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Flush composition

The rhodium catalyst (46 mg) is dissolved in acetone (10 ml) in a microhydrogenation apparatus which is then flushed three times with deuterium gas. After stirring the solution in an atmosphere of deuterium for about 1 hr the deuterium uptake ceases and constant pressure is attained. 5a-Cholest-2-ene (136, 19.5 mg) is added and the stirring continued until deuterium uptake ceases (about 3/4 hr). The solvent is evaporated to dryness and the residue is extracted with hexane and the resulting solution filtered through a small alumina column (3 g, activity 111). Evaporation of the hexane gives 2, 3 -d2-5oc-cholestane (137) 18 mg, 92% mp 78-79° isotope composition 94%d2,5%d, andl%do. ... [Pg.188]

If hot water and W ater vapor at 175°F are used to flush mixture A from the tank, the mixture composition can only shift along AC to E. Mixtures between A and E are flushed from the tank, mixed with air to give a mixture between parts AE and B. After examining several other... [Pg.491]

Figures 33.3-33.4 show the results at the end of the simulation, after groundwater composition and microbial activity across the aquifer have approached steady state. Once the sulfate initially present is consumed or flushed from the aquifer, the only source of sulfate is in the recharging groundwater. With time in the simulation, sulfate reducing bacteria grow into a community that consumes sulfate from the recharging groundwater and some of the acetate diffusing into the aquifer the acetate and sulfate are consumed in equal molar proportions, according to Reac-... Figures 33.3-33.4 show the results at the end of the simulation, after groundwater composition and microbial activity across the aquifer have approached steady state. Once the sulfate initially present is consumed or flushed from the aquifer, the only source of sulfate is in the recharging groundwater. With time in the simulation, sulfate reducing bacteria grow into a community that consumes sulfate from the recharging groundwater and some of the acetate diffusing into the aquifer the acetate and sulfate are consumed in equal molar proportions, according to Reac-...
Early tests of the SCWO reactors (discussed below) indicated significant corrosion and plugging. Plugging problems were solved by procedural modifications that include periodic flushing with clean water at slightly subcritical conditions. The corrosion is mitigated by inserting various composite liners that resist the corrosivity of the different feed streams. [Pg.126]

Red clover is a plant that contains isoflavones in a slightly different composition compared with soy. Red clover contains formononetin and biochanin A, which are not present in soy and may thus have additional biological activity. So far, four studies (Barber et ah, 1999 Knight et ah, 1999 van de Weijer, 2002 Tice et ah, 2003) have been performed using isoflavones derived from red clover (Table 4.3). These have used doses of isoflavones ranging from 40 to 160 mg. Three out of four of these studies did not show any effects, even in spite of a very large sample size (Tice et ah, 2003). Only one study showed a reduction in the number of hot flushes. The reduction, however, was small (van de Weijer and Barentsen, 2002). Red clover therefore does not appear to have much of an effect on the reduction of hot flushes. [Pg.96]

The third desorbent characteristic is that the desorbent material must be easily separated from the two Sorbex process products extract and raffinate. The adsorbent chamber s composition profile produces extract and raffinate streams comin-gled with desorbent. In order for the process to be economical, the separation of the feed components from the desorbent (achieved through fractionation) is set by the boiling point differences between the species. Depending on the selectivity possessed by the desorbent over that of the feed normals, the subsequent desorbent rates needed to flush feed normal paraffins from the adsorbent s selective volume and the resulting extract or raffinate streams from the Sorbex chambers could contain in some cases more than 50% desorbent. High concentration of desorbent demonstrates the importance of the desorbent characteristics when selecting a desorbent. [Pg.254]

B. Oxidation procedure for the small-scale experiments. The required amounts of hexan-l-ol, AA-TEMPO, Mg(N03)2, NBS and HOAc were loaded in the reactor and the flask was connected to the volumetric manifold. The flask was flushed three times with oxygen and immersed in the thermostated water bath held at the reaction temperature for two minutes to equilibrate the system. The oxygen was admitted to the reaction pressure and the continuous monitoring of the oxygen uptake initiated and recorded against the time. After the reaction was completed the product composition was analyzed by GC using dioxane as an internal standard. [Pg.129]

Other researchers attempted improved control of product stoichiometry by wrapping reactant-mixture pellets (Tl2Os, BaO, CaO, and CuO) in gold foil and then sealing them in silica ampoules that had been flushed with oxygen (8)(51). Multiphase samples, however, were still obtained. Nominal starting metal compositions of 1 1 3 3 and 2 2 2 3 (Tl Ba Ca Cu) resulted in the largest amounts of 2223 and 2212 phases, respectively the samples... [Pg.275]


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See also in sourсe #XX -- [ Pg.5 , Pg.224 ]




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