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Normal saturation

Flotation Air flotation has proved to be successful in concentrating secondaiy sludges to about 4 percent solids. The incoming solids are normally saturated with air at 275 to 350 kPa (40 to 50 psig) prior to being released in the flotation tank. As the air comes out of solution, the fine bubbles are trapped under the suspended solids and cany... [Pg.2228]

Tyrosine is converted to dopa by the cytoplasmic enzyme tyrosine hydroxylase. This is the rate-limiting step 5 x 10 M) in DA synthesis, it requires molecular O2 and Fe + as well as tetrahydropterine (BH-4) cofactor and is substrate-specific. It can be inhibited by a-methyl-p-tyrosine, which depletes the brain of both DA and NA and it is particularly important for the maintenance of DA synthesis. Since the levels of tyrosine are above the for tyrosine hydroxylase the enzyme is normally saturated and so it is not possible to increase DA levels by giving tyrosine. [Pg.141]

Sometimes it may become necessary to shut-in a gas well when the demand for gas is low. In such instances, the well is shut-in for an indefinite period, after which it is reopened and production is resumed. It often has been found that the production rate of gas from the reopened well is substantially less than it was before the well was shut-in. During production, the inner wall of the production tubing will be coated with a film of condensed freshwater because of the geothermal gradient. This water flows down when production is interrupted and can cause formation damage. This may occur because clays are normally saturated with brine water and not with freshwater. This swelling can be prevented with the injection of some additive, for example, sodium chloride, potassium chloride, calcium chloride, or an alcohol or a similar organic material [1853]. [Pg.63]

Fig. 4.2. The effect of chain length (li) on the degree of hydrolysis [%] of primary amides by rat liver preparations (5 h at pH 7.4). Black bars amides of normal saturated fatty acids hatched bar isohexanamide unshaded bars amides of m-phenyl-substituted saturated fatty... Fig. 4.2. The effect of chain length (li) on the degree of hydrolysis [%] of primary amides by rat liver preparations (5 h at pH 7.4). Black bars amides of normal saturated fatty acids hatched bar isohexanamide unshaded bars amides of m-phenyl-substituted saturated fatty...
Table 2 Transferability of intra- and inter-pair correlation energy contributions in some normal saturated hydrocarbons for a CH-bond at the end of the molecules and between two neighboring CH-bonds. respectively)... Table 2 Transferability of intra- and inter-pair correlation energy contributions in some normal saturated hydrocarbons for a CH-bond at the end of the molecules and between two neighboring CH-bonds. respectively)...
The application of the LMBPT on the ab initio level to some normal saturated hydrocarbons was first performed using STO-3G basis set (Kapuy et al., 1987). Similar calculations have been carried out by the use of MINI basis set. The transferability of some correlation energy contributions in systems CHa, CsH 2 and CiHie,... [Pg.50]

Noteworthy is the behaviour of some dyes, for example indanthrone dyes, which become opaque with high-power laser irradiation in contrast to the normal saturation of absorption discussed above 15>. It could be shown that in these cases photochemical processes are operative, creating species which exhibit a higher absorption coefficient at the laser wavelength 18>. [Pg.11]

TABLE 7.1 IUPAC and Common Names for a Variety of Normal Saturated and Unsaturated Surface Active Compounds... [Pg.302]

Supersaturation.—One of the most frequent difficulties in crystallization is due to super saturation. This condition arises when the normal saturation concentration of a salt solution is exceeded without the appearance of any crystals, and as the solution cools further it becomes steadily more supersaturated. When crystallization finally starts, it proceeds with great rapidity, forming a mass of poorly defined crystals unsuited to drying. The tendency toward supersaturation is most marked in the case of very soluble substances which form viscous or syrupy solutions. Lead acetate, sodium thiosulfate, ferric nitrate, and sulfuric acid are good examples. [Pg.16]

The word wet in wet gas does not mean that the gas is wet with water but refers to the hydrocarbon liquid which condenses at surface conditions. In fact, reservoir gas is normally saturated with water. [Pg.156]

Under quiescent conditions a concentration substantially in excess of normal solubility or a temperature lower than the normal saturation temperature can be maintained. The maximum supersaturation appears to be a fairly reproducible quantity, but is reduced or even eliminated by stirring or by the introduction of dust or seed crystals. Some data are shown in Figure 16.1(c) and in Table 16.1. They are expressed as AC = C — Csat or as AC/Csat or as AT=T- Fsat. According to the data of Table 16.1(d), subcooling correlates roughly with the heat of solution. The increments AC and AT can be quite substantial quantities. [Pg.523]

