiveness factor increased from nearly zero to one, the active solid volume increased by a factor of 7. If the solid temperature had remained the same, the heat sink would also have had to increase sevenfold. This could not be sustained by the heat transfer rate to the particles, so the particle temperature had to decrease. This reduced the heat sink and increased the driving force for heat transfer until a balance was found, which is represented by the curve for the inlet in Fig. 30. [Pg.376]


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See also in sourсe #XX -- [ Pg.105 , Pg.106 , Pg.107 ]




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