Two-line system

Figure 8-38. Moire patterns from the superposition of two patterns at increasing angles. Top two line systems Bottom two circle systems [54].

Determination of dispersion Single-line system. Also determine the dispersion by clamping the reagent tube to convert to a single-line system remove the tube from the pump. Determine the dispersion as above-and compare with that of the two-line system. 

If original stoichiometric concentrations and pumping rates in the two-line system are equal, then equivalence is met at which means... 

Technically, FIA titrations can be performed either in a single-line system, as discussed previously, or in a two-line system (cfr. Fig. 2.14 and Section 4.9.). For a two-line system, where titrant R is confluenced to a sample zone dispersed in an inert carrier stream. 

The continuous line in Figure 16 shows results from fitting a single tie line in addition to the binary data. Only slight improvement is obtained in prediction of the two-phase region more important, however, prediction of solute distribution is improved. Incorporation of the single ternary tie line into the method of data reduction produces only a small loss of accuracy in the representation of VLE for the two binary systems. 

Figure 4-19. Calculated selectivities in two ternary systems show large improvements when tie-line data are used to supplement binary VLB data for estimating binary parameters.

Figure A2.5.3. Typical liquid-gas phase diagram (temperature T versus mole fraction v at constant pressure) for a two-component system in which both the liquid and the gas are ideal mixtures. Note the extent of the two-phase liquid-gas region. The dashed vertical line is the direction x = 1/2) along which the fiinctions in figure A2.5.5 are detemiined.

Figure A2.5.4. Themiodynamic fimctions (i, n, and C as a fimction of temperature T at eonstant pressure and eomposition x = 1/2) for the two-eomponent system shown in figure A2.5.3. Note the diflferenee between these and those shown for the one-eomponent system shown in figure A2.5.2. The fiinetions shown are dimensionless as in figure A2.5.2. The dashed lines represent metastable extensions (superheating or supereooling) of the one-phase systems.

Figure B2.4.5. Simulated lineshapes for an intennolecular exchange reaction in which the bond joining two strongly coupled nuclei breaks and re-fomis at a series of rates, given beside tlie lineshape. In slow exchange, the typical spectrum of an AB spin system is shown. In the limit of fast exchange, the spectrum consists of two lines at tlie two chemical shifts and all the coupling has disappeared.

This equation was derived for a two-dimensional system, where the areal density, p, of the snow was used. It applies equally to a three-dimensional system, where the discontinuity is a plane instead of a line, and p is the volume density. 

A multiple pipe line system consisting of two or more parallel lines of different diameters and different lengths. 

Method two The system time eonstant is the interseetion of the slope at t = 0 with the final value line (see Figure 3.13) sinee... 

Special resins consist of a two-phase system composed of a mix of a highly condensed, and no longer soluble, PF-resin with a standard type PF-resin [63]. Another two-phase resin is composed of a highly condensed PF-resin, still in an aqueous solution, and of a PF dispersion [64]. The purpose of such special resins is the gluing of wet wood, where the danger of overpenetration of the resin into the wood surface exists and would cause a starved glue line. 

Two-component systems consist of (1) polyol or polyamine, and (2) isocyanate. The hardening starts with the mixing of the two components. Due to the low viscosities of the two components, they can be used without addition of solvents. The mass ratio between the two components determines the properties of the bond line. Linear polyols and a lower surplus of isocyanates give flexible bond lines, whereas branched polyols and higher amounts of isocyanates lead to hard and brittle bond lines. The pot life of the two-component systems is determined by the reactivity of the two components, the temperature and the addition of catalysts. The pot life can vary between 0.5 and 24 h. The cure at room temperature is completed within 3 to 20 h. 

Figure 4.1 Schematic diagram of a coupled column system. The first column (ID) is connected to the second column (2D) tlirough the interface or valve system. The interface can be a diiect coupling, a live T-union, a complex multiport valve, or a thermal or cryogenic modulation system. The stimulus can be the switching of the valve, abalancing pressure to divert flow towards 2D, an added flow that is used in pressure tuning, or the drive mechanism for the modulator. The line to detector 1 will normally be a non-retaining section of column. In a two-oven system, ID and 2D will be in different ovens the dotted line indicates separately heated zones.

Because a phase change is usually accompanied by a change in volume the two-phase systems of a pure substaiice appear on a P- V (or a T- V) diagram as regions with distinct boundaries. On a P- V plot, the triple point appears as a horizontal line, and the critical point becomes a point of inflection of the critical isotherm, T = T (see Figure 2-78 and Figure 2-80). 

Quality of a Wet Vapor, in the vapor-liquid region of a pure substance, the composition of a two-phase system (at given T and P) varies from pure saturated liquid at the bubble jjoint M to pure saturated vapor at the dew point N along the line MQN on the P- V diagram (Figure 2-80). For a wet vapor represented by an intermediate... 

We draw two lines representing these two expressions for pe as a function of pH in Fig. 5-1. We discuss five cases for this system ... 

---