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Sodium carbonate, solution tables

Table 6.2 shows the solubilities of common ionic compounds. If an ionic compound is insoluble, then that substance will fall out of (or precipitate from) solution when the appropriate ions are present. For example, if copper) II) sulfate solution is added to sodium carbonate solution. Table 6.2 shows that the combination of copper(II) and carbonate ions forms a precipitate of copper(II) carbonate ... [Pg.85]

With a reactive solvent, the mass-transfer coefficient may be enhanced by a factor E so that, for instance. Kg is replaced by EKg. Like specific rates of ordinary chemical reactions, such enhancements must be found experimentally. There are no generalized correlations. Some calculations have been made for idealized situations, such as complete reaction in the liquid film. Tables 23-6 and 23-7 show a few spot data. On that basis, a tower for absorption of SO9 with NaOH is smaller than that with pure water by a factor of roughly 0.317/7.0 = 0.045. Table 23-8 lists the main factors that are needed for mathematical representation of KgO in a typical case of the absorption of CO9 by aqueous mouethauolamiue. Figure 23-27 shows some of the complex behaviors of equilibria and mass-transfer coefficients for the absorption of CO9 in solutions of potassium carbonate. Other than Henry s law, p = HC, which holds for some fairly dilute solutions, there is no general form of equilibrium relation. A typically complex equation is that for CO9 in contact with sodium carbonate solutions (Harte, Baker, and Purcell, Ind. Eng. Chem., 25, 528 [1933]), which is... [Pg.2106]

Add 1 ml of the ether to 0.1-0.15 g of finely powdered anhydrous zinc chloride and 0.5 g of pure 3,5-dinitrobenzoyl chloride (Section 9.6.4, p. 1241) contained in a test tube attach a small water condenser and reflux gently for 1 hour. Treat the reaction product with 10 ml of 0.75 m sodium carbonate solution, heat and stir the mixture for 1 minute upon a boiling water bath, allow to cool and filter at the pump. Wash the precipitate with 5 ml of 0.75 m sodium carbonate solution and twice with 5 ml of ether. Dry on a porous tile or upon a pad of filter paper. Transfer the crude ester to a test tube and boil it with 10 ml of dichloro-methane filter the hot solution, if necessary. If the ester does not separate on cooling, evaporate to dryness on a water bath, and recrystallise the residue from 2-3 ml of either aqueous ethanol or light petroleum. Determine the melting point of the resulting 3,5-dinitrobenzoate (see Table 10.4). [Pg.1255]

The more water molecules there are, the greater the weight of chemical necessary to provide the same activity in solution. For example, the equivalent of 35.0 grams anhydrous would be 41.0 grams of monohydrate (Conversion Tables Sodium Carbonate Conversion Table). [Pg.24]

Notes to Table V.29 1. If a solution is supplied for analysis, use sufficient to contain 1 0 g of solid material, render it strongly alkaline with saturated sodium carbonate solution and evaporate it down to 10-15 ml. [Pg.447]

The most important industrial example of cation exchange is the preparation of sodium-montmorillonite/bentonite from calcium bentonite. As seen in Table 2.2, calcium ions have greater affinity to the layer charge than sodium ions, so the calcium-sodium cation exchange must be performed in the presence of carbonate ions. It means that calcium-montmorillonite/bentonite is suspended in sodium carbonate solution. Calcium ions precipitate with carbonate ions, so sodium ions can occupy the interlayer space. This process is known as soda activation of bentonite. The disadvantage of soda activation is that sodium-montmorillonite is contaminated with calcium carbonate. [Pg.96]

A similar trend was observed when kaolin was leached for 1 hr. at 250°C with sodium carbonate solutions of different concentrations (Table IV). At the lowest concentration (0.2 M), part of the kaolinite was converted to the sodalite-type natrodavyne while the impurities were untouched. At the highest concentration of sodium carbonate (2.0 M), the kaolinite was converted to the cancrinite-type natrodavyne, and although the quartz was extracted, the illite remained. [Pg.468]

