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Viscosity modifiers, analysis

Applications Over the last 20 years, ICP-AES has become a widely used elemental analysis tool in many laboratories, which is also used to identify/quantify emulsifiers, contaminants, catalyst residues and other inorganic additives. Although ICP-AES is an accepted method for elemental analysis of lubricating oils (ASTM D 4951), often, unreliable results with errors of up to 20% were observed. It was found that viscosity modifier (VM) polymers interfere with aerosol formation, a critical step in the ICP analysis, thus affecting the sample delivery to the plasma torch [193]. Modifications... [Pg.622]

Thus, with this modified analysis the circulation contribution is proportional to E, in agreement with the Bueche, De Gennes and Graessley results. However, now a power of molecular weight is lost in the viscosity,... [Pg.87]

The shear stresses and the shear rates in Fig. 8 were computed by the appropriate formula for Newtonian flow at the capillary wall. But if the results of such a computation indicate that the viscosity varies with shear rate, then the Rabinowitsch analysis is applied to determine the correct shear rate at the wall for non-Newtonian behavior (c. References 2 and 3). Figure 4-9 illustrates how the addition of a polymeric viscosity modifier to a paraffinic petroleum base oil changes the viscosity behavior from Newtonian (Fluid B) to non-Newtonian (Fluids C, D and E). The shear rates and the shear stresses have a hundred-fold range. [Pg.71]

Bansal, J. G. and McElroy, F. C., Accurate Elemental Analysis of Multigrade Lubricating Oils by ICP Method, Effect of Viscosity Modifiers, SAE Technical paper 932694,1993. [Pg.41]

ADDITIVE ANALYSIS (MOLD-RELEASE, ANTISTAT, IMPACT AND VISCOSITY MODIFIERS)... [Pg.200]

If the preceding analysis of hydrodynamic effects of the polymer molecule is valid, K should be a constant independent both of the polymer molecular weight and of the solvent. It may, however, vary somewhat with the temperature inasmuch as the unperturbed molecular extension rl/M may change with temperature, for it will be recalled that rl is modified by hindrances to free rotation the effects of which will, in general, be temperature-dependent. Equations (26), (27), and (10) will be shown to suffice for the general treatment of intrinsic viscosities. [Pg.612]

Runnels and Eyman [41] report a tribological analysis of CMP in which a fluid-flow-induced stress distribution across the entire wafer surface is examined. Fundamentally, the model seeks to determine if hydroplaning of the wafer occurs by consideration of the fluid film between wafer and pad, in this case on a wafer scale. The thickness of the (slurry) fluid film is a key parameter, and depends on wafer curvature, slurry viscosity, and rotation speed. The traditional Preston equation R = KPV, where R is removal rate, P is pressure, and V is relative velocity, is modified to R = k ar, where a and T are the magnitudes of normal and shear stress, respectively. Fluid mechanic calculations are undertaken to determine contributions to these stresses based on how the slurry flows macroscopically, and how pressure is distributed across the entire wafer. Navier-Stokes equations for incompressible Newtonian flow (constant viscosity) are solved on a three-dimensional mesh ... [Pg.96]

When a thermal treatment was applied to starch before the analysis, a very different behavior (Fig. 23b) was obtained. After such a treatment, no maximum was observed for the viscosity which increased slowly up to 82°C. In the case of starch modified with octadienyl chains (DS 0.055 (Fig. 23c) and DS 0.1 (Fig. 23d)), the viscosities were much lower than for native starch (b) in both cases. The presence of hydrophobic chains at the surface of the material could prevent the interaction of water molecules with the macromolecules after the splitting, thus avoiding the formation of a gel. [Pg.117]

In the in situ consolidation model of Liu [26], the Lee-Springer intimate contact model was modified to account for the effects of shear rate-dependent viscosity of the non-Newtonian matrix resin and included a contact model to estimate the size of the contact area between the roller and the composite. The authors also considered lateral expansion of the composite tow, which can lead to gaps and/or laps between adjacent tows. For constant temperature and loading conditions, their analysis can be integrated exactly to give the expression developed by Wang and Gutowski [27]. In fact, the expression for lateral expansion was used to fit tow compression data to determine the temperature dependent non-Newtonian viscosity and the power law exponent of the fiber-matrix mixture. [Pg.215]