For the structural analysis of cyclic fatty acid derivatives (polymerized drying oils, copolymerization products of fatty oils with various hydrocarbons), in principle the same graphical methods can be developed as have been described for the investigation of hydrocarbon mixtures. However, the construction of useful graphical representations is hampered by the fact that reliable data on physical constants are restricted to the normal saturated fatty acids and their methyl and ethyl esters the synthesis of pure unsaturated fatty acids is already extremely difficult, to say nothing of more complicated cyclic or branched compounds. [Pg.89]

Most of the common forms of corrosion of metals and alloys in a cooling system involve oxygen. The water is normally saturated with O2, and it is the rate of diffusion to a metal surface that is an important factor in the subsequent rate of corrosion reactions. The rate of diffusion is, in turn, affected by the circulating water velocity, the metal surface, temperature and microbiological foulants, etc. Oxygen is capable of accepting electrons and acts as a cathode in the electrochemical cell. At the cathode area, several reactions take place (as described in Section 4.1). [Pg.96]

Condensation can, therefore, take place in narrow capillaries at pressures which are lower than the normal saturation vapour pressure. Zsigmondy (1911) suggested that this phenomenon might also apply to porous solids. Capillary rise in the pores of a solid will usually be so large that the pores will tend to be either completely full of capillary condensed liquid or completely empty. Ideally, at a certain pressure below the normal condensation pressure all the pores of a certain size and below will be filled with liquid and the rest will be empty. It is probably more realistic to assume that an adsorbed monomolecular film exists on the pore walls before capillary condensation takes place. By a corresponding modification of the pore diameter, an estimate of pore size distribution (which will only be of statistical significance because of the complex shape of the pores) can be obtained from the adsorption isotherm. [Pg.125]

Figure 2 shows adsorption isotherms of two sulfated ethoxy-late type anionics - Alipal EP-110 and Alipal EP-120 - on the 85/15 VA/BA latex surface. Again it is soen that the lower molecular weight EP-110 shows a C type isotherm similar to NaLS while the higher molecular weight EP-120 exhibits a normal saturation type isotherm. [Pg.228]

It is well known (3,5,6) that sodium lauryl sulfate interacts with some polymers such as polyvinyl acetate causing solubilization of the insoluble polymer leading to an increase in viscosity. In Figure 3, viscosity of the homopolymer and 70/30 VA/BA at various NaLS/polymer ratio is shown. It is seen that the viscosity of the 2% latex dispersion increases with increase in NaLS/polymer ratio. Similar visoosity data for the 85/15 VA/BA was intermediate between the homopolymer and 70/30 VA/BA latexes. Surfactants that showed a normal saturation type adsorption behavior did not show any significant visoosity increase of the latex. [Pg.228]

More detailed examination and sampling allows association of hydrothermal circulation with specific vent fields. In such waters samples in the Galapagos Rift by the Alvin deep submersible, Jenkins, Edmond, and Corliss (1978) report juvenile He enrichments which dwarf the normal saturation concentrations by factors up to 11 for 4He and 60 for 3He (Figure 4.6). A particularly significant feature of this report is that added He occurs roughly in proportion to added heat AT up to 12°C in sampled water), corresponding to about 7.6 x 10 xcal/atom of 3He (Figure 4.7). Jenkins et al. note that if this value is representative, hydrothermal circulation may indeed account for the depression of conductive heat flow relative to models for total heat flux. As... [Pg.117]

To demonstrate the computational capacities of the SLG-MINDO/3 method we carried out calculations (for the fixed geometry) for a series of normal, saturated hydrocarbons ranging from CH4 to C20H42 by the SLG-MINDO/3 and SCF-MINDO/3 methods. It has been shown that the dependence of computation time on the system size is essentially non-linear in the case of the HFR approximation and is practically linear for the geminal approach. The SLG-MINDO/3 procedure is faster than the SCF-MINDO/3 one even for the simplest hydrocarbons. In the case of the normal hydrocarbon C20H42 (its semiempirical calculation uses 122 basis functions) the computation time for two methods differs 30 times in favor of the SLG approach. [Pg.144]

