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Closed aqueous system

The slopes for the other lines are obtained in the same way. Approximating the charge balance expression (3.62) by H" HC03 gives the equilibrium pH for a closed aqueous system containing carbonic acid. [Pg.103]

Example 4.8. pH Change Resulting from Photosynthetic CO2 Assimilation As a result of photosynthesis with NOs assimilation, a surface water with an alkalinity of 8.5 X 10 eq liter" showed within a 3-h period a pH variation from 9.0 to 9.5. What is the rate of net CO2 fixation [Assume a closed aqueous system, that is, no exchange of CO2 with the atmosphere and no deposition of CaC03 (25°C), pATi = 6.3, pK2 = 10.2.]... [Pg.174]

Figure 4.17. Computed concentrations of C02(aq) and HCOf as a function of time for the reversible reaction C02(aq) + H2O = HCO + at 25 C in a closed aqueous system. The total concentration, Cj = [C02(aq)] + [HCOf ], is 1 x 10 M. C02(aq) is assumed to be nonvolatile, (b) Computed velocities, t fonvanJ> t backwam. and in ibe reaction mixture as a function of time for C02 Figure 4.17. Computed concentrations of C02(aq) and HCOf as a function of time for the reversible reaction C02(aq) + H2O = HCO + at 25 C in a closed aqueous system. The total concentration, Cj = [C02(aq)] + [HCOf ], is 1 x 10 M. C02(aq) is assumed to be nonvolatile, (b) Computed velocities, t fonvanJ> t backwam. and in ibe reaction mixture as a function of time for C02<aq) + H2O = HCOj" + H. At equilibrium, the velocity in both directions is 0.24 s V...
Dissolution kinetics of a simple component close to saturation and the mechanism of the backward precipitation reaction are still subject to controversy. Minerals such as calcite and aragonite are known to reach rapidly a dissolution equilibrium when placed in closed aqueous systems. According to simple and classical thermodynamical concepts, this requires that each forward... [Pg.443]

The use of non-aqueous media offered new attractive possibilities for the analysis of hydrophobic compounds, which are often difficult to be analyzed due to their low solubility in aqueous media. Selectivities that are difficult to be obtained in aqueous buffers can be easily obtained using non-aqueous systems, due to larger differences in the ionized—unionized equilibrium for two closely related substances in non-aqueous solvents compared to aqueous solvents. Organic solvents such as methanol, ACN, ethanol, formamide, dimethyl formamide. [Pg.279]

In many cases only one of the enantiomers displays the desired biological effect, the other is ineffective or even harmful. The development of enantioselective catalysis in non-aqueous solvents has been closely followed by the studies of similar aqueous systems - logically, attempts were made in order to solubilize the ligands and catalysts in aqueous media. Using aqueous/organic biphasic systems (often water/ethyl acetate) one may have a possibility of recovery and recycle of the often elaborate and expensive catalysts. However, with a few exceptions, up till now catalyst recovery has been rather a desire than a subject of intensive studies, obviously because of the lack of large-scale synthetic processes. [Pg.75]

Oscarson DW, Huang PM, Liaw WK, Hammer UT (1983) Kinetics of oxidation of arsenite by various manganese dioxides. Soil Sci Soc Am J 47 644-648 Pang LP, Close M, Flintoft M (2005) Degradation and sorption of atrazine, hexazinone and pro-cymidone in coastal sand aquifer media. Pest Man Sci 61 133-143 Paris DF, Lewis DL (1976) Accumulation of metoxychlor by microorganisms isolated from aqueous systems. BuU Environ Contam Toxicol 13 443-450 Parr JF, Smith S (1976) Degradation of toxaphene in selected anaerobic soil environments. Soil Science 121 52-57... [Pg.406]

A number of observations help to understand the mechanism of hematite formation from ferrihydrite in aqueous systems i. e. under conditions essentially different from those for solid-state transformation by dry heating (see 14.2.6). Air-dry storage of ferrihydrite containing 100-150g H20/kg of water (found by weight loss) at room temperature for 20.4 years in closed vessels led to partial transformation to fairly well crystalline hematite with a little goethite (Schwertmann et al., 1999). In contrast, no hematite was formed from ferrihydrite if the content of adsorbed water was substantially reduced (Stanjek and Weidler, 1992 Weidler, 1997) as seen from the following examples ... [Pg.391]

