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Particle size resins

Small particle size resins provide higher resolution, as demonstrated in Fig. 4.41. Low molecular weight polystyrene standards are better separated on a GIOOOHxl column packed with 5 /u,m resin than a GlOOOHg column packed with 10 /Ltm resin when compared in the same analysis time. Therefore, smaller particle size resins generally attain a better required resolution in a shorter time. In this context, SuperH columns are best, and Hhr and Hxl columns are second best. Most analyses have been carried out on these three series of H type columns. However, the performance of columns packed with smaller particle size resins is susceptible to some experimental conditions such as the sample concentration of solution, injection volume, and detector cell volume. They must be kept as low as possible to obtain the maximum resolution. Chain scissions of polymer molecules are also easier to occur in columns packed with smaller particle size resins. The flow rate should be kept low in order to prevent this problem, particularly in the analyses of high molecular weight polymers. [Pg.143]

The injection volume should be kept as small as possible to attain maximum resolution in analyses. This is particularly important in analyses on columns packed with small particle size resins such as SuperH. Injection volumes of 0.1 % or less of the total column volume are recommended on SuperH columns. A few times larger injection volumes may be applied to other series of H type columns. [Pg.145]

The sample concentration also should be kept as low as possible, particularly in analyses of polymers on columns packed with small particle size resins. The maximum sample concentration to achieve maximum resolution decreases as the sample molecular weight becomes higher and the resin particle size becomes smaller. It is usually in the range of 0.05-5 mg/ml, depending on the sample molecular weight and resin particle size. [Pg.145]

Polyvinyl acetate homopolymer emulsion. High molecular weight, large particle size resin. May be used with thermosetting resins, starches, softeners, nondurable water repellents and plasticizers. Base for adhesives. T(g) 28C. [Pg.383]

The same particle-size resin as used for the loading studies should be used for scaleup. The choice of particle size is a trade-off between resolution, which decreases with an increase in particle size, and pressure drop, which also decreases with an increase in particle size. Often, bulk resins are not offered in the full range of particle sizes that analytical columns are. Additionally, a size should be selected so that the column pressure drop does not exceed the resin limitations. [Pg.247]

Resin and fillers of different density are separated by rotational forces. Even when a mixture of different particle sized resin is used, the finer particles manage to sift through the larger particles to the mold surface. If a material of higher density such as filler is added, this will, by itself, enhance the movement of heavier particles to the mold surface to cause cross-sectional inhomogeneities in the composition. This has been confirmed by studies involving incorporation of... [Pg.771]

Polytetrafluoroethylene selection. Polymer selection for compounding granular PTFE is relatively straightforward. Fine cut resins are used as a starting point to produce filled compounds. These powders have relatively small particle size and form the most uniform compounds. Typically, smaller particle size resins produce compounds with higher physical properties. [Pg.25]

Much lower particle size resins are produced when compared to suspension resins (1 /u.m vs 150 /xm) with some residual siufactant from the polymerization process retained on the polymer. The small particle size imparts a lack of porosity to the resin and the demands on plasticizer behavior in a plastisol tend to be more complex. Choice of plasticizer is made with consideration given to the required viscosity of the plastisol and the required rheology of the plastisol. It is common to encounter formulations with two or three different plasticizers. [Pg.5709]

Poly(vinyl chloride). Poly(vinyl chloride) can be molded in liquid or powdered form. The liquid plastisols are fluid suspensions of fine particle-sized resins in a plasticizing liquid. PVC compounds are easily processed. They can be formulated to produce articles ranging from flexible to semirigid, with durometer hardness of 60 Shore A to 65 Shore D (see Vinyl Chloride Polymers). [Pg.7241]

The effectiveness and workability of a mortar or grout depends on the proper selection of fillers, or combination of fillers, particle size, resin viscosity, and reactivity of catalysts and hardeners. Hardener systems must be formulated for application at temperature ranges of approximately 60-90°F (15-32°C). The lower the temperature the slower the set the higher the temperature the faster the set. [Pg.178]

There are two principal PVC resins for producing vinyl foams suspension resin and dispersion resin. The suspension resin is prepared by suspension polymerization with a relatively large particle size in the 30—250 p.m range and the dispersion resin is prepared by emulsion polymerization with a fine particle size in the 0.2—2 p.m range (245). The latter is used in the manufacture of vinyl plastisols which can be fused without the appHcation of pressure. In addition, plastisol blending resins, which are fine particle size suspension resins, can be used as a partial replacement for the dispersion resin in a plastisol system to reduce the resin costs. [Pg.420]

Gopolymerization. The chemistry of the resin matrix, the type and degree of porosity, the particle size, and the particle size distribution are estabhshed in the copolymerization step. Formulations and operating procedures must be strictiy foHowed. Reaction vessels must be weH designed. Mistakes made during copolymerization are rarely corrected during functionalization. [Pg.372]

Post-curing and chemical modification improves chemical and solvent resistance (20). Paraformaldehyde and acetylene diurea are added to a hot borax solution. Toluenesulfonamide (p and o), a few drops of phosphorous acid. Brilliant Yellow 6G [2429-76-7] Rhodamine E3B, and Rhodamine 6GDN [989-38-8] are added. After heating, the mass is cured in an oven at 150°C. The resulting cured resin is thermoset but can be ground to fine particle sizes. [Pg.301]

Suspension Polymers. Methacrylate suspension polymers are characterized by thek composition and particle-size distribution. Screen analysis is the most common method for determining particle size. Melt-flow characteristics under various conditions of heat and pressure are important for polymers intended for extmsion or injection molding appHcations. Suspension polymers prepared as ion-exchange resins are characterized by thek ion-exchange capacity, density (apparent and wet), solvent sweUing, moisture holding capacity, porosity, and salt-spHtting characteristics (105). [Pg.270]

Phenolic Dispersions. These systems are predominantly resin-in-water systems in which the resin exists as discrete particles. Particle size ranges from 0.1 to 2 p.m for stable dispersions and up to 100 p.m for dispersions requiring constant agitation. Some of the earliest nonaqueous dispersions were developed for coatings appHcations. These systems consist of an oil-modified phenoHc resin complexed with a metal oxide and a weak solvent. [Pg.298]

Dispersions. In phenoHc resin dispersions, the continuous phase is water or a nonpolar hydrocarbon solvent. The resin exists as droplets that have particle sizes of 1—20 p.m and are dispersed in the continuous phase. Aqueous dispersions are prepared either in situ during the preparation of the resin itself or by high shear mixing (25,35). [Pg.303]

Steps 1 and 2 can be described as physical plasticization, and the precise details of how this is carried out depends on the appHcations technology involved, ie, suspension or paste PVC. The rate at which step 2 occurs depends on the physical properties of plasticizer visocity, resin porosity, and particle size. [Pg.123]

Plastisol Viscosity and Viscosity Stability. After the primary contribution of the resin type in terms of its particle size and particle size distribution, for a given PVC resin, plastisol viscosity has a secondary dependence on plasticizer viscosity. The lower molecular weight and more linear esters have the lowest viscosity and hence show the lowest plastisol viscosity, ie, plastisol viscosity for a common set of other formulation ingredients... [Pg.127]

Of the three worldwide manufacturers of poly(ethylene oxide) resins. Union Carbide Corp. offers the broadest range of products. The primary quaUty control measure for these resins is the concentrated aqueous solution viscosity, which is related to molecular weight. Specifications for Polyox are summarized in Table 4. Additional product specifications frequendy include moisture content, particle size distribution, and residual catalyst by-product level. [Pg.343]


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