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Resin porosity

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]

Thermoporometry [107] has also been used in evaluating resin porosity [108] and in effect gives information on the solvent wetted state of resins. The technique exploits the phenomenon that the freezing point of a liquid is depressed when it is confined in pores of small radius. Calorimetric measurements on solvent imbibed resins at increasingly reduced temperatures allows a distribution curve to be generated. This in turn can be related to a pore size distribution. The technique is not routine nor widely practiced and more information is available in reference [17]. [Pg.31]

Concentration gradients can exist within the resin pore structure. Ion diffusion is complex since the resin porosity is low and this leads to steric hindrance effects and tortuous diffusion paths. Also, ion diffusion is coupled to the fixed ionic groups and the mobility of each ion within the resin due to charge balance. This coupled diffusion is present in both boundary layer and pore transport. Also, the forward and reverse rates of ion exchange can be affected by the different mobilities of the ions. [Pg.217]

Ion-exchange chromatography involves more variables than other forms of chromatography. Distribution coefficients and selectivities are functions of pH, solute charge and radius, resin porosity, ionic strength and type of buffer, type of solvent and temperature. The number of experimental variables makes lEC a very versatile technique but a difficult one because of the effort needed to optimise a separation. [Pg.25]

Precipitation of the growing polymer from the initial solution of styrene and DVB in an inert diluent during crosshnking copolymerization results in the formation of a two-phase heterogeneous network, in which one phase is presented hy the highly crosshnked and rigid polymer, while the rejected diluent forms another phase. After removing the diluent, permanent voids remain in the copolymer beads. The total pore volume, and the inner surface area, S, are the major characteristics of the porous structure these are intimately related to pore size and pore size distribution. These parameters determine the practical apphcation frelds of the polymeric adsorbent resins therefore, a precise quantitative characterization of resin porosity becomes an important task. [Pg.72]

Keywords silicone resin, porosity, dielectric constant, low k, modulus... [Pg.696]

Type Functional group Specific surface area mVg-resin Porosity ml/ml-resin Exchange capacity meg/g-resin... [Pg.173]

TABLE 2.1 Effect of Resin Porosity on the Powder Mix Time of PVC Resins... [Pg.21]

Resin Gel Content Although the resin requirements for extruded film and sheet are similar to those of other general purpose extrusion applications, some differences exist. Resin gel content (or lack thereof) is extremely important for extruded film and sheet. Since suspension resins typically have lower gel levels than mass resins, suspension resins are generally preferred in these applications. The two main ways resin manufacturers control gel content are through resin reactor hygiene and resin porosity. [Pg.30]

Higher levels of resin porosity also tend to reduce gel levels in the final product. The more porosity a resin particle has, the more easily it can absorb plasticizer and fuse with the other resin particles. The correlation is not perfect, but there is a strong relationship between gel content and porosity in resins for flexible PVC applications. [Pg.30]

Resin Porosity Resin porosity is a desirable characteristic for flexible PVC. In rigid PVC, a small amount of porosity is desirable to facilitate the absorption of the liquid stabilizer and other lubricants. However, excessive resin porosity can be a detriment to rigid PVC by lowering the bulk density of the resin. As mentioned above, this can have a negative effect on extruder output. [Pg.34]

Duolite A-7 2.2 1.12 Phenolic type resin. High porosity and hydrophilic matrix. pH range is 0 to 6. [Pg.1113]

Suspension polymerization of VDE in water are batch processes in autoclaves designed to limit scale formation (91). Most systems operate from 30 to 100°C and are initiated with monomer-soluble organic free-radical initiators such as diisopropyl peroxydicarbonate (92—96), tert-huty peroxypivalate (97), or / fZ-amyl peroxypivalate (98). Usually water-soluble polymers, eg, cellulose derivatives or poly(vinyl alcohol), are used as suspending agents to reduce coalescence of polymer particles. Organic solvents that may act as a reaction accelerator or chain-transfer agent are often employed. The reactor product is a slurry of suspended polymer particles, usually spheres of 30—100 pm in diameter they are separated from the water phase thoroughly washed and dried. Size and internal stmcture of beads, ie, porosity, and dispersant residues affect how the resin performs in appHcations. [Pg.386]

