Elution, development, procedures

The equivalence of AT and A values makes Eqs. (8-3) and (8-4) directly applicable to elution systems. For thin-layer or other bed development procedures we can derive analogous relationships. Eliminating f(X,S) between Eqs. (6-8) and (8-2a) gives... 

The preceding discussion assumes that the composition of a binary solvent remains effectively constant for either elution or bed,development procedures. As a binary solvent A-B first wets the adsorbent bed, however, ihe stronger solvent component B will be selectively adS Orbbd, leaving the iclvancing solvent front depleted of B. As the solvent trii ates through the bed, this process is repeated until pure A is left in the solvent front. At the same time the adsorbent near the inlet of the bed becomes saturated with B, so that the unadsorbed solvent at this point reverts to its original... 

Factors relative to the quality of a chromatogram, such as preparation of the sorbent layer, development procedure (isocratic or gradient elution), and post-chromatographic derivatization. 

Development of the Chromatogram. The term development describes the process of performing a chromatographic separation. There are several ways in which separation may be made to occur, eg, frontal, displacement, and elution chromatography. Frontal chromatography uses a large quantity of sample and is usually unsuited to analytical procedures. In displacement and elution chromatography, much smaller amounts of material are used. 

The design procedure described above will, in theory, be applicable only to samples that are separated by isocratic development. Under gradient elution conditions the (k ) value of each solute is continually changing, together with the viscosity of the... 

The moist cells were suspended in 750 parts of volume of ethanol and extracted by warming at 60°C for 1 hour. A total of 3 extractions were carried out in a similar manner and the extracts were pooled, diluted with water and further extracted three times with 1,000 parts of volume portions of n-hexane. The n-hexane layer was concentrated to dryness under reduced pressure to recover 4.12 parts of a yellow oil. This oily residue was dissolved in 6 parts by volume of benzene and passed through a column (500 parts by volume capacity) packed with Floridil (100 to 200 meshes). Elution was carried out using benzene and the eluate was collected in 10 parts by volume fractions. Each fraction was analyzed by thin-layer chromatography and color reaction and the fractions rich in ubiquinone-10 were pooled and concentrated under reduced pressure. By this procedure was obtained 0.562 part of a yellow oil. This product was dissolved in 5 parts by volume of chloroform, coated onto a thin layer plate of silica gel GF254 (silica gel with calcium sulfate) and developed with benzene. The fractions corresponding to ubiquinone-10 were extracted, whereby 0.054 part of a yellow oil was obtained. This oil was dissolved in 10 parts by volume of ethanol and allowed to cool, whereupon 0.029 part of yellow crystals of ubiquinone-10 were obtained, its melting point 4B°to 50°C. 

To determine secondary alkanesulfonates in sewage wastewaters, solid phase extraction (SPE) and a single-step procedure which combines elution and injection port derivatization for analysis with GC-MS were developed [36]. Again a tetrabutylammonium ion pair reagent was employed both to elute the secondary alkanesulfonates as their ion pairs from CI8-bonded silica disks and to derivatize sulfonate ion pairs under GC injection port conditions. Secondary alkanesulfonates were effectively recovered from samples of raw sewage (>92%) and from primary (>98%) and secondary (>85%) effluents. No... 

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