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Inert fraction

The composition of the inert fraction depends on the chemical composition of the waste input. Most probably the inorganic parts of the PVC formulations, like metal-containing stabilisers, will end up in this slag. [Pg.13]

In the case of Mg (Fig. 2 and Table 1) it is evident that magnesium was equally extracted after the first and fifth phase, which indicates that mainly in these samples Mg is either in the most mobile, exchangeable fraction, that is the fraction of Mg-clays (probably the montmorillonite clays) or in the inert fraction, Mg from the silicate matrix. [Pg.298]

The relevant models for the reactive distillation column and peripherals have been developed and implemented into the simulation environment ASPEN Custom Modeler . Simulations of the heterogeneously catalysed synthesis of TAME have included 11 components. The species and the boiling points at the operating pressure of 4 bar are listed in Table 1. The key components of the inert fractions of the feed have been used to represent the hydrocarbon fractions (see Table 1). VLE is described by UNIQUAC model, with the Redlich-Kwong equation of state. In simulations, four reactions are considered the main reactions (l)-(3) and the formation of dimethyl ether (7). [Pg.716]

Separations based upon differences in the physical properties of the components. When procedures (1) or (2) are unsatisfactory for the separation of a mixture of organic compounds, purely physical methods may be employed. Thus a mixture of volatile liquids may be fractionally distilled (compare Sections 11,15 and 11,17) the degree of separation may be determined by the range of boiling points and/or the refractive indices and densities of the different fractions that are collected. A mixture of non-volatile sohds may frequently be separated by making use of the differences in solubilities in inert solvents the separation is usually controlled by m.p. determinations. Sometimes one of the components of the mixture is volatile and can be separated by sublimation (see Section 11,45). [Pg.1092]

The results in fig. 5.1 show that zeroth-order rates of nitration in solutions of acetyl nitrate in acetic anhydride are much greater than the corresponding rates in solutions in inert organic solvents of nitric acid of the same stoichiometric concentration as that of acetyl nitrate. Thus, for corresponding concentrations of nitric acid and acetyl nitrate, nitration in acetic anhydride is e. 5 x 10 and 10 times faster than nitration in sulpholan and nitromethane respectively. This fact, and the fact that the fraction of free nitric acid in solutions of acetyl nitrate in acetic... [Pg.87]

The system of primary interest, then, is that of a condensable vapor moving between a Hquid phase, usually pure, and a vapor phase in which other components are present. Some of the gas-phase components may be noncondensable. A simple example would be water vapor moving through air to condense on a cold surface. Here the condensed phase, characterized by T and P, exists pure. The vapor-phase description requiresjy, the mole fraction, as weU as T and P. The nomenclature used in the description of vapor-inert gas systems is given in Table 1. [Pg.96]

DAG is treated with ethanol and hydrochloric acid in the presence of inert solvent, eg, chlorinated solvents, hydrocarbons, ketones, etc. The L-ascorbic acid precipitates from the mixture as it forms, minimising its decomposition (69). Cmde L-ascorbic acid is isolated through filtration and purified by recrystallization from water. The pure L-ascorbic acid is isolated, washed with ethanol, and dried. The mother Hquor from the recrystallization step is treated in the usual manner to recover the L-ascorbic acid and ethanol contained in it. The cmde L-ascorbic acid mother Hquor contains solvents and acetone Hberated in the DAG hydrolysis. The solvents are recovered by fractional distillation and recycled. Many solvent systems have been reported for the acid-catalyzed conversion of DAG to L-ascorbic acid (46). Rearrangement solvent systems are used which contain only the necessary amount of water required to give >80% yields of high purity cmde L-ascorbic acid (70). [Pg.17]

On occasion the changes in gas flow and in the mole fraction of inert gas are so small that the inclusion of terms such as (1 — y) a.ndy%M can be neglected or at least can be included in an approximate way. This leads to some of the simplified procedures described later. [Pg.1355]

One such simphfication was suggested by Wiegand [Trans. Am. Jn.st. Chem. Eng., 36, 679 (1940)], who pointed out that the logarithmic-mean mole fraction of inert gas ysM (oi ysM) is often very nearly equal to the arithmetic mean. Thus, substituflon of the relation... [Pg.1355]

Op 1.3808. Fractionate through an efficient column preferably in an inert atmosphere and store in aliquots in sealed tubes [Bieber J Am Chem Soc 74 4700 7952 Slocombe et al. J Am Chem Soc 72 1888 1950],... [Pg.239]


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See also in sourсe #XX -- [ Pg.29 ]




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