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Resin performance

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]

Molecular weight assignments for such resins will be dependent on the method used for measurement. Each manufacturer has his own relative scale. In practice, absolute molecular weight determination is not important. The method used must discriminate between resins with sufficient resolution to allow prediction of resin performance in the applications of interest. [Pg.890]

Variances in resin performance and capacities can be expected from normal annual attrition rates of ion-exchange resins. Typical attrition losses that can be expected include (1) Strong cation resin 3 percent per year for three years or 1,000,000 gals/ cu.ft (2) Strong anion resin 25 percent per year for two years or 1,000,000 gals/ cu.ft (3) Weak cation/anion 10 percent per year for two years or 750,000 gals/ cu. ft. A steady falloff of resin-exchange capacity is a matter of concern to the operator and is due to several conditions ... [Pg.387]

A second strategy is to attach a linker (also referred to as a handle or anchor) to the resin followed by assembly of the molecule. A linker is bifunctional spacer that serves to link the initial synthetic unit to the support in two discrete steps (Fig. 3). To attach a linker to a chloromethyl-PS resin, a phenol functionality such as handle 4 is used to form an ether bond (Fig. 4). To attach the same handle to an amino-functionalized support, acetoxy function 5 or a longer methylene spacer of the corresponding phenol is applied to form an amide bond. Both of these resins perform similarly and only differ in their initial starting resin [4], An alternative approach is to prepare a preformed handle in which the first building block is prederivatized to the linker and this moiety is attached to the resin. For peptide synthesis, this practice is common for the preparation of C-terminal peptide acids in order to reduce the amount of racemization of the a-carbon at the anchoring position [5],... [Pg.183]

Purify the thiolated antibody by gel filtration using a desalting resin. Perform the chromatography using 0.1M sodium phosphate, 0.15M NaCl, pH 7.2, containing lOmM EDTA as the buffer. To obtain efficient separation between the reduced antibody and excess reductant, the sample size applied to the column should be at a ratio of no more... [Pg.794]

Remove excess crosslinker by gel filtration using a desalting resin. Perform the chromatography using 0.1M sodium phosphate, 0.15M NaCl, lOmM EDTA, pH 7.5. [Pg.839]

As an example for an application of the method to post-cleavage synthesis of heterocycles, the cyclization of 2-nitroaryl azides based on the ortho-ri tto resins performed at approximately 100 °C yields benzofuroxane in high purities (Equation 78) <2004SL1163>. [Pg.384]

Compression rates typically vary between 0.0025 and 0.0055 for pellet feedstocks. If the compression rate is too low, then the compaction rate of the solid feedstock may not be high enough to force the entrained gas out through the hopper. If the compression rate is too high, poor melting performance and solid bed breakup can occur. For example, LDPE resins can be melted very easily using a screw with a compression rate of 0.0055, while LLDPE resins perform best with a compression rate near 0.0030 [3, 4]. If an LLDPE is extruded using a screw with a compression rate of 0.0055, then solid bed breakup and solid polymer particles in the extrudate are likely to occur. [Pg.192]

A new GPPS resin was tested at a customer s injection-molding plant as an Improvement over an incumbent resin manufactured by a competitor. The new resin performed well in the process except that it created parts with a 5% rejection rate due to a splay defect. The competitive resin was reported to run well but with a lower... [Pg.412]

One percent cross-linked polystyrene and Argopore resin performed equally well. The compatibility with polar solvents makes Argopore the most versatile resin when investigating new reaction conditions. [Pg.239]

The advantages of heterogeneous solid phase in combinatorial chemistry, especially in terms of purification procedures, can be obtained also by solution-phase chemistry, using solid support assistance. The resin performs a specific function during the library synthesis and then is simply removed by filtration, leaving the pure library components in solution. A well-known adapted technique uses solid supported reagents or catalysts during a combinatorial synthesis, where the solid phase is filtered off and discarded after the reaction in which it was involved. A new application is represented by solid-phase purification, where one or more solid supports are added to trap the excess of... [Pg.122]

Even with one type of resin, performance may vary greatly from sample to sample of the resin. This has been clearly shown for DEAE-cellulose by Himmelhoch and Petersen (1966). The charac-... [Pg.259]

The most frequently used resin type for water softening is the Na type. A typical ion-exchange reaction is described by Eq. (29). Owing to the presence of NaHCOg, treated effluent pH is always weakly caustic. The regeneration of resin performed with sodium chloride solution is described by Eq. (30) ... [Pg.281]

The solvents used for electrodeposition resins perform three functions. First, the solvent facilitates handling during the preparation of the aqueous solution since these carboxyl containing materials are either resinous or sticky semi-solids. Second, the solvent may accompany the vehicle during deposition and therefore can influence the flow characteristics during post-deposition bake or cure. Third, the solvent can confer better water solubility characteristics on the resin and thus help to maintain bath stability, a factor of prime importance in electrocoating. [Pg.150]

Teflon Fluorocarbon Resin, Performance Guide for the Chemical Processing Industry, DuPont, Technical Bulletin No. E-2162 3-3. [Pg.112]

Eor the resin manufacmrers, blending provides means to improve and broaden the resin performance and therefore it enhances the demands... [Pg.20]


See other pages where Resin performance is mentioned: [Pg.358]    [Pg.326]    [Pg.222]    [Pg.889]    [Pg.387]    [Pg.834]    [Pg.54]    [Pg.792]    [Pg.838]    [Pg.849]    [Pg.245]    [Pg.20]    [Pg.699]    [Pg.126]    [Pg.672]    [Pg.332]    [Pg.294]    [Pg.300]    [Pg.899]    [Pg.383]    [Pg.66]    [Pg.235]    [Pg.102]    [Pg.899]    [Pg.378]    [Pg.35]    [Pg.220]    [Pg.9]    [Pg.284]    [Pg.63]    [Pg.13]    [Pg.20]   
See also in sourсe #XX -- [ Pg.387 ]




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