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Impurities incorporation, and purification

Meanwhile attempts to find an air oxidation route directly from p-xylene to terephthalic acid (TA) continued to founder on the relatively high resistance to oxidation of the /Moluic acid which was first formed. This hurdle was overcome by the discovery of bromide-controlled air oxidation in 1955 by the Mid-Century Corporation [42, 43] and ICI, with the same patent application date. The Mid-Century process was bought and developed by Standard Oil of Indiana (Amoco), with some input from ICI. The process adopted used acetic acid as solvent, oxygen as oxidant, a temperature of about 200 °C, and a combination of cobalt, manganese and bromide ions as catalyst. Amoco also incorporated a purification of the TA by recrystallisation, with simultaneous catalytic hydrogenation of impurities, from water at about 250 °C [44], This process allowed development of a route to polyester from purified terephthalic acid (PTA) by direct esterification, which has since become more widely used than the process using DMT. [Pg.13]

Many other nonequilibrium modes of impurity incorporation occur, primarily through segregation of impurities at defect and inclusion sites. As discussed throughout this chapter, these impurities can be systematically reduced from the final product through optimization of crystallization and separation steps. In particular, the thermodynamic approach outlined in Section 3.5.1 can be effectively used commercially to select solvents and optimize processing conditions to greatly improve the purification of crystalline materials. [Pg.96]

Figure 7.5 Mechanisms of impurity incorporation, measures to prevent it, and additional purification steps. Figure 7.5 Mechanisms of impurity incorporation, measures to prevent it, and additional purification steps.
Figure 15.4 Mechanisms of impurity incorporation in a crystal layer as well as measures to prevent it and additional purification measures (postc stallization treatments) [6,7]. Figure 15.4 Mechanisms of impurity incorporation in a crystal layer as well as measures to prevent it and additional purification measures (postc stallization treatments) [6,7].
Well formed crystals are expected to be pure because each molecule or ion must fit perfectly into the lattice as it leaves the solution. Impurities would normally not fit as well in the lattice, and thus remain in solution preferentially. Hence, molecular recognition is the principle of purification in crystallization. However, there are instances when impurities incorporate into the lattice, hence, decreasing the level of purity of the final crystal product. Also, in some cases, the solvent may incorporate into the lattice forming a solvate. In addition, the solvent may be trapped (in liquid state) within the crystal formed, and this phenomenon is known as inclusion. [Pg.22]

Here, we show two cases for impurity segregation between melt and crystal as it grows in time. Note that an initial purification occurs in both cases but the distribution coefficient for the case on the right is such that the amount of impurity actually incorporated into the crystal, ki Cq. [Pg.279]

It appears that purification of commercially available solvents is sometimes required for the complete elimination of impurity resonances. Occasionally, these impurities may be turned into advantage, as in the case of C2D2CI4 where the (known) C2DHCI4 content may be used as an internal standard for quantitation. Thus, removal of every impurity peak is not always essential for identification and quantitative analysis of stabilisers in PE. Determination of the concentration of additives in a polymer sample can also be accomplished by incorporation of an internal NMR standard to the dissolution prepared for analysis. The internal standard (preferably aromatic) should be stable at the temperature of the NMR experiment, and could be any high-boiling compound which does not generate conflicting NMR resonances, and for which the proton spin-lattice relaxation times are known. 1,3,5-Trichlorobenzene meets the requirements for an internal NMR standard [48]. The concentration should be comparable to that of the analytes to be determined. [Pg.698]

The synthetic route should aim at incorporating the label as late as possible in the sequence. This requires the development of rapid syntheses (generally not more than 3 h for compounds) including HPLC purification and formulation of the radiopharmaceutical for intravenous injection. The large amounts of reagents compared to those of the labelled substrate [20] usually lead to rapid reactions. However, unexpected labelled compounds can also arise from side reactions of reagents in excess or from reactive impurities present in the reaction medium [21]. [Pg.205]

The main requirement in this area is thus to minimise the presence of deleterious impurities, notably transition elements and organic materials. This can be achieved by careful choice of raw materials and by avoiding contamination during processing, particularly milling. In some cases special purification steps are incorporated into the production process to remove problem contaminants. [Pg.74]

In any event, extensive purification in the laboratory by any applicable method, including preparative high-performance liquid chromatography, is recommended as part of growth potential determination studies. The importance of this effort cannot be over-stated since a particular compound may not grow only because of the presence of impurities and not because of inherent crystal lattice incorporation restrictions. [Pg.217]

Besides chemical conversion and chemical vapor transport, the reduction process is a purification step, too. Trace impurities, always present in the oxide, may evaporate. On the other hand, foreign phases can be incorporated during the CVT growth of tungsten, finally leading to inclusions in the tungsten powder particles. This is of special interest in the production of non-sag tungsten wire used for incandescent lamps. [Pg.89]

Lastly, the mass transport processes at the crystal-liquid interface play a central role in crystallization. The influence of solvent and impurities on the structure and growth rates of faces is considered in this chapter along with its effect on the incorporation of impurities. The solvent solute-impurities interactions in solution will also be shown to interact in subtle, but important, ways with the interface during the crystallization process. With appropriate thermodynamic analysis it is shown how these interactions ultimately affect crystallization as a purification process. [Pg.67]


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