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Solution line

The conductor-like screening model (COSMO) is a continuum method designed to be fast and robust. This method uses a simpler, more approximate equation for the electrostatic interaction between the solvent and solute. Line the SMx methods, it is based on a solvent accessible surface. Because of this, COSMO calculations require less CPU time than PCM calculations and are less likely to fail to converge. COSMO can be used with a variety of semiempirical, ah initio, and DFT methods. There is also some loss of accuracy as a result of this approximation. [Pg.212]

The ease with which the ferrous ion can be oxidized to a ferric ion in the electrowinning cell furthers this reaction. Attack on the copper is most apparent at the solution line, where it results in corrosion of the loops supporting the cathodes, leading to dropped cathodes. [Pg.207]

Fig. 1. Vapor pressure and relative humidity over CaCl solutions and solids. The straight horizontal lines ia the right-hand portion represent two soHd phases and a gas phase for vertical line iatersections. In addition, a soHd phase, saturated solution, and a vapor phase occur ia the regions between the vertical lines. The lower left-hand corner shows the ice solution line. The region ia between, with skewed isothermal lines, represents unsaturated solutions ... Fig. 1. Vapor pressure and relative humidity over CaCl solutions and solids. The straight horizontal lines ia the right-hand portion represent two soHd phases and a gas phase for vertical line iatersections. In addition, a soHd phase, saturated solution, and a vapor phase occur ia the regions between the vertical lines. The lower left-hand corner shows the ice solution line. The region ia between, with skewed isothermal lines, represents unsaturated solutions ...
With reference to Fig. 18-81 (both graphs), EF represents the locus of overflow compositions for the case in which the overflow stream contains no inert sohds. E F represents the overflow streams containing some inert sohds, either by entrainment or by partial solubihty in the overflow solution. Lines GF, GL, and GM represent the loci of underflow compositions for the three different conditions indicated on the diagram. In Fig. 18-81 7, the constant underflow line GM is par-aUel to EF, the hypotenuse of the triangle, whereas GF passes through... [Pg.1676]

Fig. 64. Single-chain behavior in semi-dilute PDMS/d-chlorbenzene solutions. Line-shape parameter (3 as a function of Q at the concentration c = 0.18 and c = 0.45, indicating the occurance of two crossover effects, as predicted by the concept of incompletely screened hydrodynamic interactions. (----), (---) asymptotic Zimm and Rouse behavior, respectively. (Reprinted with per-... Fig. 64. Single-chain behavior in semi-dilute PDMS/d-chlorbenzene solutions. Line-shape parameter (3 as a function of Q at the concentration c = 0.18 and c = 0.45, indicating the occurance of two crossover effects, as predicted by the concept of incompletely screened hydrodynamic interactions. (----), (---) asymptotic Zimm and Rouse behavior, respectively. (Reprinted with per-...
The principle of operation of this device is simple. A small amount of the flowing water volumetrically displaces foam concentrate from the tank into the main water stream. The working pressure of the vessel must, of course, be above the maximum static water pressure encountered in the system. This type of proportioner may consist of one tank or pressure container with a watertight divider so that it operates as two tanks, two tanks separately connected to the water and foam solution lines, or the tanks in the system may each be fitted with flexible diaphragms or bladders to separate the "driving" water from foam concentrate or they may rely simply on differences in density of the two liquids to retard mixing during operation. [Pg.212]

Fig. 6.40 A phase diagram calculated using SCFT for a mixture containing equal amounts of two homopolymers and a symmetric diblock, all with equal chain length (Janert and Schick 1997a). A-rich and B-rich swollen lamellar bilayer phases are denoted LA and LH respectively whilst the corresponding disordered phases are denoted A and B. The con-solute line of asymmetric bilayer phases LA and Lu, shown dotted, is schematic.The dashed line is the unbinding line. The arrows indicate the locations of the unbinding transition X jN and multicritical Lifshitz point, cMiV " 6.0. Fig. 6.40 A phase diagram calculated using SCFT for a mixture containing equal amounts of two homopolymers and a symmetric diblock, all with equal chain length (Janert and Schick 1997a). A-rich and B-rich swollen lamellar bilayer phases are denoted LA and LH respectively whilst the corresponding disordered phases are denoted A and B. The con-solute line of asymmetric bilayer phases LA and Lu, shown dotted, is schematic.The dashed line is the unbinding line. The arrows indicate the locations of the unbinding transition X jN and multicritical Lifshitz point, cMiV " 6.0.
The optimal solution line for the family of the e-constraint problems is a one dimensional manifold in the parameter space. It defines a trade-off curve in the objective function space. [Pg.336]

