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Typically Aqueous Mixtures

The reliable estimation of residual water in dried solids is of importance but is beset by several problems, mainly related to the shape and interpretation of DSC heating traces, as illustrated in Figure 11 for a typical aqueous mixture, maximally frozen, from which any relaxation enthalpy contribution has been removed by annealing." The drawn-out DSC heating trace represents the superposition of several distinct processes Tg of the mixture, the heat of dilution, produced by ice... [Pg.165]

The reflection of inter-solvent attractions in reactivity trends in binary aqueous mixtures has been considered. In the particular case of dissociation of the [Fe(5-NOaphen)3] + cation, as indeed in Bu Cl solvolysis, there is a remarkably good correlation between AG" and G, the excess Gibbs free energy of mixing for the respective solvent mixtures, for the so-called typically aqueous mixtures. These are mixtures with positive G values, and IrA I > and include such commonly studied mixtures as aqueous methanol, ethanol, t-butyl alcohol, acetone, dioxan, and THF. A similar AG /G correlation has been reported for D substitution by cyanide at the [Fe(CN)5(3,5-Me2Py)] anion. ... [Pg.267]

Polymerization takes place, in the following manner in the presence of suitable peroxide catalyst these compounds polymerize with themselves (homopolymerizatiOn) in aqueous emulsion. When the reaction is complete, the emulsified polymer may be used directly or the emulsion coagulated to yield the solid polymer (312). A typical polymerization mixture is total monomer (2-vinylthiazole), 100 sodium stearate, 5 potassium persulfate, 0.3 laurylmercaptan, 0.4 to 0.7 and water, 200 parts. [Pg.397]

Chemistry. Chemical separation is achieved by countercurrent Hquid— Hquid extraction and involves the mass transfer of solutes between an aqueous phase and an immiscible organic phase. In the PUREX process, the organic phase is typically a mixture of 30% by volume tri- -butyl phosphate (solvent) and a normal paraffin hydrocarbon (diluent). The latter is typically dodecane or a high grade kerosene (20). A number of other solvent or diluent systems have been investigated, but none has proved to be a substantial improvement (21). [Pg.204]

Fig. 14 Typical log k/YBr plots for assisted and unassisted alkene brominations. Allylbenzene and 1-pentene, less crowded than cis-methyl-t-butylethylene and methylideneadamantane, exhibit the smallest m-values. The points corresponding to acetic acid (O) and trifluoroethanol (A), two weakly nucleophilic solvents, are below the regression line for water, methanol, ethanol and their aqueous mixtures ( ) of similar nucleophilicity. In contrast, they are on the line for the branched alkenes where steric crowding inhibits nucleophilic assistance by alcoholic solvents (Ruasse et al, 1991, Ruasse and Motallebi, 1991). Fig. 14 Typical log k/YBr plots for assisted and unassisted alkene brominations. Allylbenzene and 1-pentene, less crowded than cis-methyl-t-butylethylene and methylideneadamantane, exhibit the smallest m-values. The points corresponding to acetic acid (O) and trifluoroethanol (A), two weakly nucleophilic solvents, are below the regression line for water, methanol, ethanol and their aqueous mixtures ( ) of similar nucleophilicity. In contrast, they are on the line for the branched alkenes where steric crowding inhibits nucleophilic assistance by alcoholic solvents (Ruasse et al, 1991, Ruasse and Motallebi, 1991).
Like most other metal carboxylates, the calcium carboxylate (Ca(RCOO)2) formed during Equation (6.19) readily forms a soap , the name arising since its aqueous solutions feel slippery and soapy to the touch. The other commonly encountered metal carboxylates are the major components of household soap, which is typically a mixture of potassium stearate and potassium palmitate (the salts of stearic and palmitic acids). [Pg.245]

Reversed-phase separations currently dominate in CEC. As a result, the vast majority of the mobile phases are mixtures of water and an organic solvent, typically acetonitrile or methanol. In addition to the modulation of the retention, the mobile phase in CEC also conducts electricity and must contain mobile ions. This is achieved by using aqueous mixtures of salts instead of pure water. The discussion in Sect. 2 of this chapter indicated that the electro osmotic flow is created by ionized functionalities. The extent of ionization of these functionalities that directly affects the flow rate depends on the pH value of the mobile phase. Therefore, the mobile phase must be buffered to a pH that is desired to achieve the optimal flow velocity. Obviously there are at least three parameters of the mobile phase that have to be controlled (i) percentage of the organic solvent, (ii) the ionic strength of the aqueous component, and (iii) its pH value. [Pg.37]

Two-constant equation of state phase behavior calculations for aqueous mixtures often require the use of temperature dependent binary interaction parameters. The methods used for evaluating these parameters for some of the typical aqueous binary pairs found in coal gasification and related process streams are described. Experimental and predicted phase compositions based on these methods are illustrated for aqueous pairs containing CO2. H2S, NH3, and other gases. [Pg.413]

