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Organic liquids variables

Chloroaluminate(III) ionic liquid systems are perhaps the best established and have been most extensively studied in the development of low-melting organic ionic liquids with particular emphasis on electrochemical and electrodeposition applications, transition metal coordination chemistry, and in applications as liquid Lewis acid catalysts in organic synthesis. Variable and tunable acidity, from basic through neutral to acidic, allows for some very subtle changes in transition metal coordination chemistry. The melting points of [EMIM]C1/A1C13 mixtures can be as low as -90 °C, and the upper liquid limit almost 300 °C [4, 6]. [Pg.43]

These correlations are presumed to include the effect of pressure, because the density group is essentially a pressure factor. The correlations are probably not general, because they omit variables such as surface tension, the type of solid, and the geometric arrangement. Another weakness is that the burnout data for the five organic liquids are estimates (and reported so) by Cichelli and Bonilla (C2). These researchers did not heat their surface to destruction. Thus the accuracy of the maximum q/A values is unknown. [Pg.52]

In this technique, a stream of gas (e.g. He, N2) is used to promote separation of the components of small (pi) volumes of vapours or volatile liquids introduced into one end of a column packed with fine particles of inert solid coated with an organic liquid film (for special applications the packing can be an adsorbent material). The operating conditions are determined by sample type and the variables which can be adjusted include the column packing (e.g. different liquid coating), temperature and gas flow rate. The separated sample components are detected as they emerge from the column after different time intervals. [Pg.19]

Many attempts have been made to synthesise organophosphorus compounds directly from the element with varying degrees of success.i In general mixtures of products are obtained, and the yields are frequently low and variable. The main difficulty is the insolubility of phosphorus in organic liquids and consequently the reactions are heterogeneous with the attendant problems of diffusion and local concentration differences. [Pg.231]

Coefficient JT has been evaluated from plant data and correlated with operating variables such as plate spacing and flow rates. A correlation that includes the effect of surface tension is given below [Eq. 18.65] values of for use with this equation are shown in Fig. 18.28. A value of u = 20 dyn/cm is typical of organic liquids, and the correlation shows that the flooding velocity with such liquids is about 20 percent lower than that for water, for which surface tension or for systems that foam easily ... [Pg.565]

SFE is generally fast, I he rate of mass transfer between a sample matrix and an extraction fluid is determined by the rate of diffusion of a species in the fluid and the viscosity of the fluid — the greater the diffusion rate and (he lower the viscosity, the greater the rate of mass transfer. As we have noted earlier, both of these variables are more favorable for supercritical fluids than for typical liquid solvents. Because of this, SFE can generally be completed in 10 to 60 minutes, whereas extractions with an organic liquid may require several hours or even days,... [Pg.863]

Since the pnbf for a cylindrical test element differs by as much as 20 % in vertical and horizontal orientations [ ], at 1 atm, one cannot be sure that the difference between the curves of Weil and Lacaze, or Roubeau, and these data are not due to geometrical effects, until the effect of this variable is explored at higher pressures. It is evident that Bonilla and Cichelli s recommended curve (based upon a wide variety of organic liquids) cannot be relied upon with an uncertainty of less than 100%. From these data, it seems probable that peak flux approaches zero asymptotically as the critical temperature is approached. [Pg.83]

Inga JR, Morsi BI. (1999) Effect of operating variables on the gas holdup in a large-scale slurry bubble column reactor operating with an organic liquid mixture. Ind. Eng. Chem. Res., 38 928-937. [Pg.498]

Section V on Testing in Environments (H. Hack, Section Editor) includes chapters on outdoor and indoor atmospheres, seawater, fresh water, soils, concrete, industrial waters, industrial chemical, petroleum, high-temperature gases, organic liquids, molten salts, liquid metals, corrosion inhibitors, in-vivo, and microbiological effects. Each chapter provides a descriptive overview of the environment and factors and variables affecting corrosion rates and mechanisms. [Pg.2]


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