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Viscosity drift

The phosphite esters function in this formulation as primary heat stabilizers by replacing labile chlorides on PVC via the Arbuzov rearrangement mechanism. When phosphites are used at optimized levels in combination with catalytic amounts of zinc and normal levels of epoxidized soybean oil, they provide excellent early color and adequate long-term stability to flexible PVC compounds. Their use also helps in lowering stabilization cost, elimination of toxic metals, elimination of plate out, poor printability, viscosity drift in plastisols, haze, bloom, water blush, and staining. [Pg.110]

Their use also helps in lowering stabilization cost, elimination of toxic metals, elimination of plateout, poor printability, viscosity drift in plastisols, haze, bloom, water blush, and staining. [Pg.295]

SER Continuous Advancement Process. The recent literature review indicates efforts to develop continuous advancement processes to produce SERs. Companies seek to improve process efficiencies and product quality. One of the major deficiencies of the traditional batch advancement process is the long reaction time, resulting in EEW and viscosity drift, variable product quality, and gel formation. In addition, it is difficult to batch process higher MW, higher viscosity SERs such as types 9 and 10 resins. Shell patented several versions of the... [Pg.2672]

TROYSAN CMP is an organo-metal1ic water soluble liquid. It is especially useful in aqueous systems where viscosity drift from spoilage is a problem. [Pg.244]

Some concerns directly related to a tomizer operation include inadequate mixing of Hquid and gas, incomplete droplet evaporation, hydrodynamic instabiHty, formation of nonuniform sprays, uneven deposition of Hquid particles on soHd surfaces, and drifting of small droplets. Other possible problems include difficulty in achieving ignition, poor combustion efficiency, and incorrect rates of evaporation, chemical reaction, solidification, or deposition. Atomizers must also provide the desired spray angle and pattern, penetration, concentration, and particle size distribution. In certain appHcations, they must handle high viscosity or non-Newtonian fluids, or provide extremely fine sprays for rapid cooling. [Pg.334]

This equation shows that for a given collection efficiency, the precipitator size is inversely proportional to particle drift velocity and directly proportional to gas flow rate. Increasing the gas density (migration velocity is a function of gas viscosity) by reducing its temperature or increasing the pressure will reduce the precipitator size. However, theory does not account for gas velocity. This is a variable that influences particle re-entrainment and the drift velocity. This typically requires an ESP design at lower velocities than predicted in theory. [Pg.363]

Since AAS is a ratio method, many instrumental errors (e.g. long-term source drift, small monochromator drifts) should cancel out, as 7 is ratioed to I . However, a stable uptake rate, or aspiration rate, is required. This falls as the viscosity of the solution sprayed is increased. Nebulizer uptake interferences can be minimized if the dissolved salts content of samples and standards is approximately matched. For example, when determining pg cm sodium levels in 2 M phosphoric acid, ensure that the standards are also dissolved in 2 M phosphoric acid, using a blank to check for contamination. [Pg.42]

Up to now, only hydrodynamic repulsion effects (Chap. 8, Sect. 2.5) have caused the diffusion coefficient to be position-dependent. Of course, the diffusion coefficient is dependent on viscosity and temperature [Stokes—Einstein relationship, eqn. (38)] but viscosity and temperature are constant during the duration of most experiments. There have been several studies which have shown that the drift mobility of solvated electrons in alkanes is not constant. On the contrary, as the electric field increases, the solvated electron drift velocity either increases super-linearly (for cases where the mobility is small, < 10 4 m2 V-1 s-1) or sub-linearly (for cases where the mobility is larger than 10 3 m2 V 1 s 1) as shown in Fig. 28. Consequently, the mobility of the solvated electron either increases or decreases, respectively, as the electric field is increased [341— 348]. [Pg.160]

