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INDEX solution treatment

Fane (1996) proposed an overall water quality index for treatment based on pathogen, turbidity, colour and salt removal. This criterion was modified to suit the study in this project and is presented in Table 8.11. The equation for the water quality parameter (WQP) used in this study, is the sum of the rejections of solute of interest, in this study colloids, organics and cations. For experiments where several colloids, organics and cations were tested, the average is taken (see last equation). [Pg.291]

Unfortunately, none of the commonly used molecular probes is adequate to evaluate column-to-column variabilities [88]. The absolute prediction of retention of any compound involves the use of a rather complex equation [89,90] that necessitates the knowledge of various parameters for both the solute and the solvent [91]. The relative prediction of retention is based on the existence of a calibration line describing the linearity between log and interaction index. This second approach, although less general than the first, is simpler to use in practice, and it often gives more accurate results than the first. With a proper choice of calibration solutes, it is possible to take into account subtle mobile phase effects that cannot be included in the theoretical treatment. [Pg.541]

A thermal treatment at 160°C for 1 hour has proved to be adequate for the removal of aggregates that persist at 145°C in TCB or ODCB solutions of polyethylene. Such a treatment enables one to obtain true solutions for use in SEC. Solution of polyethylene in aCN appears to be incomplete even after the 160 C treatment and aCN is therefore not recommended for use in SEC with polyethylene, despite the favorable specific refractive index Increment of its solutions. [Pg.279]

Continuous Stirred Tank Reactors. Biesenberger (8) solved for the MWD with condensation polymerization in a CSTR, analogous to the treatment Denbigh (14) provided for the other two mechanisms. In this case, the variable residence time distribution leads to an extremely broad MWD with even the maximum weight fraction at the lowest molecular weight (monomer). The dispersion index approaches infinity as the condensation is driven to completion in a stirred tank reactor. A sequential analytical solution of the algebraic equations was obtained with a numerical evaluation of the consecutive equations. [Pg.35]

The advantage of the kinetic treatment lies in the fact that (i) also solutions far from equilibrium can be handled and (ii) the range of validity of Eq. (169) can be given (similarly as in the diffusion case, cf. Section VI.2./). Since in the above derivations bulk defect chemistry was assumed to be established at x = 0, the index bulk was used in Eq. (169) to allow for more general situations. Note that these explicit formulae predict defined dependencies on the control parameters which can be checked provided defect chemistry is known. For simple situations (see Refs.252,253) a power law relationship results ( is a constant)... [Pg.142]

Fig. 7.19 H2O2-UV treatment of pentachloro-phenol in aqueous solution diminution of relative toxicity index (bacterial toxicity established by Toxichromo test using Escherichia coli), of organic chlorine in PCP [Cljorganic =... Fig. 7.19 H2O2-UV treatment of pentachloro-phenol in aqueous solution diminution of relative toxicity index (bacterial toxicity established by Toxichromo test using Escherichia coli), of organic chlorine in PCP [Cljorganic =...
Fig. 7.20 H2O2-UV treatment of the reactive azo dye Remazol Black-B in aqueous solution diminution ofTOC, dye concentration and of relative toxicity index (established by Microtox technique). Conditions [C26H2iN5Na40i9Se] =... Fig. 7.20 H2O2-UV treatment of the reactive azo dye Remazol Black-B in aqueous solution diminution ofTOC, dye concentration and of relative toxicity index (established by Microtox technique). Conditions [C26H2iN5Na40i9Se] =...
Our discussion here explores active connections between the potential distribution theorem (PDT) and the theory of polymer solutions. In Chapter 4 we have already derived the Flory-Huggins model in broad form, and discussed its basis in a van der Waals model of solution thermodynamics. That derivation highlighted the origins of composition, temperature, and pressure effects on the Flory-Huggins interaction parameter. We recall that this theory is based upon a van der Waals treatment of solutions with the additional assumptions of zero volume of mixing and more technical approximations such as Eq. (4.45), p. 81. Considering a system of a polymer (p) of polymerization index M dissolved in a solvent (s), the Rory-Huggins model is... [Pg.173]

Isotherms are normally developed to evaluate the capacity of the carbon for the adsorption of different contaminants. Data are obtained in batch tests, which determine the equilibrium relationship between the compound adsorbed on the carbon and that remaining in solution. The isotherms are used as screening tools to determine which carbon is suitable for a given application. Batch equilibrium tests are often complemented by dynamic column studies to determine system size requirements, contact time, and carbon usage rates [19]. Other parameters that are used to characterize activated carbons for water treatment include phenol number, an index of the ability to remove taste and odor, and molas.ses number, which correlates with the ability to adsorb higher molecular weight substances. However, these parameters still do not reflect performance in service, and they can only be considered as guidelines. [Pg.37]


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See also in sourсe #XX -- [ Pg.188 ]




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INDEX solution

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