FIG. 17. Comparison between Monte Carlo simulation (symbols) with decamers and the mean-field solution (lines) of the simplified model with the harmonic grafting potential. The net osmotic pressure is given as a function of separation for various value of surface o and y. solid line and circles y —1.0, one charge per 50.77 A2. Dotted line and squares y = 1.0, one charge per 101.54 A2. Dashed line and diamonds y = 0.875, one charge per 50.77 A2 [61]. [Pg.499]

At the point C the two liquid layers become identical, and this is called the critical solution point or con-solute point. If the total applied pressure is varied, both the critical temperature and composition of the critical mixture alter and we obtain a critical solution line. As an example of this we give in table 16. If the dependence of the critical solution temperature on pressure for the system cyclohexane -f aniline. An increase of pressure raises the critical solution temperature, and the mutual solubility of the two substances is decreased. We saw earlier that the applied pressure had only a small effect on the thermodynamic properties of condensed phases, and we notice in this case that an increase of pressure of 250 atm. alters the critical temperature by only 1.6 °C. [Pg.238]

Fig. 16.21. Critical solution line in a ternary system at constant pressure. ... Fig. 16.21. Critical solution line in a ternary system at constant pressure. ...
Fig. 28 Layer thickness increase due to formation of a PEL-PEL complex during exposure of a MePVP brush to a PSSNa solution or a PMAA solution. Lines are a guide to the... Fig. 28 Layer thickness increase due to formation of a PEL-PEL complex during exposure of a MePVP brush to a PSSNa solution or a PMAA solution. Lines are a guide to the...
Figure 3.13 Maximum velocity being reached at the axis in the steady-state region of the duct with a linear EPR h = 0,3 near the walls dots numerical solution, lines by the analytical formulae for A = 0 (curve 1) A = 1 (2) 5 (3) 10 (4) 15 (5) 20 (6) 50 (7) 100 (8) 200 (9) 400 (10) and A = 1000 (curve 11). Figure 3.13 Maximum velocity being reached at the axis in the steady-state region of the duct with a linear EPR h = 0,3 near the walls dots numerical solution, lines by the analytical formulae for A = 0 (curve 1) A = 1 (2) 5 (3) 10 (4) 15 (5) 20 (6) 50 (7) 100 (8) 200 (9) 400 (10) and A = 1000 (curve 11).
Fig. 10. Relative excitation spectra of the emission of LiZnVO4 (1) at 5 K, the high-pressure modification of LiZnVO4 (2) at 5K, SiO2-V,Al (J) at 77 K, LiMgPo.99Vo.oif 4 (4) at 5 K and 1 0.99 0.01 4 ( 1 at 300 K. Curve (6) gives the absorption spectrum of VO in aqueous solution. Lines are dotted for clarity only. After Ref. 23... Fig. 10. Relative excitation spectra of the emission of LiZnVO4 (1) at 5 K, the high-pressure modification of LiZnVO4 (2) at 5K, SiO2-V,Al (J) at 77 K, LiMgPo.99Vo.oif 4 (4) at 5 K and 1 0.99 0.01 4 ( 1 at 300 K. Curve (6) gives the absorption spectrum of VO in aqueous solution. Lines are dotted for clarity only. After Ref. 23...
Another interesting variation on negative diazo resists involves compositions of aqueous acetic acid solution of 4-dimethylaminophenyldiazonium chloride and zinc chloride in a poly(N-vinyl pyrrolidone) binder this is coated over cresol novolac film on a silicon wafer substrate. " The diazonium compound diffuses into the phenolic layer and is eventually partitioned in a uniform layer between the top layer and the phenolic resin. On exposure, the diazonium compound in the top layer bleaches and acts as a contrast-enhancement dye, while in the bottom it decomposes to the nonpolar 4-dimethylaminochlorobenzene, which acts as a dissolution inhibitor of the phenolic resin during development in aqueous-base solution. Line and space feature resolution of 0.5 p-m has been reported for this material. [Pg.234]