Ion-exchange resins are categorized by the nature of functional groups attached to a polymeric matrix, by the chemistry of the particular polymer in the matrix, and by the porosity of the polymeric matrix. There are four primary types of functionaHty strong acid, weak acid, strong base, and weak base. Another type consists of less common stmctures in specialty resins such as those which have chelating characteristics. [Pg.371]

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]

Macroporous resins are also called macroreticular. Macroporous resins have a measurable porosity. It does not disappear when the resin is dry. Porosity is more dependent on the solvent used when manufacturing the copolymer than on the degree of cross-linking. [Pg.376]

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]

Heat resistance is an important characteristic of the bond. The strength of typical abrasive stmctures is tested at RT and at 300°C. Flexural strengths are between 24.1 and 34.4 MPa (3500—5000 psi). An unmodified phenoHc resin bond loses about one-third of its room temperature strength at 298°C. Novolak phenoHc resins are used almost exclusively because these offer heat resistance and because the moisture given off during the cure of resole resins results in undesirable porosity. Some novolaks modified with epoxy or poly(vinyl butyral) resin are used for softer grinding action. [Pg.305]

The resins used in air and oil filters are moderate-to-low molecular weight, catalyzed by caustic in one step 10—20% alcohol is added soHds content is in the range of 50—60%. These resins are designed to penetrate the sheet thoroughly, yet not to affect the porosity of the paper. In the B-stage, the resin must have sufficient flexibiHty to permit pleating the C-stage should have stiffness and resistance to hot oil. [Pg.306]

Synthetic polymeric adsorbents have a high porosity, large surface area, and an inert hydrophobic surface. These resins can be regenerated ... [Pg.227]

Polymer-based, synthetic ion-exchangers known as resins are available commercially in gel type or truly porous forms. Gel-type resins are not porous in the usual sense of the word, since their structure depends upon swelhng in the solvent in which they are immersed. Removal of the solvent usually results in a collapse of the three-dimensional structure, and no significant surface area or pore diameter can be defined by the ordinaiy techniques available for truly porous materials. In their swollen state, gel-type resins approximate a true molecular-scale solution. Thus, we can identify an internal porosity p only in terms of the equilibrium uptake of water or other liquid. When crosslinked polymers are used as the support matrix, the internal porosity so defined varies in inverse proportion to the degree of crosslinkiug, with swelhng and therefore porosity typically being more... [Pg.1500]

Truly porous, synthetic ion exchangers are also available. These materials retain their porosity even after removal of the solvent and have measurable surface areas and pore size. The term macroreticular is commonly used for resins prepared from a phase separation technique, where the polymer matrix is prepared with the addition of a hq-uid that is a good solvent for the monomers, but in which the polymer is insoluble. Matrices prepared in this way usually have the appearance of a conglomerate of gel-type microspheres held together to... [Pg.1500]


See other pages where Resin porosity is mentioned: [Pg.376]    [Pg.376]    [Pg.210]    [Pg.265]    [Pg.545]    [Pg.667]    [Pg.210]    [Pg.19]    [Pg.376]    [Pg.376]    [Pg.210]    [Pg.265]    [Pg.545]    [Pg.667]    [Pg.210]    [Pg.19]    [Pg.1109]    [Pg.15]    [Pg.403]    [Pg.352]    [Pg.373]    [Pg.378]    [Pg.379]    [Pg.532]    [Pg.532]    [Pg.185]    [Pg.307]    [Pg.125]    [Pg.55]    [Pg.346]    [Pg.521]    [Pg.493]    [Pg.376]    [Pg.1501]    [Pg.1720]    [Pg.395]   
See also in sourсe #XX -- [ Pg.43 ]

See also in sourсe #XX -- [ Pg.37 ]




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