The flow sensitivity indicates that while a detector may be accurately balanced in terms of resistance and voltage, the reference flow only reduces the flow sensitivity of the analytical column flow by a factor of three to four. Much of the drift due to flow changes comes from the flow controllers. One type commonly used today has been found to have a mass flowrate proportional to absolute temperature. Flow induced noise, however, can come from column temperature fluctuations. Even if the front of the column is fed from a perfect flow source, a temperature change in the column will lead to a viscosity change in the carrier gas. Since the gas is compressible, a transient flow change occurs in the detector. Needless to say, a fluctuation in column temperature also leads to a fluctuation in the bleed level, which affects the recorder baseline by a much more direct process. [Pg.240]

The solution of the equation (4.2.26) cannot be found in an analytical form and thus some approximations have to be used, e.g., variational principle. Its formalism is described in detail [33, 57, 58] for both lower bound estimates and upper bound estimates. Note here only that there are two extreme cases when a(r)/D term is small compared to the drift term, reaction is controlled by defect interaction, in the opposite case it is controlled by tunnelling recombination. The first case takes place, e.g., at high temperatures (or small solution viscosities if solvated electron is considered). [Pg.199]

An internal standard is needed to compensate for differences in physical properties (such as viscosity) between the calibration standard and the test samples and drift caused by thermal changes in the laboratory that will affect the instrument optics. An appropriate internal standard element should not be naturally present in the test samples in appreciable concentrations and should not present spectral interferences with any analyte. In addition, the internal standard should be a strong emitter so that its relative concentration can be kept low, and be as chemically similar to the analyte as possible. [Pg.106]

Even if pinched injection was used, baseline drift of repetitive pinched injections was noted. This was attributed to the meniscus surface tension (Laplace pressure) effect, even though other possible effects (evaporation, buffer depletion due to electrolysis, siphoning, Joule-heat-induced viscosity change) are minimized [553]. [Pg.108]

Some of the test methods being used to measure the processing stability of polypropylene include melt flow drift measurements at elevated temperatures using an extrusion plastometer (melt indexer), melt viscosity retention measurements using a torque rheometer, retention of melt flow after repeated extrusions, and injection molded spiral test measured by the flow in inches at various temperatures and the retention of melt flow of the injected spirals. The nine commercial resins were evaluated by these methods. [Pg.248]

The relation between the mobility of the ion and the properties of the resin can be qualitatively examined with the aid of Stoke s law for the drift of a spherical object in a viscous medium (see, for example, Ref.27)). The mobility of a sphere of radius r, embedded in a medium of viscosity p and subjected to a force is... [Pg.16]

One of the most difficult problems when characterizing copolymers and polymer blends by SEC-viscometry is the accurate determination of the polymer concentration across the SEC elution curve. The concentration detector signal is a function of the chemical drift of the sample under investigation. To overcome this problem, Goldwasser proposed a method where no concentration detector is required for obtaining Mn data [72]. In the usual SEC-viscometry experiment, the determination of the intrinsic viscosity at each slice of the elution curve requires a viscosity and a concentration signal ... [Pg.20]

The evaporative light scattering detector (ELSD) [47] is based on the ability of fine particulate matter of a solute to scatter light. To obtain suitable analyte particles, the column effluent is nebulized by an inert gas in the nebulizer and aerosol droplets are allowed to evaporate in the drift tube. Droplet size is related to mobile phase properties (surface tension, density, and viscosity). Usually, high solvent-to-gas flow ratio provides the best sensitivity because it produces the largest droplet diameters. [Pg.145]


See other pages where Viscosity drift is mentioned: [Pg.400]    [Pg.180]    [Pg.432]    [Pg.37]    [Pg.236]    [Pg.181]    [Pg.80]    [Pg.638]    [Pg.655]    [Pg.658]    [Pg.43]    [Pg.235]    [Pg.293]    [Pg.425]    [Pg.54]    [Pg.86]    [Pg.180]    [Pg.189]    [Pg.169]    [Pg.38]    [Pg.31]    [Pg.109]    [Pg.278]    [Pg.158]    [Pg.165]    [Pg.27]    [Pg.571]    [Pg.20]    [Pg.238]    [Pg.400]   
See also in sourсe #XX -- [ Pg.295 ]




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