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Polymer end-points

Phthahc resins are usually processed to an acid number of 25—35, yielding a polymer with an average of 1800—2000. The solution viscosity of the polymer is usually followed to ascertain the polymer end point. The resin is cooled to 150°C and hydroquinone stabilizer (150 ppm) is added to prevent premature gelation during the subsequent blending process with styrene at 80°C. The final polymer solution is cooled to 25°C before a final quaUty check and dmmming out for shipment. [Pg.316]

The conformational properties of a flexible polyelectrolyte chain of length L (L oo) and its spatial distribution of monomers follow from the probability density G(r, Ur, 0) (Green function), where r(0) = r and r(L) = r denote the positions of the polymer end points. The Green function itself follows from the equation [40, 41, 58-60, 150] ... [Pg.7]

When polymers or other water-soluble substances are present in the sample, it is advantageous to add a small amount of chloroform to the initial reaction mixture after the subsequent addition of water, a two-phase system results which may be titrated in the usual way to a starch end point or by observing the disappearance of the iodine colour in the chloroform layer. [Pg.808]

A suitable functional group is assayed in the same sample. In general chemistry and many polymer applications, this is merely the titration of acid groups with a base, or vice versa. Note that only volumetric glassware and a method for end point determination are required to do this. [Pg.30]

High molecular weight polymers or gums are made from cyclotrisdoxane monomer and base catalyst. In order to achieve a good peroxide-curable gum, vinyl groups are added at 0.1 to 0.6% by copolymerization with methylvinylcyclosiloxanes. Gum polymers have a degree of polymerization (DP) of about 5000 and are useful for manufacture of fluorosiUcone mbber. In order to achieve the gum state, the polymerization must be conducted in a kineticaHy controlled manner because of the rapid depolymerization rate of fluorosiUcone. The expected thermodynamic end point of such a process is the conversion of cyclotrisdoxane to polymer and then rapid reversion of the polymer to cyclotetrasdoxane [429-67 ]. Careful control of the monomer purity, reaction time, reaction temperature, and method for quenching the base catalyst are essential for rehable gum production. [Pg.400]

As the polymer molecular weight increases, so does the melt viscosity, and the power to the stirrer drive is monitored so that an end point can be determined for each batch. When the desired melt viscosity is reached, the molten polymer is discharged through a bottom valve, often under positive pressure of the blanketing gas, and extmded as a ribbon or as thick strands which are water-quenched and chopped continuously by a set of mechanical knives. Large amounts of PET are also made by continuous polymerization processes. PBT is made both by batch and continuous polymerization processes (79—81). [Pg.294]

Ozonolysis. Ozonolysis of the methylhexadiene polymer was conducted (21)at room temperature on a solution of 1,03 g. polymer in 20 ml. tetrahydrofuran with the aid of the Wellsbach ozonizer. The end point for the ozonolysis was observed after about 15 min. by the reaction of excess ozone with starch-iodide solution. Triphenylphosphine was added to the reaction mixture and allowed to react at room temperature for 60 hr. The resulting product was analyzed by GLC (Hewlett Packard 5750, Porapak Q 10 ft. x 1/8 in. column at 110°C, helium pressure 60 psi, thermal conductivity detector at 190°C, injector 200°c). [Pg.173]

For fibres made from the same polymer but with different degrees of chain orientation the end points of the tensile curves, a5, are approximately located on a hyperbola. Typical examples of this fracture envelope are shown in Figs. 8... [Pg.22]

Titrations in non-aqueous solvents have been traditionally an important tool for the accurate determination of various pharmaceuticals, some acids in foods, use of some acids or bases in detergents, cosmetics and textile auxiharies, in the analysis of industrial process streams, the analysis of polymers [1-7]. The determination of the pK or pK values of organic compoimds with acidity or basicity constant less than 10 can only be reahsed in non-aqueous media. Although water has excellent solvent properties, it is not suitable for such organic compotmds since the pH jump at the equivalence point in aqueous solution carmot be evalrrated with reasonable accuracy, with this resrrlt, the end point carmot be found. Moreover, most of this compotmds ate not soluble in water. For these reasons, titration in non-aqueous media has recently acqttired great importance. It is now well known that non-aqueous titrations greatly depend on the solvents used [4, 8-13]. [Pg.327]