Irradiation with 7-rays was also used to synthesize bimetallic nanoparticles. Remita et al. synthesized poly(vinyl alcohol) (PVA)-stabilized Ag/Pt bimetallic nanoparticles by radiolysis of an aqueous mixture of Ag2S04 and K2PtCl4 at a concentration of 10-4 mol dm-3. A typical Ag plasmon absorption band is observed at —410 nm with only low intensity at the mole ratio of Ag Pt = 60 40, indicating the formation of Ag/Pt bimetallic nanoparticles. Polyfacrylic acid) was also used as the stabilizer, although the resulting UV-Vis spectra were quite different. [Pg.438]

Note that these single ion values were obtained from entirely different extrathermodynamic assumptions elaborate extrapolation procedure in the case of the water-acetone mixtures, and tetraphenylboron assumption for the water-THF mixture. n-Bu4N+ and Br showed similar behavior in the two binary systems studied this might be the consequence of the similarity between the thermodynamic properties of the two aqueous binaries e.g., both are typically aqueous systems with AHE < T ASE. ... [Pg.318]

Metal-Complex (Formazan) Dyes. The hydrazone from 2-carboxyphenylhydra-zine-4-sulfonic acid and benzaldehyde is suspended in water and then dissolved by adding aqueous sodium hydroxide to obtain pH 6.5 -7.0. This solution is added to the aqueous diazonium salt solution obtained from a typical aqueous diazotiza-tion of 4-(2-sulfooxyethylsulfonyl)-2-aminophenyl-6-sulfonic acid. The mixture is then dripped into an aqueous solution of copper sulfate, while the pH is maintained with soda at 5.5 - 6.5. After complete coupling the pH is adjusted to 1 with concentrated hydrochloric acid. The strongly acidic solution is then neutralized with alkali to pH 5.5. The copper - formazan complex is salted out along with sodium chloride, filtered, washed with dilute aqueous sodium chloride solution, and dried. A dark powder results which gives a dark blue solution in water. It consists of an electrolyte-containing powdered sodium salt of the acid 25 ... [Pg.123]

Another important factor that distinguishes this separation is that it is not environmentally or economically feasible to simply return a rejected stream to the environment, as in a typical aqueous RO process where the brine can be returned to the ocean. The federal regulations mandate that C02 emissions from refineries and chemical plants be reduced to low levels therefore, facilities can no longer afford to dispose of waste hydrocarbon streams in their flare systems. Pure streams from polyolefin reactors and vents from polymer-storage facilities, which were once flared, must be redirected to recovery systems. To reduce the economic penalty of environmental compliance, these paraffin and olefin mixtures must be recovered and recycled. In other words, two products must be made, a useful fuel and a useful chemical product, hence more process engineering is required in order to achieve such an objective. [Pg.150]

The sample matrix may also be modified to enhance extraction recovery. This is typically done by either dissolving a solid sample in a suitable solvent, usually water or a strongly aqueous mixture, or by modifying the pH or salt content of a solution. Modifying the pH to change the extraction behavior works the same way in SPME as it does for classical liquid-liquid extraction. At low pH, acidic compounds will be in the neutral form and will be extracted preferentially into the fiber coating at high pH, basic compounds are extracted favorably. Neutral compounds are not affected appreciably by solution pH. [Pg.207]

Hoegger and Freitag [32] also prepared acrylamide-based monoliths using polymerization in aqueous solutions. However, their typical polymerization mixture contained a much higher concentration of monomers (up to 29%) including piperazine diacrylamide 111 (52% in respect to total monomers), dimethylacrylamide lfi, and 2-acrylamido-2-methyl-l-propanesulfonic acid 6 dissolved in an aqueous phosphate buffer pH 7. [Pg.208]

Typically Non-Aqueous Mixtures with GE Negative (TNAN Mix-... [Pg.204]

The dependence of HE and SE on mole fraction can be complex although the overall effect on the GE -curve is not. The importance of the entropy of mixing warrants the description of such mixtures as typically aqueous (Franks, 1968b). In the following account of the kinetics of reactions in these mixtures, we examine these systems under three headings (i) typically aqueous , TA (ii) typically... [Pg.283]

TYPICALLY NON-AQUEOUS MIXTURES WITH GE NEGATIVE (TNAN MIXTURES)... [Pg.325]

The complexity of biological processes generally requires many stages to produce a final, purified product from a particular composition of raw materials. Although a typical bioprocess consists of two main parts, upstream fermentation and downstream product recovery, it is not unusual to have between 10 and 20 steps in the overall process. This reflects the complex nature of a typical fermentation broth, which will consist of an aqueous mixture of cells, intracellular or extracellular products, unreacted substrates, and by-products of the fermentation process. From this mixture, the desired... [Pg.18]

Hydrothermal bombs containing aqueous mixtures of a metal compound and phosphoric acid are typically heated to temperatures of 100-350 °C, generating autogenous pressures up to 300 bar. The pressure rises more rapidly above the critical temperature of water, 373 °C, and hydrothermal pressures of 3000bar are typically generated at 600-1000 °C in sealed metal tubes surrounded by a supporting pressure of an inert gas. [Pg.3634]


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Aqueous Mixtures

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