Orthocarhoxylic esters (general procedure) 896 A mixture of a carboximidic ester hydrochloride (0.2 mole) and an alcohol (3 moles) is stirred with careful exclusion of moisture until the salt has dissolved (the reaction vessel is fitted with a reflux condenser and a thermometer). Then anhydrous ether is added in the amount shown in the Table. The ethereal solution is then heated to the b.p. (temperature and duration shown in the Table), after which it is cooled to 0° and filtered from the precipitated ammonium chloride. The filtrate is washed with an equal volume of 10% sodium carbonate solution, then with saturated sodium carbonate solution (50 ml), dried over potassium carbonate, and fractionated at 10-30 mm. [Pg.380]

The stability of nitroglycerine is related to the trace impurity in the nitration process and the reaction temperature [x, 33], especially the impurities of trace metals and alkali metals in the processes of nitration and water-washing. Nitroglycerine obtained at relatively high temperature, before stability treatment in the common approach of washing by water and sodium carbonate solution, contains litde residue acids. The relationship between nitration temperature and stability is shown in Table 5.35. [Pg.238]

TABLE PI. Specific Gravity of Sodium Carbonate Solutions... [Pg.1553]

Green 6N and Palatine Past Red on alkalised silica gel G and alumina G layers, as had been first suggested by Stahl [76]. The slurry was prepared by mixing the adsorbent with 2.6% sodium carbonate solution instead of with water. Solvent 16 (Table 131) is employed for development it must be freshly prepared for each use. Resolution is superior on the alkalised silica gel G layers. The limit of detection is a tenth of that in the PC-procedures so far used. Most of the dyes (acid and substantive) consist of several components of different colours. [Pg.621]

Microstructure and size analyses of the precipitated silica powders were carried out using TEM and dynamic light scattering. The avera particle size, size distribution, and yield of silica powders were affected by reaction time, temperature, and concentrations of surfactant and sodium silicate solutions (Table 2.1). The particle size of silica powders increased with reaction temperature and concentration of sodium silicate, and the yield of silica powders increased with increasing reaction time. The size distribution of silica powders was affected by concentration of surfactant PEG. The optimal preparation conditions were experimentally determined for obtaining the silica powders with nanometer size, narrow size distribution, spherical shape, and high purity without sodium carbonate and surfactant... [Pg.18]

Table E.6A. Dissolution rate of 1050 in sodium carbonate solutions (mm per year) [10]... Table E.6A. Dissolution rate of 1050 in sodium carbonate solutions (mm per year) [10]...
One will undoubtedly notice the little difference between ratios 10.65 and 11.05 pertaining respectively to the sodium carbonate solution, which are not inflatable in bubbles on the opening of a pipe, and to that of rosin soap, which gave a certain diameter. But this still is a consequence of our theory indeed, according to our tables, surface viscosity is less in the second of these liquids than in the first however it follows from the stated remark at the end of 259, that if, with this rather not very energetic surface viscosity, the ratio 11.05 allows the formation of bubbles of poor size, this same ratio, and, with stronger reason, the slightly less ratio 10.65, can better allow it with a more intense surface viscosity. [Pg.245]

Another issue to consider is the thermo-volumetric relationship of the solution. Table 7.7 shows the relationship between temperature and volume of a sodium carbonate solution under controlled experimental conditions. The coefficient of volirme expansion for liqtrids is the ratio of the change in voliune per degree to the... [Pg.174]

Excess calcium hydroxide is precipitated by usiag carbon dioxide and the calcium carbonate, calcium hydroxide, and calcium phosphite are removed by filtration. The filtered solution is treated with an equivalent amount of sodium sulfate or sodium carbonate to precipitate calcium sulfate or carbonate. Sodium hypophosphite monohydrate [10039-56-2] is recovered upon concentration of the solution. Phosphinic acid is produced from the sodium salt by ion exchange (qv). The acid is sold as a 50 wt %, 30—32 wt %, or 10 wt % solution. The 30—32 wt % solution is sold as USP grade (Table 12) (63). Phosphinic acid and its salts are strong reduciag agents, especially ia alkaline solution (65). [Pg.375]

