Acetone data

Figure 10.12 Light-scattering data in the limit of C2 = 0 plotted according to Eq. (10.89) for cellulose nitrate in acetone. [Data from H. Benoit, A. M. Holtzer, and P. Doty,/. Phys. Chem. 58 635 (1954).]...

FIG. 3.5. Plots of ir/RTc versus concentration (a) various cellulose acetate fractions in acetone (data from A. Bartovics and H. Mark, J. Am. Chem. Soc., 65, 1901 (1943)) and (b) nitrocellulose in three different solvents (data from A. Dobry, J. Chem. Phys., 32, 50 (1935)). 

Fig. 11.3 Enolisation of acetone data from reference [2]. (A) Calculated from the observed data. (B) Calculated from the kinetic parameters omitting the third-order term. The inset graph for a limited concentration range of acid and base shows only small curvature.

Methanol data from Referencell8 acetone data from Reference 41. 

Count each of the samples from step 3-38 for 1 or 2 minutes. 3-42. Plot the counts per minute observed as a function of the acetone volume used. Data from this type of experiment appear in Figure 3-38. 3-43. Repeat steps 3-14, 3-15, and 3-19 for the vials containing 0.0, 0.2, and 1.8 ml of acetone. Data from this type of experiment are depicted in Figure 3-15. 

TABLE 8.1. Optimized Parameters for Acetone Data Modeling... 

Figure 4-17. Reduced radii of gyration as a function of molecular weight for poly(methyl methacrylates) in acetone. Data from Figure 4-16.

Fig. 12. Frequency dispersion ciuve of the scattered inten y changes for nitrobenzene in acetone. Data for 6 = = 90 , X = 436 nm, = 710 V

Table 3 shows results obtained from a five-component, isothermal flash calculation. In this system there are two condensable components (acetone and benzene) and three noncondensable components (hydrogen, carbon monoxide, and methane). Henry s constants for each of the noncondensables were obtained from Equations (18-22) the simplifying assumption for dilute solutions [Equation (17)] was also used for each of the noncondensables. Activity coefficients for both condensable components were calculated with the UNIQUAC equation. For that calculation, all liquid-phase composition variables are on a solute-free basis the only required binary parameters are those for the acetone-benzene system. While no experimental data are available for comparison, the calculated results are probably reliable because all simplifying assumptions are reasonable the... 

Application of the algorithm for analysis of vapor-liquid equilibrium data can be illustrated with the isobaric data of 0th-mer (1928) for the system acetone(1)-methanol(2). For simplicity, the van Laar equations are used here to express the activity coefficients. 

When there is significant random error in all the variables, as in this example, the maximum-likelihood method can lead to better parameter estimates than those obtained by other methods. When Barker s method was used to estimate the van Laar parameters for the acetone-methanol system from these data, it was estimated that = 0.960 and A j = 0.633, compared with A 2 0.857 and A2- = 0.681 using the method of maximum likelihood. Barker s method uses only the P-T-x data and assumes that the T and x measurements are error free. 

Vapor-Liquid Equilibrium Data Reduction for Acetone(1)-Methanol(2) System (Othmer, 1928)... 

For the acetone-methanol data of Othmer, the correlation coefficient is -0.678, indicating a moderate degree of correlation between the two van Laar parameters. The elongated confidence ellipses shown in Figure 2 further emphasize this correlation. 

In all its reactions the lone pair of thiazole is less reactive than that of pyridine. Table 1-61 shows three sets of physicochemical data that illustrate this difference. These are (1) the thermodynamic basicity, which is three orders of magnitude lower for thiazole than for pyridine (2) the enthalpy of reaction with BF3 in nitrobenzene solution, which is 10% lower for thiazole than for pyridine and (3) the specific rate of quaterni-zation by methyl iodide in acetone at 40°C, which is about 50% lower for... 

The following data were collected during a kinetic study of the iodination of acetone by measuring the concentration of unreacted I2 in solution. ... 

Figure 10.12 shows data for cellulose nitrate in acetone measured at Xo = 436 nm, and plotted in the manner suggested in Eq. (10.89). The following example completes the analysis of these data. 

Producers of acetone in the United States and their capacities and feedstocks are given in Table 4 (14). Data on world production and processes by regions are shown in Tables 5 and 6 (15). 

Table 5. World Acetone Production Data by Regions Other Than the United States, 1987 ...

World Capacity, Production, and Consumption. Current and future world capacity, based on aimounced new plants and expansions, and 1987 production and consumption data are shown in Table 7 (38). Consumption of acetone is expected to grow at a rate of about 2% aimually until... 

World consumption data by end use in 1987 are shown in Table 8 (39). Solvent appHcations account for the largest use of acetone worldwide, followed by production of acetone cyanohydrin for conversion to methacrylates. Aldol chemicals are derivatives of acetone used mainly as solvents (40). 

Material Safety Data Sheets (MSDS) issued by suppHers of acetone ate requited to be revised within 90 days to include new permissible exposure limits (PEL). Current OSHA PEL (54) and ACGIH threshold limit values (TLV) (55) ate the same, 750 ppm TWA and 1000 ppm STEL. Eot comparison, the ACGIH TWA values for the common mbbing alcohols are ethyl, 1000, and isopropyl, 400 ppm. A report on human experience (56) concluded that exposure to 1000 ppm for an 8-h day produced no effects other than slight, transient irritation of the eyes, nose, and throat. 

C depending on the reference consulted). Fires may be controlled with carbon dioxide or dry chemical extinguishers. Recommended methods of handlings loadings unloadings and storage can be obtained from Material Safety Data Sheets and inquiries directed to suppHers of acetone. 

