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Suspensions particles

The great variety of inspection applications required the QAP system to perform relative measurements in judgeing certain conditions and not to restrict the user to dictated inspection conditions. One important example for MPI is for example the decision whether the magnetic particle suspension can be used or has to be changed. [Pg.629]

The condition of the magnetic particle suspension is controlled by an automated ASTM-bulb. The bulb is connected to the currently used Magentic particle suspension tank by a bypass, so the suspension in use is flowing through the bulb too. In user defined periods a valve is closed and the Magentic particle suspension remained into the bulb is analysed. The automatic bulb has the ability to measure the extinction and transmission of the suspension related to the time (Figure 1, Figure 2)... [Pg.629]

The system compares its own values for good and a bad magnetic particle suspensions with the actually measured values. The system values are stored in the form of reference curves for a fresh MP-suspension used on the machine and the used MP-suspension which has to be changed. [Pg.629]

PHASE CONTACTING AND LIQUID-SOLID PROCESSING AGITATION OF LOW-VISCOSITY PARTICLE SUSPENSIONS... [Pg.1620]

Impeller Reynolds number and equations for mixing power for particle suspensions are in Sec. 5. Dispersion of gasses into liquids is in Sec. 14. Usually, an increase in mechanical agitation is more effective than is an increase in aeration rate for improving mass transfer. [Pg.2140]

Fumed silicas (Si02). Fumed silicas are common fillers in polychloroprene [40], natural rubber and styrene-butadiene rubber base adhesives. Fumed silicas are widely used as filler in several polymeric systems to which it confers thixotropy, sag resistance, particle suspension, reinforcement, gloss reduction and flow enhancement. Fumed silica is obtained by gas reaction between metallic silicon and dry HCl to rend silica tetrachloride (SiCU). SiC is mixed with hydrogen and air in a burner (1800°C) where fumed silica is formed ... [Pg.633]

In selecting cloths made from synthetic materials, one must account for the fact that staple cloths provide a good retentivity of solid particles due to the short hairs on their surface. However, cake removal is often difficult from these cloths - more than from cloths of polyfilament and, especially, monofilament fibers. The type of fiber weave and pore size determine the degree of retentivity and permeability. The objective of the process, and the properties of particles, suspension and cake should be accounted for. The cloth selected in this maimer should be confirmed or corrected by laboratory tests. Such tests can be performed on a single filter. These tests, however, provide no information on progressive pore plugging and cloth wear. However, they do provide indications of expected filtrate pureness, capacity and final cake wetness. [Pg.151]

Fluid mixing and particle suspension in unbaffled vessels (Figure 7.1(a)) may be poor, experiencing vortexing but this can be improved by the addition of wall... [Pg.191]

The effect on the process of a change in operation of the mixer system (impeller, baffles, etc.) is the final measurement of performance. Thus, operations such as blending, uniform particle suspension, reaction, gas absorption, etc., may be acceptable under one physical system and not so to the same degree under a slightly modified one. The ratio per unit volume on scale-up must be determined experimentally. [Pg.323]

Hence, for two similarly charged surfaces in electrolyte, interactions are determined by both electrostatic doublelayer and van der Waals forces. The consequent phenomena have been described quantitatively by the DLVO theory [6], named after Derjaguin and Landau, and Verwey and Over-beek. The interaction energy, due to combined actions of double-layer and van der Waals forces are schematically given in Fig. 3 as a function of distance D, from which one can see that the interplay of double-layer and van der Waals forces may affect the stability of a particle suspension system. [Pg.168]

The apparatus employed for chromatographing particle suspensions in this laboratory has been reported in detail elsewhere (ll). A sample loop of approximately O.U ml was used. The detector was a Pharmacia UV-spectrophotometer with a cell of 1 cm path length and an operating wavelength of either 25, 280 or 350 nm. The volume counter had a capacity of 1 ml. [Pg.48]

Heller and Tabibian (13) noted that errors, due to laterally scattered light and the corona effect, as large as to cause a 30 reduction in measured turbidity, may result if instruments which are perfectly suitable for ordinary absorption measurements are used for turbidity measurements without proper modifications. To evaluate the performance of our turbidity detector, particle suspensions of various concentrations of several polystyrene latex standards were prepared. Their extinction coefficients were measured using both a bench-top UV spectrophotometer (Beckman, Model 25) and the online detector (Pharmacia). [Pg.52]

To measure k using the online detector, the packed columns were replaced by a length of l/l6 in OD ss tubing and peak areas corresponding to injections of various particle suspensions and sodium dichromate solutions were recorded on chart paper. The following analysis was then applied. [Pg.56]

The particle size analysis techniques outlined earlier show promise in the measurement of polydispersed particle suspensions. The asumption of Gaussian instrumental spreading function is valid except when the chromatograms of standard latices are appreciably skewed. Calc ll.ation of diameter averages indicate a fair degree of insensitivity to the value of the extinction coefficient. [Pg.74]

Recently it has been reported that even colloidal particle suspensions themselves, without added polymers, can form dissipative structures. Periodic stripes of colloidal particles (monodisperse particles of diameter 30 nm and 100 nm, respectively) and polystyrene particles (monodisperse diameters from 0.5 to 3 pm) can be formed from dilute aqueous suspensions. The stripes are parallel to the receding direction of the edge of the suspension droplet and thus indicate that a fingering instability... [Pg.193]

Reticulated Bacterial Cellulose. A cellulose with an intertwined reticulated structure, produced from bacteria, has unique properties and functionalities unlike other conventional celluloses. When added to aqueous systems, reticulated bacterial cellulose improves the fluid rheology and the particle suspension over a wide range of conditions [1836]. Test results showed advantages in fluid performance and significant economic benefits by the addition of reticulated bacterial cellulose. [Pg.243]