Figure 6-12 compares calculated acidities for carboxylic acids (relative to the acidity of acetic acid) to experimental aqueous-phase pKa s. The overall correlation is good, and suggests a high level of cancellation of solvent effects in these closely-related systems. [Pg.247]

The elements of this group (zinc Zn, cadmium Cd, mercury Hg) all exhibit a II oxidation state in aqueous systems, and Hg also shows a I oxidation state as indicated by the unusual cation Hg2. None of the elements shows oxidation states greater than II, which indicates that the d electrons are not involved. Within the group Zn and Cd resemble each other more closely than Cd and Hg. This is especially evident in the nobility of Hg (E° positive for Zn and Cd, negative for Hg), the lack of an Hg hydroxide, the thermal instability of HgO, and the greater stabilities of many Hg complexes as compared to those of Zn and Cd. [Pg.383]

The physical chemical behavior of betaine esters of long-chain alcohols shows strong similarities to the common, closely related alkyltrimethylam-monium surfactants both in dilute and concentrated aqueous systems, hi consistence with the findings about CMC s of surfactants containing normal ester bonds (see above) it has been found that the CMC for a betaine ester with a hydrocarbon chain of n carbons is very close to the value for an alkyltrimethylammonium chloride surfactant with a hydrocarbon chain of n + 2 carbons [32], The binary phase diagram of dodecyl betainate-water has an appearance very similar to that of an alkyltrimethylammonium surfactant with a hydrophobic tail of a similar size [30]. [Pg.71]

Figure 3.3-3 Distribution ratios for (closed symbol) and Cs (open symbol) with dibenzo-18-crown-6 (0.1 m) as extractant in IL/aqueous systems ([BMIM][PF6] ( ), [HMIM][PFd ( ), [OMIM][PFe] ( )) as a function of increasing aqueous phase concentrations of [AI(N03)3] (m). From reference [7]. Figure 3.3-3 Distribution ratios for (closed symbol) and Cs (open symbol) with dibenzo-18-crown-6 (0.1 m) as extractant in IL/aqueous systems ([BMIM][PF6] ( ), [HMIM][PFd ( ), [OMIM][PFe] ( )) as a function of increasing aqueous phase concentrations of [AI(N03)3] (m). From reference [7].
The most popular method for measuring the polarity of a solute entails determination of the distribution constant between water and a water-immiscible solvent, e.g., octanol. However, because there is difficulty in dissolving proteins in the solvent, a two-phase aqueous system was developed (Shanbhag and Axelson, 1975). Albertson (1986) reported the construction of various aqueous phase systems for partitioning proteins, other macromolecules, and even cells. Recently, simpler aqueous biphase systems were selected for hydrophobic partitioning of proteins (Hachem et al., 1996). However, because of restrictions similar to those for HIC, as discussed above, it may be premature to replace the method used in Basic Protocol 5. The definition of hydrophobicity is based on the polarity of chemical compounds, which is closely related to the distribution between solvents of different polarities. This theory is similar to the elution mechanism of phase distribution chromatography as well as phase partition. However, complexity in the partition system and procedure hampers the broad use of the phase partition approaches. [Pg.310]

The need to abstract from the considerable complexity of real natural water systems and substitute an idealized situation is met perhaps most simply by the concept of chemical equilibrium in a closed model system. Figure 2 outlines the main features of a generalized model for the thermodynamic description of a natural water system. The model is a closed system at constant temperature and pressure, the system consisting of a gas phase, aqueous solution phase, and some specified number of solid phases of defined compositions. For a thermodynamic description, information about activities is required therefore, the model indicates, along with concentrations and pressures, activity coefficients, fiy for the various composition variables of the system. There are a number of approaches to the problem of relating activity and concentrations, but these need not be examined here (see, e.g., Ref. 11). [Pg.14]

The separated compounds from the reaction mixture, reference compounds, and paper blanks were cut from the developed chromatograms, and the aqueous eluates were received in volumetric flasks under a closed glass system. [Pg.108]


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Aqueous systems

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