E. Graedel, D. T. Hawkins, and L. D. Cld,si.toQ., Atmospheric Chemical Compounds, Academic Press, Odando, Fla., 1986, p. 263, cited in Hazardous Substances Data Bank, Acetone from Toxicology Data Network (TOXNET), National Library of Medicine, Bethesda, Md., Jan. 1990, NATS section in the review. 

Gestodene Gestodene (54), along with norgestimate and desogestrel, are the progestin components of the third-generation oral contraceptives (see Contraceptives). It may be crystallised from hexane/acetone (81) or ethyl acetate (82), and its crystal stmcture (83) and other spectral data have been reported (84). 

LynestrenoL Lynestrenol (73) has been used in oral contraceptives and to treat menstrual disorders. It is converted in vivo to its active metabohte norethindrone (102,103). It can be recrystallized from methanol, and is soluble in ethanol, ether, chloroform, and acetone, and insoluble in water (102). The crystal stmcture (104) and other spectral and analytical data have been reported for lynestrenol (62). 

Megestrol acetate can be recrystakhed from aqueous methanol (108). It is soluble in acetone, chloroform, and ethanol slightly soluble in ether and fixed oils and insoluble in water (107). Additional spectral and physical data have been pubHshed (62). 

Norethindrone may be recrystakhed from ethyl acetate (111). It is soluble in acetone, chloroform, dioxane, ethanol, and pyridine slightly soluble in ether, and insoluble in water (112,113). Its crystal stmcture has been reported (114), and extensive analytical and spectral data have been compiled (115). Norethindrone acetate can be recrystakhed from methylene chloride/hexane (111). It is soluble in acetone, chloroform, dioxane, ethanol, and ether, and insoluble in water (112). Data for identification have been reported (113). The preparation of norethindrone (28) has been described (see Fig. 5). Norethindrone acetate (80) is prepared by the acylation of norethindrone. Norethindrone esters have been described ie, norethindrone, an appropriate acid, and trifiuoroacetic anhydride have been shown to provide a wide variety of norethindrone esters including the acetate (80) and enanthate (81) (116). 

The physical properties of some common ketones are Hsted in Table 1. Ketones are commonly separated by fractional distillation, and vapor—Hquid equihbria and vapor pressure data are readily available for common ketones. A number of other temperature dependent physical properties for acetone, methyl ethyl ketone, methyl isobutyl ketone, and diethyl ketone have been pubHshed (3). 

The Tokuyama Soda single-step catalyst consists of a zirconium phosphate catalyst loaded with 0.1—0.5 wt % paHadium (93—97). Pilot-plant data report (93) that at 140°C, 3 MPa, and a H2 acetone mole ratio of 0.2, the MIBK selectivity is 95% at an acetone conversion of 30%. The reactor product does not contain light methyl substituted methyl pentanes, and allows MIBK recovery in a three-column train with a phase separator between the first and second columns. 

Selected physical properties of various methacrylate esters, amides, and derivatives are given in Tables 1—4. Tables 3 and 4 describe more commercially available methacrylic acid derivatives. A2eotrope data for MMA are shown in Table 5 (8). The solubiUty of MMA in water at 25°C is 1.5%. Water solubiUty of longer alkyl methacrylates ranges from slight to insoluble. Some functionalized esters such as 2-dimethylaniinoethyl methacrylate are miscible and/or hydrolyze. The solubiUty of 2-hydroxypropyl methacrylate in water at 25°C is 13%. Vapor—Hquid equiUbrium (VLE) data have been pubHshed on methanol, methyl methacrylate, and methacrylic acid pairs (9), as have solubiUty data for this ternary system (10). VLE data are also available for methyl methacrylate, methacrylic acid, methyl a-hydroxyisobutyrate, methanol, and water, which are the critical components obtained in the commercially important acetone cyanohydrin route to methyl methacrylate (11). 

Naphthalene is very slightly soluble in water but is appreciably soluble in many organic solvents, eg, 1,2,3,4-tetrahydronaphthalene, phenols, ethers, carbon disulfide, chloroform, ben2ene, coal-tar naphtha, carbon tetrachloride, acetone, and decahydronaphthalene. Selected solubiUty data are presented in Table 4. 

Physical properties of the acid and its anhydride are summarized in Table 1. Other references for more data on specific physical properties of succinic acid are as follows solubiUty in water at 278.15—338.15 K (12) water-enhanced solubiUty in organic solvents (13) dissociation constants in water—acetone (10 vol %) at 30—60°C (14), water—methanol mixtures (10—50 vol %) at 25°C (15,16), water—dioxane mixtures (10—50 vol %) at 25°C (15), and water—dioxane—methanol mixtures at 25°C (17) nucleation and crystal growth (18—20) calculation of the enthalpy of formation using semiempitical methods (21) enthalpy of solution (22,23) and enthalpy of dilution (23). For succinic anhydride, the enthalpies of combustion and sublimation have been reported (24). 

Cyclosporin A forms white prismatic crystals from acetone and is only slightly soluble in water and saturated hydrocarbons, but is very soluble in methanol, ethanol, acetone, and diethyl ether. Optical and nmr data on cyclosporins and x-ray crystallographic data on cyclosporin A and an io do derivative have been reviewed (273,275). 

The outstanding chemical property of cyanohydrins is the ready conversion to a-hydroxy acids and derivatives, especially a-amino and a,P-unsaturated acids. Because cyanohydrins are primarily used as chemical intermediates, data on production and prices are not usually pubUshed. The industrial significance of cyanohydrins is waning as more direct and efficient routes to the desired products are developed. Acetone cyanohydrin is the world s most prominent industrial cyanohydrin because it offers the main route to methyl methacrylate manufacture. 

Table 10 h NMR Spectral Data for Dibenzo Heterocycles (in Acetone)... 

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