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Solubility parameter of solvent

The overall sorption value tends to decrease with the addition of the nanoclays. The decrease is maximum for the unmodified-clay-fiUed sample. As the ternperamre of swelling increases, the penetrant uptake increases in all the systems (Table 2.5). The rate of increase of solvent uptake is slower for the unmodified-clay-filled sample compared to the modified one. From Table 2.5 it can be seen that the values are higher for THE compared to MEK in every composite system. The higher sorption can be explained from the difference in solubility parameter of solvent and rubber (9 — 99 and polarity. The solubility parameter value of MEK, THE, and the mbber is 19.8, 18.6, and 14.8 MPa, respectively. This difference is lower (3.8 MPa ) in the case of THE than that of MEK (5.0 MPa ). [Pg.41]

Absorption rates of carbon dioxide were measured in organic solutions of glycidyl methacrylate at 101.3 kPa to obtain the reaction kinetics between carbon dioxide and glycidyl methacrylate using tricaprylylmethylammonium chloride(Aliquat 336) as catalysts. The reaction rate constants were estimated by the mass transfer mechanism accompanied by the pseudo-first-order fast reaction. An empirical correlation between the reaction rate constants and the solubility parameters of solvents, such as toluene, A-methyl-2-pirrolidinone, and dimethyl sulfoxide was presented. [Pg.345]

The overall reaction between CO2 and GMA was assumed to consist of two elementary reactions such as a reversible reaction of GMA and catalyst to form an intermediate and an irreversible reaction of this intermediate and carbon dioxide to form five-membered cyclic carbonate. Absorption data for CO2 in the solution at 101.3 N/m were interpreted to obtain pseudo-first-order reaction rate constant, which was used to obtain the elementary reaction rate constants. The effects of the solubility parameter of solvent on lc2/k and IC3 were explained using the solvent polarity. [Pg.348]

Fig.2. Relationship between reaction rate constant and solubility parameter of solvent in the reaction of CO2 with GMA using Aliquat 336 at 85 C. Fig.2. Relationship between reaction rate constant and solubility parameter of solvent in the reaction of CO2 with GMA using Aliquat 336 at 85 C.
The use of the solubility envelope, together with the volumetric additivity rule for calculating solubility parameters of solvent blend and the solvent evaporation model described previously, allows an approximate assessment whether phase separation will take place or not during solvent evaporation. [Pg.174]

Figure 19 Plot of calculated solubilities versus solubility parameter of solvents. Figure 19 Plot of calculated solubilities versus solubility parameter of solvents.
The structural constraints used in the first case study namely, Eqn s 27,28 and 29 are used again. The melting point, boiling point and flash point, are used as constraints for both solvent and anti-solvent. Since the solvent needs to have high solubility for solute and the anti-solvent needs to have low solubility for the solute limits of 17 <8 < 19 and 5 > 30 (Eqn s. 33 and 37) are placed on the solubility parameters of solvent and anti-solvents respectively. Eqn.38 gives the necessary condition for phase stability (Bernard et al., 1967), which needs to be satisfied for the solvent-anti solvent pairs to be miscible with each other. Eqn. 39 gives the solid-liquid equilibrium constraint. [Pg.140]

Finally, the solubility parameter of the adhesive and the substrate must be close. Without getting too teehnieal, the solubility parameter is a rough estimate of polarity. The old saying like dissolves like can be extended to like bonds like. More aeeurately, the solubility parameter is the ealeulated potential energy of 1 em of material for eommon solvents. Polymers are assigned solubility parameters of solvents in which they are soluble. Table 19.3 lists solubility parameters for various solvents and polymers. As an example of how to use this table, butadiene-acrylonitrile rubber with 6= 9.5 bonds natural rubber (6= V.9-8.3) to phenolic plastics (6= 11.5). Note that its solubility parameter is between that of the two substrates. [Pg.357]