Schiirenberg, M., Dreisewerd, K., and Hillenkamp, F., Laser desorption/ion-ization mass spectrometry of peptides and proteins with particle suspension matrixes, Anal. Chem., 71, 221, 1999. [Pg.67]

This expression shows the difference of sonic velocity c in a particle suspension from that in the air, co as a function of the mass fraction of suspension, Xs, the relaxation times, jd and t and the frequency, w. These equations show that the acoustic velocity in a droplet suspension is a strong function of frequency and... [Pg.268]

Significance. What is the significance of these observations For succinoglycan solutions the answer is obvious, above the transition temperature they have little or no viscosity, which may be undesirable. Such polymers are usually used as viscosifiers or for particle suspension. On the other hand, a drop in viscosity may be an advantage if fluid penetrates a formation hotter than the well as there could be little or no subsequent formation damage. [Pg.168]

Transition from liquid behavior to solid behavior has been reported with fine particle suspensions with increased filler content in both Newtonian and non-Newtonian liquids. Industrially important classes are rubber-modified polymer melts (small rubber particles embedded in a polymer melt), e.g. ABS (acrylo-nitrile-butadiene-styrene) or HIPS (high-impact polystyrene) and fiber-reinforced polymers. Another interesting suspension is present in plasticized polyvinylchloride (PVC) at low temperatures, when suspended PVC particles are formed in the melt [96], The transition becomes evident in the following... [Pg.206]

Mix 50 pi of fine gold particle suspension successively with donor/acceptor plasmid DNA (up to 10 pg in total), 50 pi of 2.5 M CaCl2, and 20 pi of 0.1 M Spermidine while vortexing. [Pg.443]

M. Schiirenberg, K. Dreisewerd, and F. Hillenkamp, Laser Desorption/Ionization Mass Spectrometry of Peptides and Proteins with Particle Suspension Matrices, Anal. Chem., 71, 221 229(1999). [Pg.160]

Add 20 pi of the carboxyethylsilanetriol (as the 25 percent aqueous solution) to the particle suspension with mixing. [Pg.574]

Combine the ligand solution with the particle suspension and mix thoroughly. [Pg.598]

Add 100 mg EDC and mix to dissolve. To facilitate faster dissolution, EDC may be dissolved immediately before use as a concentrated stock solution in reaction buffer and then an aliquot of this solution added to the particle suspension to obtain the correct final concentration. [Pg.598]

Add the protein to be coupled to the particle suspension in an amount equal to 1-10 X molar excess over the calculated monolayer for the protein type to be coupled. Mix thoroughly to dissolve. Low concentrations of protein may result in particle aggregation, because a single protein molecule can react with more than one particle. [Pg.602]


See other pages where Suspensions particles is mentioned: [Pg.629]    [Pg.443]    [Pg.428]    [Pg.146]    [Pg.631]    [Pg.44]    [Pg.188]    [Pg.805]    [Pg.163]    [Pg.2]    [Pg.56]    [Pg.448]    [Pg.204]    [Pg.60]    [Pg.571]    [Pg.572]    [Pg.132]    [Pg.132]    [Pg.588]    [Pg.594]    [Pg.594]    [Pg.596]   
See also in sourсe #XX -- [ Pg.166 ]

See also in sourсe #XX -- [ Pg.158 , Pg.169 , Pg.171 ]




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Anisotropic particles suspensions

Ceramic suspensions particle size

Ceramic suspensions particle structure

Colloidal suspension of solid particles

Dilute suspensions particle fall speed

Dynamic mobility spherical particles suspensions

Exercise 15.1 Distribution of particles in suspension and grain size sorting resulting from settling

Fluid-particle suspensions

Large primary suspension particles

Large solid particles, suspensions

Lipid suspension particles

Mass Transfer to Suspensions of Small Particles

Microfiltration and Coagulation of Particle Suspensions

Mono-disperse colloidal particles suspensions

Monodisperse suspensions particle size measurements

Nonspherical particles suspension viscosity

Particle Interactions in Suspensions

Particle concentrated suspension

Particle size distribution in suspension polymerization

Particle size distribution suspension polymerization

Particle size ophthalmic suspensions

Particle size reduction suspensions

Particle size suspensions, solubility

Particle stress, suspensions

Particle suspension layer stability

Particle-gas suspension

Particle/cell suspension

Particles and Colloidal Suspensions

Particles being held in suspension by Brownian motion

Particles in suspension

Pharmaceutical suspensions particles flocculation

Point particles in dilute gases and suspensions

Polydisperse suspensions particle size measurements

Rheology of clay particle suspensions

Rigid particles suspensions

Rigid particles suspensions rheology, models

SUSPENSION STABILITY AND PARTICLE CAPTURE

Single particle suspension

Slurry reactor particle suspension

Small solid particles, suspensions

Spherical particles, suspension

Stresses for Suspensions of High-Aspect Ratio Particles and Molecules

Surfactants suspension particle adhesion

Suspension models particle shape effect

Suspension of Spherical Particles

Suspension of fine particles

Suspension of particles

Suspension of particles example calculation

Suspension of settling particles

Suspension of solid particles

Suspension particle nonlinear dynamics

Suspension polymerization particle size

Suspensions Containing Charged Particles

Suspensions Containing Large Solid Particles

Suspensions Containing Small Solid Particles

Suspensions Containung Non-charged Particles

Suspensions of coarse particles

Suspensions particle size

Suspensions particle size classification system

Suspensions particle size distribution

Suspensions, humic particles

Suspensions, monodisperse, particle

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