Standard Tint Paper.—A solution of caramel in water is made of such concentration that when diluted one hundred times (10 c.c. made up to 1 litre) the tint of this diluted solution equals the tint produced by the Nessler test in 100 c.c. water containing. 000075 grm. of ammonia, or. 00023505 grm. AmCl. With this caramel solution lines are drawn on strips of white filter paper (previously well washed with distilled water, to remove traces of bleaching matter, and dried) by means of a quill pen. When the marks thus produced are dry, the paper is cut into pieces of the same size as the test paper previously described, in such a way that each piece has a brown line across it near the middle of its length, and only such strips are preserved in which the brown line has a breadth varying from 1 2 mm. to 1 mm. (1/50 of an inch to 1/25 of an inch). [Pg.112]

Joule Heating in Electrokinetic Flow Theoretical Models, Fig. 4 Comparison of the theoretical plate numbers, N = Lo/H, between the analytical solution (lines) and the previous experiment (symbols). The solid line is determined from Eq. 46, while the dashed line accounts for 40 % of the plate numbers in the solid line (Reprinted from [7])... [Pg.1497]

Fig. 11.1. Slructure of the low-temperature phase (black circles oxygen atoms) of oxonium perchlorate (H3OCIO4) A, Raman spectra and B, details of the vCI-O(H) stretching region are given for the crystal (line a), the molten salt (Une b) and the aqueous solutions (line c) (with permission). Fig. 11.1. Slructure of the low-temperature phase (black circles oxygen atoms) of oxonium perchlorate (H3OCIO4) A, Raman spectra and B, details of the vCI-O(H) stretching region are given for the crystal (line a), the molten salt (Une b) and the aqueous solutions (line c) (with permission).
FIG. 6. Dependence of the frequency shift on potential in the double-layer region on gold in different solutions. Lines were calculated for the mass-effect [see Eq. (54)]. Arrows show the approximate position of the pzc. (From Ref. 98.)... [Pg.35]

Figure 3 shows the pseudo first-order kinetic response for the disappearance of the epoxy in buffered methanol solutions (lines are for clarity only). [Pg.2698]

Solution line is the boundary that is formed on a material surface when two phases have a stable interface that remains in one location for an extended time. The exjxrsure alternates between continuous and partial immersion. The solution line level may change due to agitation, or when a vessel or tank is filled by different amounts. Solution line effects cause oxidant levels at the metal surface to fluctuate. [Pg.782]

Figure 3.378. Typical data for drag-reducing polymer solutions falls between the turbulent solutions line for pipe flow, and laminar line, 64/Re, greatly extended beyond its usual limit of a Reynolds number of 2300, where /= pipe friction coefficient in engineering equal to pressure drop per length times the diameter, divided by l/2pf, and p = density, [1080],... Figure 3.378. Typical data for drag-reducing polymer solutions falls between the turbulent solutions line for pipe flow, and laminar line, 64/Re, greatly extended beyond its usual limit of a Reynolds number of 2300, where /= pipe friction coefficient in engineering equal to pressure drop per length times the diameter, divided by l/2pf, and p = density, [1080],...
The rapidity of convergence of substitution methods depends strongly on the slope of the solution line with respect to the diagonal line. If direct substitution diverges, either the problem must be reformulated or... [Pg.78]


See other pages where Solution line is mentioned: [Pg.394]    [Pg.48]    [Pg.160]    [Pg.265]    [Pg.779]    [Pg.192]    [Pg.2238]    [Pg.2000]    [Pg.332]    [Pg.65]    [Pg.46]    [Pg.499]    [Pg.158]    [Pg.1988]    [Pg.372]    [Pg.436]    [Pg.38]    [Pg.2682]    [Pg.783]    [Pg.783]    [Pg.145]    [Pg.444]    [Pg.1951]   
See also in sourсe #XX -- [ Pg.782 ]




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