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Forming and Polymerization

The heated drawing machine is one of the most expensive parts of the system. The following is a list of the main features that the material used should satisfy  [Pg.27]

If the resin is scratched on the mold surface, not only flie final finishing of the product surface will be lacking, but the removed resin may be absorbed in oflier surface areas of the pultruded product as well, or may even clog up flie mold itself. In this case, an intermittent pultrusion is required, in order to obtain consistent polymerization along the entire mold. If so, flie initial part of the drawing should be cured to prevent the resin from gelling outside the mold and around it [Pg.27]

Usually, drawing machines are composed of two separated parts along a horizontal plane parallel to the pultrusion direction. In the case of simpler sections, for instance, bars, single-block molds are used, obtained by piercing it and flien smoothing the hole that can also be chromium-coated wifli specific techniques. The finishing of the product surface is positively impacted by the absence of joints in the molds. [Pg.27]

The heating of the material within the drawing machine takes place in the majority of systems via conduction through the drawing machine. This, in turn, is heated through external plates or electrical resistances located inside. This second solution is, of course, more expensive than the first. Oflier heating systems make use of radiating systems or hot oil transfer systems. [Pg.28]

Nevertheless, in order to grant a uniform distribution and recurrence of the object s properties in all its parts and at every work shift, the temperature control, which ranges on average between 150 °C and 170 °C, should only allow for a maximum tolerance of 1 °C. [Pg.28]


Continuous stirred-tank reactors can behave very differently from batch reactors with regard to the number of particles formed and polymerization rate. These differences are probably most extreme for styrene, a monomer which closely follows Smith-Ewart Case 2 kinetics. Rate and number of particles in a batch reactor follows the relationship expressed by Equation 13. [Pg.9]

In the prepolymerizer, the polymer particles are formed and polymerized to 7-8 wt. % conversion before being transferred to the autoclave where the particles are polymerized to a solid powder at about 88% conversion. [Pg.269]

The free-radicals are generated by discharge of proton, peroxides and easily reducible compounds at the cathode according to Eq. (1—4). The radial-anion of monomer is obtained by both direct and indirect electron transfer process [Eq. (5—6)]. The indirect process means that the active oxidizing species is formed from the electrolytes by electrode reaction, followed by interaction with the monomer. An unstable monomer like a,a -2-trichloro-p-xylene is formed and polymerizes instantaneously [Eq. (7)]. The regeneration of ferrous ion from the pool of used up ferric ion in a redox system is electrolytically successful [Eq. (8)] and an... [Pg.379]

These kinetic results have led to a variety of interpretations. Magat and associates have proposed kinetic schemes based on the idea that a steady state does not exist and that only small (primary) radicals can terminate polymer chains (52, 93). Bamford and Jenkins have criticized this concept of emulsion-type polymerization (77). They point out that if the source of initiation were removed no more small radicals would be formed and polymerization should continue indefinitely. They cite a photosensitized reaction at 60° in which the light was shut off at about 15% conversion, whereupon the rate fell to one-half of its original value in 60 seconds. Bamford and Jenkins point also to evidence from the fast reaction that argues against emphasis on termination between polymer radicals and small radicals. [Pg.414]

Under these conditions, however, stable peroxides may form and polymerization of lactones can occur. Lewis acids, e.g. BF3, SbFs, have been used to activate hydrogen peroxide in similar Baeyer-Villiger oxidations.241... [Pg.120]

The compound 0s03F2 (indistinguishable by X-ray methods from 0s02F3)533 is made by reaction of osmium metal with a 2 1 oxygen-fluorine mixture523 or from 0s04 and BrF3.524 There is much doubt about its structure, but the compound made at normal temperatures exists in at least three different crystalline forms and polymeric structures seem more likely.652... [Pg.596]

Aluminium ions produce an electric field in aqueous solution, which is sufficient for hydrated hydroxyions to form and polymerization to occur. Polymerization of the hydrolysis product results in new compounds, which structure has not yet been found [1,2,3,4]. [Pg.346]

Lewisite will rapidly react with water to form chlorovinylarsonous acid (CVAA). CVAA will slowly convert to the arsinoxide form and polymerization reactions can also occur. Earlier studies indicated that animals (species not specified) exposed to lewisite either topically or via injection were found to have measurable levels of CVAA in the urine and throughout the digestive system (Waters and Williams, 1950). [Pg.529]

When a mixture of a monomer and a radical initiator is heated, or photo-irradiated, in an ESR sample cell, propagating radicals are formed and polymerization proceeds... [Pg.63]

Lipids with the appropriate sugars as headgroups and with polymerizable units in the hydrophobic chain were synthesized, and liposomes from these monomers were formed and polymerized. Upon addition of Con A to the liposome solution, a precipitate formed that contained intact liposomes (as controlled by e.m.). If low molecular weight sugars which can compete with the liposomes for the binding sites of Con A were added, the liposomes re-dissolved (Fig. 8). Thus, in the case of a model system, it could be shown that recognition of polymeric liposomes by specific protein structures can be achieved (14). [Pg.30]

Under these conditions, a soluble double aluminium-copper (I) chloride salt (AlCuCU) is formed and polymerization is initiated by a benzene radical-cation species. The polymerization is slow and PPP is obtained as a dark brown solid, insoluble in all organic solvents, with a molecular weight lower than that of PPP obtained by the usual Kovavic route. [Pg.209]

Figure 7.4, a summary of various studies, reveals that in the second stage, fewer primary particles are formed and polymerization occurs essentially by the growth of polymer particles. As the propagation continues, monomer molecules from the emulsified monomer droplets (see Fig. 7.5) diffuse toward the propagating chains within the polymer particles. The diffusion of the monomer to the polymer particles continues at a fairly rapid rate to maintain constant monomer concentration in the polymer particles. [Pg.302]


See other pages where Forming and Polymerization is mentioned: [Pg.28]    [Pg.418]    [Pg.271]    [Pg.432]    [Pg.784]    [Pg.1109]    [Pg.696]    [Pg.24]    [Pg.27]    [Pg.284]    [Pg.311]    [Pg.430]   


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