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In the second-stage the temperature is raised to 270 280 C and polymerization proceeds with the removal of ethylene glycol being facilitated by using a partial vacuum of 0.5 1 torr (66 133 Pa). The rst stage of the polymerization is a solution polymerization. The second stage is a melt polymerization since the reaction temperature is above the crystalline melting temperature of the polymer. Figure 2-12 illustrates a commercial process for this polymerization {Ellwood, 1967].

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Speakers in schematic symbol are shown in side-view, although the artwork is anything but standardized. Usually speakers consist of a small rectangle (the magnet) and a funnel-shaped trapezoid (the cone) whose dimensions vary with the artist s whim. Often the symbol is lacking all identifiers other than an ohm rating (commonly 8 , but lesser and greater ohmage will be encountered). At other times SPK or SPEAKER will be used as a label. If a speaker diameter is of importance, this information will more than likely be included in the master parts list. Speakers are polarized components (although, unlike batteries and LEDs, they ll still work if wired in reverse, but they ll be out of phase with other speakers in the system wired correctly). Examine the speaker s two soldering terminals and you ll probably see polarity marks. Follow this information and wire the speaker as the schematic indicates.

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2-126

(continued)

The properties and usefulness of the nal polymer depends on controlling its structure by appropriate control of process variables during polymerization and subsequent processing into product Temperature control and the choice of catalysts are critical in minimizing deliterious side reactions A dual catalyst system is used in PET synthesis The rst-stage catalyst is an acetate of manganese, zinc, calcium, cobalt, or magnesium Antimony(III) oxide is usually added as the second-stage catalyst; it is ineffective alone for the rst-stage reaction The rststage catalyst is often inactivated by the addition of an alkyl or aryl phosphite or phosphate The production of high-molecular-weight polymer requires the complete removal of ethylene glycol because of the unfavorable equilibrium that would otherwise exist If ethylene glycol were not removed, equilibrium would be established at too low an extent of reaction (approximately p < 0:7) and the product would be of very low molecular weight (Fig 2-8).

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A unique feature of the ester interchange process is the absence of the need for stoichiometric balance of the two functional groups at the start of the polymerization Stoichiometric balance is inherently achieved at the end of the second stage of the process In fact, an excess of ethylene glycol is initially used to increase the rate of formation of bis(2-hydroxyethyl)terephthalate The TA process is a modi cation of the DMT process Terephthalic acid and an excess of ethylene glycol (in the form of a paste) are used to produce the bis(2-hydroxyethyl)terephthalate, which is then polymerized as described above The TA process has grown to exceed the DMT process Poly(ethylene terephthalate), known by the trade names Mylar, Dacron, and Terylene, is a very high volume polymer the United States production of PET ber and plastic was over 95 billion pounds in 2001.

The global production is about 6 times that of the United States These gures are especially impressive when we note that PET was not introduced as a commercial product until 1953 Because of its high crystalline melting temperature (270 C) and stiff polymer chains, PET has good mechanical strength, toughness, and fatigue resistance up to 150 175 C as well as good chemical, hydrolytic, and solvent resistance Fiber applications account for about 45% of the total PET production Poly(ethylene terephthalate) ber has outstanding crease resistance, has good abrasion resistance, can be treated with crosslinking resins to impart permanent-press (wash-and-wear) properties, and can be blended with cotton and other cellulosic bers to give better feel and moisture permeation Fiber applications include wearing apparel, curtain, upholstery, thread, tire cord, and fabrics for industrial ltration More than 5 billion pounds of PET per year nd applications as plastics, mostly for.

and the simultaneous yields of the prime seasoned corporate bond averages The municipal-corporate relationships are pictured in Chart 46 Municipal yields tended to be low (and municipal bond prices high) relative to corporates in periods when average marginal federal income tax rates were high because municipal interest was tax exempt The effects of tax bracket creep during the inflationary 1970 s are evident in Chart 46, as are the Reagan tax cuts in the 1980 s Relative to corporates, the former increased the demand for municipals and reduced their relative yield, while the latter had the opposite effect RISK RATES Although prime bond yields usually ranged between 250 and 5% during the first sixty-five years of the twentieth century in the United States, investors were offered a wealth of opportunities to work their money harder.

FIGURE C-12

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