A large number of salts of sahcyhc acid have been prepared and evaluated for therapeutic or other commercial use. Table 7 hsts those most frequently referenced. Sodium sahcylate has analgesic, antiinflammatory, and antipyretic activities and was used extensively in the sixteenth and seventeenth centuries as a remedy, prepared from natural sources, for arthritis and rheumatism. In the 1990s the salt can be obtained directly from Kolbe-Schmitt carboxylation or by the reaction of sahcyhc acid with either aqueous sodium bicarbonate or sodium carbonate. The resulting mixture is heated until effervescence stops the salt is then isolated by filtration and evaporation to dryness at low temperatures. Generally, the solution must be kept slightly acidic so that a white product is obtained if the mixture is basic, a colored product results. The USP product contains 99.5—100.5% NaC H O (anhydrous). The May 1996 price was 8.15/kg (18). [Pg.288]

Brine Preparation. Rock salt and solar salt (see Chemicals frombrine) can be used for preparing sodium chloride solution for electrolysis. These salts contain Ca, Mg, and other impurities that must be removed prior to electrolysis. Otherwise these impurities are deposited on electrodes and increase the energy requirements. The raw brine can be treated by addition of sodium carbonate and hydroxide to reduce calcium and magnesium levels to below 10 ppm. If further reduction in hardness is required, an ion-exchange resin can be used. A typical brine specification for the Huron chlorate ceU design is given in Table 6. [Pg.499]

TABLE 2-25 Partial Pressures of H O over Aqueous Solutions of Sodium Carbonate... [Pg.133]

All chemicals, whether inorganic or organic, are either acidic, basic, or neutral. An example of an inorganic acid is sulfuric acid used in automobile batteries, while the acetic acid found in vinegar is an organic acid. Ammonia found in many household cleaners is a base, as are sodium carbonate and sodium hydroxide (lye). Sodium chloride (common salt) is an example of a salt because it is produced by the neutralization of hydrochloric acid with sodium hydroxide. A solution of table sugar in water is neutral (pH 7) because it does not contain hydrogen ions nor does it react with bases to produce water. [Pg.14]

C17-0033. Determine the concentrations of the ionic species present in a 0.36 M solution of sodium carbonate, Na2 CO3 (see Table 17-2 for K. values). [Pg.1260]

A traditional system for the preparation of table olives, involves a treatment of the fresh fruit with a solution of NaOH to hydrolised the bitter glycoside oleuropein, followed by a lactic fermentation in brine. The modifications that take place on pectic polysaccharides of olives (Manzanilla variety) during this process was smdied. Processing induced a net loss of polysaccharides soluble in sodium carbonate and a paralel accumulation of water and Imidazole/HCl soluble polysaccharides. A general decrease of the apparent molecular weight of water and carbonate soluble polysaccharides was also detected. [Pg.569]

Table 1 lists experimental results from HPWH s original paper [2] in which the dissolution of benzoic acid tablets in aqueous sodium hydroxide solutions was measured gravimetrically. Results from other dissolution experiments in acetate, phosphate, carbonate, and tetraborate buffers, where agreement between theory and experiment were comparable to those listed in Table 1, established this paper and the theoretical HPWH model as the premier reference for dissolution with reaction in pharmaceutics in the 1960s and throughout the 1970s. [Pg.129]

Andreeva and coworkers518 improved on the preparation of Au/a-Fe203 by using a deposition-precipitation method. The preparation involved deposition of Au hydroxide with a solution of sodium carbonate at 60 °C and pH = 8.0 on a fresh precipitate of iron hydroxide. The precipitate was aged for 1 hour at 60 °C, filtered, washed, dried under vacuum at 80 °C, and calcined in air at 400 °C for 2 hours. A comparison of properties and activities is provided in Table 122. The iron oxide crystallites were about 10 nm in both samples investigated. [Pg.261]


See other pages where Sodium carbonate, solution tables is mentioned: [Pg.76]    [Pg.217]    [Pg.161]    [Pg.608]    [Pg.56]    [Pg.208]    [Pg.154]    [Pg.233]    [Pg.140]    [Pg.102]    [Pg.140]    [Pg.605]    [Pg.244]    [Pg.1262]    [Pg.522]    [Pg.13]    [Pg.396]    [Pg.845]    [Pg.16]    [Pg.941]    [Pg.372]    [Pg.396]   
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