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Partial reduction factors

Partial reduction factors that need to be adopted should be provided by the supplier of the geotextile. In the absence of these parameters, the designer can choose default values (which have to be conservative) for each partial reduction factor. [Pg.351]

Combining these equations and integrating yield Cf = CioX for a volume reduction factor X = Q/Qo and the observed component passage Si. This allows one to determine either final concentrations from crossflow rates or the reverse. For a fully retained product (Sj= 0), a 10-fold volume reduction (X = 10) produces a 10-fold more concentrated product. However, if the product is only partially retained, the volume reduction does not proportionately increase the final concentration due to losses through the membrane. [Pg.42]

In synthesis, the principal factors that affect the choice of a reducing agent are selectivity among functional groups (chemoselectivity) and stereoselectivity. Chemo-selectivity can involve two issues. One may wish to effect a partial reduction of a particular functional group or it may be necessary to reduce one group in preference to another,78 In the sections that follow, we consider some synthetically useful partial and selective reductions. [Pg.401]

DAS (11.7) is synthesised from 4-nitrotoluene-2-sulphonic acid (11.6) by the route outlined in Scheme 11.1. An important factor in the preparation of DAST brighteners in the purity necessary for good performance is the purity of the DAS used as starting material. At one time DAS made in this way contained significant amounts of yellow azoxy compounds similar to 11.8, which formed the main components of the obsolescent dye Sun Yellow (Cl Direct Yellow 11) made by the partial reduction and self-condensation of intermediate 11.6. Today the major manufacturers supply DAS essentially free from these undesirable impurities [37]. [Pg.309]

Atteberry and Boyd have separated TcO and ReO on Dowex-2 resin using a mixture of 0.1 M (NH j SO and 0.1 M (NH j SCN as eluent. The two elution peaks are partially resolved, but the cross contamination is rather high. Much better results are obtained if perchlorate is used as the elutriant . Because of some peculiarities of commercial resins, the highest practically attainable separation factors of TcO and ReO are l(f -10 It has been found that the volumes of the eluents consumed in the elution of pertechnetate and perrhenate are inversely proportional to the perchlorate concentration. The separation on Dowex 1-X4 is described in Fig. 6. Partial reduction of TcO or ReO reduces the efficiency of the chromatographic separation since the elution peaks frequently become blurred . [Pg.127]

One of the more difficult partial reductions to accomplish is the conversion of a carboxylic acid derivative to an aldehyde without over-reduction to the alcohol. Aldehydes are inherently more reactive than acids or esters so the challenge is to stop the reduction at the aldehyde stage. Several approaches have been used to achieve this objective. One is to replace some of the hydrogens in a group III hydride with more bulky groups, thus modifying reactivity by steric factors. Lithium tr i - / - b u to x y a I u m i n u m hydride is an example of this approach.42 Sodium tri-t-butoxyaluminum hydride can also be used to reduce acyl chlorides to aldehydes without over-reduction to the alcohol.43 The excellent solubility of sodium bis(2-methoxyethoxy)aluminum hydride makes it a useful reagent for selective... [Pg.267]

An additional contributing factor to the diuresis induced by osmotic diuretics is the increase in renal medullary blood flow that follows their administration. This medullary hyperemia reduces the cortex-meduUary osmolar gradient by carrying away interstitial Na+ and urea. This partial reduction of the osmolar gradient impairs normal reabsorption of tubular water, which occurs from the descending limb of Henle and the collecting duct. [Pg.250]

The results of partial structure factors analysis of reflectivity data relating to DPPC monolayers on a water subphase are shown in Tables 2 through 4. Table 2 summarizes the results gained from fitting experimental data to Eq. 10 pertaining to the DPPC alkyl-chain region of the monolayer. It is apparent that on expansion of the monolayer, both the expected reductions in thickness and the number density of the DPPC chains occur (Table 2). The decrease in thickness (from 20 A to 18 A) is explained by the increased number of gauche conformers introduced into the chains on expansion. The decrease in number density is a function of area per molecule and allows this quantity to be calculated (1/A, = njx). On comparison of these values in Table 2 it can... [Pg.256]

Besides selectivity to aromatic nitriles, the minimization of the direct ammonia oxidation to N2 side-reaction is a critical factor, because otherwise runaway conditions may be possible. There is always competition between NH3 oxidation and ammoxidation on the catalyst surface. Furthermore, contact between ammonia and the catalyst surface, particularly at high temperatures, causes a partial reduction of the oxide surface because of NH3 oxidation to N2. Therefore, control of the rate of unselective oxidation of ammonia to N2 is an important factor in determining the selectivity of the nitrile product, because this side reaction limits the availability of the surface ammonia species that are necessary for nitrile synthesis. [Pg.792]

A quantitative explanation of data based on the two-particle, exchange-coupled model can be attempted only when protons appear in the form of relatively well-isolated pairs, such as in water. The data recorded for partially deuterated water by Chatzidimitriou-Dreismann et al. [Chatzidimitriou-Dreis-mann 1997 (a)] (see Fig. 6) were interpreted by Karlsson [Karlsson 2003 (a)] in terms of reduced pair CS as given in Eq. (7). With a relative deuterium concentration Xn = Ce>/(ch + rr>), the probabilities for forming IIX), />20 and HDO molecules is phh = c2h,pdd = c2D and phd = 2 cr cd, respectively (for Xd = 0.5 one has p2H = 0.25, p2D = 0.25 and 2 ph Pd = 0.50, etc.). With reduction factors Jim for H - H pairs, Jdd for D-D pairs, and Jhd = 1 (no exchange correlation) for H - D pairs, the model predicts the cross section ratio... [Pg.542]

Partial reduction is common, leading to some uncertainty about the composition of the catalyst in the active system. Figure 6.13 shows nickel crystallites in contact with NifAl2]04. which may play some role in the catalytic step. If Ni[ Ab]04 ts not a factor, then better results may be possible by eliminating calcination and reducing the deposited hydroxide or salt directly. [Pg.117]

Sulphur bearing Partial pressure (atm) Exposure Sulphur. uptake Carbon) uptake % Deposition reduction factor ... [Pg.232]


See other pages where Partial reduction factors is mentioned: [Pg.53]    [Pg.351]    [Pg.409]    [Pg.351]    [Pg.409]    [Pg.53]    [Pg.351]    [Pg.409]    [Pg.351]    [Pg.409]    [Pg.121]    [Pg.854]    [Pg.604]    [Pg.854]    [Pg.401]    [Pg.267]    [Pg.240]    [Pg.61]    [Pg.363]    [Pg.223]    [Pg.682]    [Pg.28]    [Pg.124]    [Pg.121]    [Pg.353]    [Pg.241]    [Pg.303]    [Pg.278]    [Pg.717]    [Pg.682]    [Pg.109]    [Pg.458]    [Pg.261]    [Pg.194]    [Pg.984]    [Pg.244]   
See also in sourсe #XX -- [ Pg.351 ]

See also in sourсe #XX -- [ Pg.351 ]




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