An 8.2/70/30 composition is antiferroelectric at zero field but becomes ferroelectric when fields greater than lMVm-1 are applied. As a consequence the hysteresis loop has a narrow region at low fields which develops into a normal saturating characteristic at higher fields (Fig. 8.13). This behaviour is temperature sensitive but occurs to a sufficient extent for practical application between 0 and 40 °C. [Pg.457]

Figure 9.17 Distribution of major fatty acids ( xg fatty acids L-1 and xg fatty acid mg-1 OC) in particulate organic matter (POM), very high molecular mass dissolved organic matter (VHDOM) (30 kDa-0.02 xm), and high molecular mass DOM (HDOM) (1-30 xm) in Delaware Bay estuary. Bacterial fatty acids (FA) included branched and normal saturated acids and 15 1A4 and PUFA = polyunsaturated fatty acids. (Modified from Mannino and Harvey, 1999.)... Figure 9.17 Distribution of major fatty acids ( xg fatty acids L-1 and xg fatty acid mg-1 OC) in particulate organic matter (POM), very high molecular mass dissolved organic matter (VHDOM) (30 kDa-0.02 xm), and high molecular mass DOM (HDOM) (1-30 xm) in Delaware Bay estuary. Bacterial fatty acids (FA) included branched and normal saturated acids and 15 1A4 and PUFA = polyunsaturated fatty acids. (Modified from Mannino and Harvey, 1999.)...
The procedure as given is generally applicable for the reduction of esters to alcohols in excellent yields. When preparing the solid normal saturated alcohols, the procedure may be modified, if desired, to permit the recovery of the acid from the unreduced ester. After the alkali is removed the alcohol layer is washed with two successive portions of 20 per cent salt solution which are discarded. Neither the strong alkali nor the salt solutions remove an appreciable amount of organic acid. A solution of 50 g. of calcium chloride in 150 cc. of water is added to the butyl alcohol solution, the mixture is steam-distilled until the butyl alcohol is removed, and the flask and contents are allowed to cool. A hole is made in the cake of solid alcohol and the water layer removed. Two liters of toluene is added and the flask warmed and shaken until the alcohol dissolves and only fine crystals of the calcium salt of the unreduced acid remain. The solution is cooled to 350 and filtered with suction. The calcium soap is removed from the filter, warmed with about 500 cc. of toluene, cooled, filtered, and washed with a little more toluene. The combined toluene solutions may be concentrated and the alcohol crystallized, or the toluene may be completely distilled and the residue vacuum distilled. The insoluble calcium... [Pg.53]

Normal range for TI is 50-160 fig/dL in males TIBC is 250-400 /ng/dL, and transferrin is 200-400 mg/dL (mean is 295). Even though TI is a low normal and transferrin is a high normal, saturation is only 12%, and we can conclude that the patient is mildly iron-deficient. [Pg.195]

The clearest results were obtained with the normal, saturated fatty acids and alcohols. These formed stable films, which would stand considerable compression laterally, and (at room temperature on distilled water) gave a very clearly marked critical area at which the surface pressure first appeared, this point being of course Pockels s critical point of the first diminution of surface tension. As the area was reduced from large initial areas no surface pressure could be detected until the area had reached about 22 sq. A. per molecule and at 20 5 sq. A. the pressure increased very rapidly indeed with further increase of pressure. The curve I of Fig. 15 shows the relation between surface pressure and area per molecule, which is obtained with accurate apparatus for the fatty acids on water curve III is that obtained with the alcohols.3... [Pg.24]

LiP catalyzes the oxidation of 3,4-dimethoxybenzyl alcohol (veratryl alcohol) to veratryl aldehyde. Since this reaction can be easily followed at 310 nm, it is the basis for the standard assay for this enzyme (26,27). The enzyme exhibits normal saturation kinetics for both veratryl alcohol and H202 (28,43). Steady-state kinetic results Indicate a ping-pong mechanism in which H202 first oxidizes the enzyme and the oxidized intermediate reacts with veratryl alcohol (43). The enzyme has an extremely low pH optimum ( 2.5) for a peroxidase (43,44) however, the rate of formation of compound I (kx, Fig. 2) exhibits no pH dependence from 3.0-7.0 (45,46). Addition of excess veratryl alcohol at pH 3.0 results in the rapid conversion of... [Pg.130]


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