The phosphoric acid esters of diacyl glycerides, phospholipids, are important constituents of cellular membranes. Lecithins (phosphatidyl cholines) from egg white or soybeans are often added to foods as emulsifying agents or to modify flow characteristics and viscosity. Phospholipids have very low vapor pressures and decompose at elevated temperatures. The strategy for analysis involves preliminary isolation of the class, for example by TLC, followed by enzymatic hydrolysis, derivatization of the hydrolysis products, and then GC of the volatile derivatives. A number of phospholipases are known which are highly specific for particular positions on phospholipids. Phospholipase A2, usually isolated from snake venom, selectively hydrolyzes the 2-acyl ester linkage. The positions of attack for phospholipases A, C, and D are summarized on Figure 9.7 (24). Appropriate use of phospholipases followed by GC can thus be used to determine the composition of phospholipids. [Pg.464]

Figure 7.11 shows modified Crawford-Wilke [11] correlation plot curves. Note that the y-axis is a type of Reynolds number, as discussed in Chap. 6. This y-axis number is similar to the Reynolds number, having density (Dc), viscosity (Uc), and velocity (Vc and Vd). If you review Chap. 6 and the Reynolds number, the same dimensional analysis is seen in the order given in Fig. 7.11 on the y-axis. The x-axis relates to viscosity (Uc), surface tension (0 ), density (Dc), and packing size factor (FJ. Originally the square root of the x-ordinate was used in the Crawford-Wilke correlation plotted against such a Reynolds number. Also, only one curve was made in this original work, the top curve labeled Crawford-Wilke in Fig. 7.11. This top curve represents the point at which the continuous phase is saturated with solute, in equilibrium condition. Eckert [9] reported that when Vc is increased, beginning at Vc = 0, the system floods before Vc reaches this saturation Crawford-Wilke curve. Figure 7.11 shows modified Crawford-Wilke [11] correlation plot curves. Note that the y-axis is a type of Reynolds number, as discussed in Chap. 6. This y-axis number is similar to the Reynolds number, having density (Dc), viscosity (Uc), and velocity (Vc and Vd). If you review Chap. 6 and the Reynolds number, the same dimensional analysis is seen in the order given in Fig. 7.11 on the y-axis. The x-axis relates to viscosity (Uc), surface tension (0 ), density (Dc), and packing size factor (FJ. Originally the square root of the x-ordinate was used in the Crawford-Wilke correlation plotted against such a Reynolds number. Also, only one curve was made in this original work, the top curve labeled Crawford-Wilke in Fig. 7.11. This top curve represents the point at which the continuous phase is saturated with solute, in equilibrium condition. Eckert [9] reported that when Vc is increased, beginning at Vc = 0, the system floods before Vc reaches this saturation Crawford-Wilke curve.
Capillary zone electrophoresis (CZE) is the most simple and widely used mode in CE. Separations take place in an open-tube, fused silica capillary under the influence of an electric field. The velocity of the analytes is modified by controlling the pH, viscosity, or concentration of the buffer, or by changing the separation voltage. The electroosmotic flow is often used in this mode to improve resolution or to shorten analysis times. [Pg.155]

The earliest general model of adaptation to temperature in membrane lipids focused on the physical state ( static order or viscosity [= 1 / fluidity ]) of the bilayer. The finding that the physical state of membrane lipids from Escherichia coli cultured at different temperatures was similar at the different growth temperatures led to the homeoviscous adaptation hypothesis, which states that lipid composition is modified during thermal acclimation to facilitate retention of a relatively stable membrane physical state (Sinensky, 1974). At the outset of any discussion of homeoviscous adaptation, it is important to examine carefully what is meant by physical state (or the related terms static order, viscosity, and fluidity ). In such an analysis, one must also consider the physical methods that are used to make such measurements—and the limitations of these techniques. [Pg.359]

According to the element analysis results, the determination of modified oligomer relative viscosities, to the spectra data and references [7], the scheme of interaction of oligoisobutylene-alkylated phenols with element sulfur in our case can be written in the following way ... [Pg.58]


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Viscosity analysis

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