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Chemical separation three-column

In chemical analysis, chromatography may permit the separation of more than a hundred components from a mixture in a single run. Explain why chromatography can provide such a large separating power. In production chromatography, the complete separation of a mixture containing more than a few components is likely to involve two or three columns for optimum economic performance. Why is this ... [Pg.247]

Flavonol isomers, which differ only in the position of hydroxyl group on their chemical structures, showed different chromatographic behaviors. Liu et al. separated three flavonol isomers (3-hydroxyflavone, 6-hydroxy-flavone, and 7-hydroxyflavone) by a lab-constmcted packed column SFC system with carbon dioxide modified with ethanol containing 0.5% (V/V) phosphoric acid as the mobile phase. The effects of temperature, pressure, composition of mobile phase, and packed-column type on... [Pg.687]

Parameterization When having separated general from specific aspects, the parameterization aspect can be addressed. How to adapt a model to a specific context (company), to a specific chemical process, to a specific subdomain of chemical engineering etc. Parameterization is handled within the three columns but not by a general mechanism. [Pg.602]

Many separations which would be difficult to achieve by conventional distillation processes may be effected by a distillation process in which a solvent is introduced which reacts chemically with one or more of the components to be separated. Three methods are presented for solving problems of this type. In Sec. 8-1, the 0 method of convergence is applied to conventional and complex distillation columns. In Sec. 8-2, the 2N Newton-Raphson method is applied to absorbers and distillation columns in which one or more chemical reactions occur per stage. The first two methods are recommended for mixtures which do not deviate too widely from ideal solutions. For mixtures which form highly nonideal solutions and one or more chemical reactions occur per stage, a formulation of the Almost Band Algorithm such as the one presented in Sec. 8-3 is recommended. [Pg.275]

Flavonol isomers, which differ only in the position of hydroxyl group on their chemical structures, showed different chromatographic behaviors. Liu et al. ° separated three flavonol isomers (3-hydroxyflavone, 6-hydro-xyflavone, and 7-hydroxyflavone) by a lab-constructed packed column SFC system with carbon dioxide modified with ethanol containing 0.5% (VAO phosphoric acid as the mobile phase. The effects of temperature, pressure, composition of mobile phase, and packed-column type on the separation were studied. It was indicated that the addition of phosphoric acid to the mobile phase enabled flavonol isomers to be eluted from the column. It was also shown that a phenyl-bonded silica column was better and the ODS column was not as effective for the isomer separation. Increasing pressure shortened the retention time of each compound, with good resolution, and higher temperature led to longer retention times, and even the loss of the bioactivities of these components. Under selected conditions, the separation of these isomers was very satisfactory, as illustrated in Fig. 2. [Pg.892]

Systems analogous to solvent extraction. A more satisfactory continuous system from the viewpoint of resin utilization would be based upon the counter-current principle as employed so successfully in liquid-liquid extraction processes. Hutcheon describes a three-column system of this type (Fig. 3.6) for separating two components A and B, independent of the type of plant in which it would be operated. The resin passes down column I and then down column II in counter-current flow with two aqueous solutions. The main one of these is the feed solution which enters at the base of column I, but it is mixed with the scrub solution or stripping solution which has passed up column II, again in counter-current flow to the resin. As in a solvent extraction process, chemical compositions of the two solutions are adjusted so that Ea> 1 and <1, where Ea and Eb are the extraction factors applicable in a solvent extraction process, i.e. [Pg.93]

All parts in contact with solutions are made of inert materials. The chemical separation section is symmetrical and operated in an alternating mode between left and right. Simultaneously three operations are performed activity from the gas-jet (Stender et al. 1980) is collected on a polyethylene frit, previously collected activity is dissolved and transported to a column for chemical separation on one side, and the next colurtm is washed and conditioned on the other side. The products of interest are eluted from the columns onto preheated tantalum or titanium disks and the eluent is evaporated. After flaming and cooling, the disk is placed in the measuring position. Typical times from the end of irradiation to the start of measurements are 50 s, which makes it possible to study nuclides with a half-life down to 10—15 s. [Pg.2412]

Avet an, V. S., Petlyuk, F. B., Serafimov, L. A. (1973). Optimal Design Three-Columns of Separation Unit of Lowest Carbon Acids with Water. In The Optimal Design in Refining and Chemical Industry. 3, pp. 127-137. Moscow VNIPIneft (Rus.). [Pg.320]

Basically, gas chromatography separates chemicals in vapor based on each chemical s distinct distribution coefficient between the stationary and mobile phases. A column containing the stationary phase is the heart of the technique, and the carrier gas (mobile phase) is used to carry the chemicals through the column. (A complete discussion of gas chromatography is beyond the scope of this book. Numerous excellent publications on gas chromatography are available, and we have included three references in the bibliography at the end of the book.)... [Pg.140]

Figure 11.1 The direct and indirect sequences of simple distillation columns for a three-product separation (From Smith R and Linnhoff B, 1998, Trans IChemE ChERD, 66, 195, reproduced by permission of the Institution of Chemical Engineers.)... Figure 11.1 The direct and indirect sequences of simple distillation columns for a three-product separation (From Smith R and Linnhoff B, 1998, Trans IChemE ChERD, 66, 195, reproduced by permission of the Institution of Chemical Engineers.)...

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