Fig. 4. Solubility of gases. log. 2 at 25cC and I atm versus square of solubility parameter of solvents... Fig. 4. Solubility of gases. log. 2 at 25cC and I atm versus square of solubility parameter of solvents...
Fig. 15. Aggregation numbers of barium dinonylnaphtalene sulfonate versus solubility parameter of solvents. [J. Phys, Chem. 74, 1817 (1970)]... Fig. 15. Aggregation numbers of barium dinonylnaphtalene sulfonate versus solubility parameter of solvents. [J. Phys, Chem. 74, 1817 (1970)]...
It follows from Eq. (7.12) that only positive values of y are permitted, whereas it was mentioned above that the criterion for complete solvent-polymer miscibility is yn < 0.5. The conclusion is that the difference in solubility parameters of solvent and polymer must be small. If we assume that Vs 80 cm3/mol = 0.8 x 10-4 m3/mol, then at room temperature, the maximum value of l<5p-<5sl would be 4 (MJ/m3)1/2 = 2 (cal/cm3)1/2. This number, of course, depends strongly on the liquid molar volume. [Pg.203]

There are many sources of data for the solubility parameters of solvents and polymers. Daubert and Danner (1990) have compiled accurate solubility parameters for over 1250 industrially important low molecular weight compounds. Barton (1983, 1990) has tabulated solubility parameters for most of the industrially important polymers. [Pg.10]

A more convenient procedure relies on calculations of S values rather than experimental assessments. Solubility parameters of solvents can be correlated... [Pg.449]

The method of DiPaola-Baranyi and Guillet is an extension of the work of Bristow and Watson [21] who calculated solubility parameters for a series of network polymers from swelling equilibria. The basis is that the solubility parameters of solvent, 61, and polymer, 2) are introduced in the form of Regular Solution theory [19] to account for enthalpic effects ... [Pg.49]

Figure 22. Conductivity ratio (k/k ) of Nafion vs. solubility parameter of solvents. (Ref. 179 reprinted by permission of the publisher. The Electrochemical Society, Inc.)... Figure 22. Conductivity ratio (k/k ) of Nafion vs. solubility parameter of solvents. (Ref. 179 reprinted by permission of the publisher. The Electrochemical Society, Inc.)...
Solubility parameters of solvents can be correlated with the structure, molecular weight, and density of the solvent molecule. According to the additive method of Small [15], the solubility parameter is calculated from a set of additive constants, F, called molar attraction constants, by the relationship. ... [Pg.200]

Figure 1. Solvent uptake of Nafion 120 vs. solubility parameters of solvents (3). Figure 1. Solvent uptake of Nafion 120 vs. solubility parameters of solvents (3).
Figure 7. Upper part conductivity ratio (vm/ve) of Nafion in solvent + 0.05 N LiOH vs. solubility parameter of solvent. aM, membrane conductivity Figure 7. Upper part conductivity ratio (vm/ve) of Nafion in solvent + 0.05 N LiOH vs. solubility parameter of solvent. aM, membrane conductivity <te, electrolyte conductivity. Lower part solvent uptake of Nafion-Li vs. solubility parameter...
Reduced viscosity of several alkyd resins as a function of solvent power (solubility parameter) of solvent at concentration of 40 g/tnL. Copyright 1957 Federal Society of Paint Technology. [Pg.677]

The energy of vaporization is not accessible for polymers, but cohesive energy density of polymers can be determined from PVT-data. However, common ways for determining polymer solubility parameters use thermodynamic properties of polymer solutions and their relations to excess enthalpy or excess Gibbs energy per unit volume. These excess quantities are related to the (square) difference between the solubility parameters of solvents and polymers, i.e. (d -... [Pg.2258]

Achieving a suitable particle size with better yield is important in precipitation polymerization as many parameters affect its mechanism. We have prepared GA based MIPs by the precipitation polymerization and observed the effect of porogen on particle size and specific molecular recognition properties (Pardeshi et al, 2014], MIP, M-lOO prepared in the porogen acetonitrile and MIP, M-75 prepared in a mixture of acetonitrile-toluene (75 25 v/v), resulted in the formation of microspheres with approximately 4 pm particle size and surface area of 96.73 m g and nanoparticles (0.8-1000 nm] and a surface area of 345.9 m g" respectively. The results have shown that effect of toluene on the particle size of MIPs depends on the type of cross-linker used and its solubility parameter. Matching the solubility parameter of solvent mixture and cross-linkers is important to obtain the desired particle size in MIPs. The MIPs selectively recognized GA in presence of its structural analogues. Pure GA with percent recovery of 75 ( 1.6) and 83.4 ( 2.2) was obtained from the aqueous extract of herb Emblica officinalis by M-lOO and M-75, respectively. [Pg.637]


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