Finally, one should recognize that determinations of the critical concentration depend wholly on the validity of the equilibrium or steady-state assumptions. If a stable end point for prdtomer-polymer coexistence is not attained, then kinetic factors affect the observed behavior. With the well recognized tendency of tubulin to lose its ability to engage in assembly reactions upon storage even at low temperature, and with the presence of various nucleotide hydrolases and transphosphorylases in microtubule protein, such kinetic effects are a serious problem. [Pg.190]

Though the above mechanism had value in describing the steady-state tubulin flux, Karr and Purich (1979) pointed out that a number of association-dissociation steps can occur for each net protomer addition. They found that the rate of isothermal dilution-induced disassembly of microtubules proceeded at rates 500- to 1000-fold greater than the observed treadmilling rate which itself corresponded to a turnover of about 7% of the tubulin pool/hour (Margolis and Wilson, 1978). Karr and Purich (1979) also proposed that the unidirectional treadmilling model be amended to account for the rapidity of on-off events at the polymer ends, and they offered the alternative mechanism presented here. [Pg.201]

For higher accuracy in the low polymer concentration range, two different methods were used. In the case of PAA, potentiometric titrations of solutions of PAA were performed with 0.01 N NaOH using a Brinkman model, Westbury, NY, automated titrator. Blank tests indicated no interfering species. Known amounts of PAA were used to prepare a calibration curve immediately after titration of the samples containing unknown amounts of polymer. The starting point of the titration was pH 4.0, and the end point was reached near pH 8. Total volumes of 75 or 100 cc were used for the titrations, and the ionic strength was controlled at 0.01 M NaCl. [Pg.295]

Wenz and colleagues at Bayer Polymers Inc. describe the use of Raman spectroscopy to determine the reaction end point for the emulsion production of ABS graft copolymer [197]. Early termination reduces product yield and results in an extra product purification step termination too late reduces product quality. [Pg.222]

Fig. 4 a Mean-field result (solid line) for the rescaled brush free energy per polymer as a function of the inverse interaction parameter 1/F- The infinite stretching resnlt is indicated by a horizontal dotted line, the broken straight line denotes the infinite stretching result with the leading correction dne to the finite end-point distribntion entropy. b Rescaled lateral pressnre within mean-field theory (solid line) compared with the asymptotic infinite-stretching result (dotted line)... [Pg.162]

Fig. 5 Left Mean-field results for the rescaled averaged polymer paths which end at a certain distance Ze from the wall for (S = I, 10, 100 (from top to bottom), corresponding to stretching values of y = 1.1, 1.9, 5.6 (as defined in Eq. 18). The thick solid line shows the unconstrained mean path obtained by averaging over all end-point positions. Note that the end-point stretching is small but finite for all finite stretching parameters p. Right End-point distributions... Fig. 5 Left Mean-field results for the rescaled averaged polymer paths which end at a certain distance Ze from the wall for (S = I, 10, 100 (from top to bottom), corresponding to stretching values of y = 1.1, 1.9, 5.6 (as defined in Eq. 18). The thick solid line shows the unconstrained mean path obtained by averaging over all end-point positions. Note that the end-point stretching is small but finite for all finite stretching parameters p. Right End-point distributions...
Aquacoat ECD (ethylcellulose polymer, acetyl alcohol, and sodium lauryl sulfate in water) Coating for tablets and capsules Repeat-dose toxicity with routine end points (90 days—oral rat) and reproduction toxicity (embryo-fetal study in rat) No adverse findings for general toxicity or reprotoxicity 29, 30... [Pg.22]


See other pages where Polymer end-points is mentioned: [Pg.466]    [Pg.160]    [Pg.6151]    [Pg.147]    [Pg.466]    [Pg.160]    [Pg.6151]    [Pg.147]    [Pg.43]    [Pg.236]    [Pg.225]    [Pg.405]    [Pg.124]    [Pg.294]    [Pg.117]    [Pg.298]    [Pg.302]    [Pg.37]    [Pg.113]    [Pg.70]    [Pg.242]    [Pg.392]    [Pg.705]    [Pg.168]    [Pg.244]    [Pg.169]    [Pg.164]    [Pg.167]    [Pg.169]    [Pg.159]    [Pg.296]    [Pg.35]    [Pg.96]    [Pg.88]   
See also in sourсe #XX -- [ Pg.160 ]

See also in sourсe #XX -- [ Pg.160 ]




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End point

Pointed end

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