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Injectable polymers monomer

At 30% conversion a replicate analysis showed that composition could be determined with 1.4% reproducibility (standard deviation as a % of mean) and conversion with -h 2.1%. A duplicate at 52% conversion showed a relative error ( fference/mean) of 1.7% and 2.7% respectively. Between 30 and 80% conversion, although no gel effe t is evident in the data the polymer/monomer mkture becomes sticky and difficult to handle. Somewhat beyond 80% conversion the n-butyl meth rylate content for these compositions becomes too small to be detected with the procedure developed. Additional optimization of concentration injected and det tor utilized is required for very high conversions. [Pg.163]

Table V shows the concentrations of polymer (usually in THF/polymer/monomer mixtures), the GPC that they were directly injected into, and the Column Code involved (Ref. Table 1). No effect of different concentration was observed in the chromatograms from GPC 2 when concentrations of samples A to E inclusive were changed by 33%. GPC 1 chromatograms were too disturbed by sampling to be useful except as a rough guide to sampling position. Table V shows the concentrations of polymer (usually in THF/polymer/monomer mixtures), the GPC that they were directly injected into, and the Column Code involved (Ref. Table 1). No effect of different concentration was observed in the chromatograms from GPC 2 when concentrations of samples A to E inclusive were changed by 33%. GPC 1 chromatograms were too disturbed by sampling to be useful except as a rough guide to sampling position.
The results are shown in Figures 3.76(a) and (b). Figure 3.76(a) shows the conductivity as a function of the potential of the polymer-coated electrode and Figure 3.76(b) shows the conductivity as a function of the charge injected per monomer ring. The conductivity of the fully oxidised polymer was found to be significantly lower than that obtained by other workers via ex situ measurements, 10 2 1 cm 1 compared with I02 fi 1 cm The difference... [Pg.344]

Polymers. In order to prove the versatility of the microfluidics system as a platform for different applications, its ability to separate mixtures of polymers was tested. MALDI mass spectra show two different polymer distributions separated in time (Figure 11.6). The two different polymer distributions can be easily assigned to the injected polymers by the peak-to-peak separation due to the different molecular weight of the monomers. The first pattern recorded in time was assigned to PS (Figure 11.6a) and the... [Pg.264]

Suspension polymerization of methyl methacrylate is used mainly for the production of injection moulding and extrusion grades of polymer. Suspension polymer is also used in the preparation of polymer-monomer doughs for dentures. Polymerization is carried out batch-wise in a stirred reactor, jacketed for heating and cooling the reactor is capable of withstanding a pressure of 3—4 atmospheres. A typical basic formulation might be as follows ... [Pg.129]

The reaction was carried out in 10 vials using a robot to add more monomer at the appropriate times. Each vial contained monomer, initiator, and an excess of the cis-olefln terminator. At the end of each 30 min cycle, a second addition of monomer was added to vials 2-10. On each subsequent monomer addition, another vial was eliminated so that at the last time period, only the 10th vial received an injection of monomer. As can be seen in the table, even after 10 additions of monomer, the polymer... [Pg.27]

Dicyclopentadiene is also polymerized with tungsten-based catalysts. Because the polymerization reaction produces heavily cross-Unked resins, the polymers are manufactured in a reaction injection mol ding (RIM) process, in which all catalyst components and resin modifiers are slurried in two batches of the monomer. The first batch contains the catalyst (a mixture of WCl and WOCl, nonylphenol, acetylacetone, additives, and fillers the second batch contains the co-catalyst (a combination of an alkyl aluminum compound and a Lewis base such as ether), antioxidants, and elastomeric fillers (qv) for better moldabihty (50). Mixing two Uquids in a mold results in a rapid polymerization reaction. Its rate is controlled by the ratio between the co-catalyst and the Lewis base. Depending on the catalyst composition, solidification time of the reaction mixture can vary from two seconds to an hour. Similar catalyst systems are used for polymerization of norbomene and for norbomene copolymerization with ethyhdenenorbomene. [Pg.431]

An example is poly(bis(p-carboxyphenoxy)propane) (PCPP) which has been prepared as a copolymer with various levels of sebacic anhydride (SA). Injection molded samples of poly (anhydride) / dmg mixtures display 2ero-order kinetics in both polymer erosion and dmg release. Degradation of these polymers simply releases the dicarboxyhc acid monomers (54). Preliminary toxicological evaluations showed that the polymers and degradation products had acceptable biocompatibiUty and did not exhibit cytotoxicity or mutagenicity (55). [Pg.192]

Fractionation by GPC was sessed by changing injected concentrations and by GPC analysis of polymer before and after fractionation. Efficiency of fractionation of polymer from monomer did not appear to be a source of error. In fact, an advantage of this method over others is that the separation of monomer from the polymer can be clearly monitored and controlled,... [Pg.163]

SAMPLE NO. POLYMERIZATION TIME (min) CONVERSION STYRENE IN MONOMER INITIAL STYRENE IN MONOMER GPC 2 CHROMATOGRAM VARIANCE GPC INJECTED INTO TOTAL AMOUNT OF POLYMER INJECTED (mg) VOLUME INJECTED GAUSSIAN FIT TO GPC 2 CHROMATOGRAM... [Pg.173]


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