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Liquid ITIES

The mixture of glycerin and PVC emulsion is completely absorbed by sponge cubes, which are further tumbled to achieve uniform distribution of liquid. ITie impregnated cubes are exposed to 100"C for 30 min and at 127"C for 40 min, which is sufficient to sinter particles of PVC. Glycerin is washed out by water in the next step and cubes are dried. Cubes have a PVC/cellulose ratio of 3.41/1 and they have a microporous structure. The cubes are used to remove toxic organic species from water such as polychlorinated biphenyls, dioxins, polyaromatie hydrocarbons, nitroaromatics, pesticides, herbieides, and volatile halocarbons. [Pg.268]

The computer subroutines for calculation of vapor-phase and liquid-phase fugacity (activity) coefficients, reference fugac-ities, and molar enthalpies, as well as vapor-liquid and liquid-liquid equilibrium ratios, are described and listed in this Appendix. These are source routines written in American National Standard FORTRAN (FORTRAN IV), ANSI X3.9-1978, and, as such, should be compatible with most computer systems with FORTRAN IV compilers. Approximate storage requirements and CDC 6400 execution times for these subroutines are given in Appendix J. [Pg.289]

ITi = weight in air of the water required to fill the pyknometer at fC W2 = weight in air of the liquid required to fill the pyknometer at t°C d = density of water in grams per milliliter at fC Sync = specific gravity of the liquid at t°C referred to water at t°C corrected for the buoyant effect of air... [Pg.448]

For a better understanding of the interactions between parameters, it is often helpful to calculate the effective bubble rise velocity from measurea valves of for example, the data of Mersmann (loc. cit.) indicated = 0.6 for = 0.05 iti/s, giving U, = 0.083 m/s, which agrees with the data reported in Fig. 14-43 for the rise velocity of bubble clouds. The rise velocity of single bubbles, for d - 2 mm, is about 0.3 m/s, for liquids with viscosities not too different from water. Using this value in Eq. (14-220) and comparing with Fig. 14-104, one finds that at low values of the rise velocity of the bubbles... [Pg.1426]

Liquid spills. Possibil- Provide spill control through adequate ity of accumulation of drainage and curbs or dikes flammable liquids. adequate ventilation resulting in fire or explosion hazard. down systems Minimize possibility of ignition Minimize possibility of spills API RP 750 CCPS G-22 CCPS G-24 CCPS G-30 Lees 1996 NFPA 69 NFPA-15... [Pg.31]

Figure 13.4 (a) ITie cri-bridged polymeric structure of liquid SbFs (schematic) show-ing the three sorts of F alom. (b) Structure of the tetrameric molecular unit in crystalline (SbFs)4 show[Pg.562]

Concerning a liquid droplet deformation and drop breakup in a two-phase model flow, in particular the Newtonian drop development in Newtonian median, results of most investigations [16,21,22] may be generalized in a plot of the Weber number W,. against the vi.scos-ity ratio 8 (Fig. 9). For a simple shear flow (rotational shear flow), a U-shaped curve with a minimum corresponding to 6 = 1 is found, and for an uniaxial exten-tional flow (irrotational shear flow), a slightly decreased curve below the U-shaped curve appears. In the following text, the U-shaped curve will be called the Taylor-limit [16]. [Pg.690]

In the laser flash method, a melt of interest is placed between two parallel plates. The upper plate is heated stepwise and the thermal diffusiv-ity is measured from the rise in temperature. The specific design for molten materials and especially slags employed by Ohta et al. is based on the differential three-layer technique utihzing a special cell that can be accommodated in the system. A schematic diagram of the principle of the measurement section is shown in Fig. 31. A laser pulse irradiates the upper (platinum) crucible and the temperature response of the surface of the lower platinum crucible is observed, a liquid specimen being sandwiched between the two. [Pg.187]

An interface between two immiscible electrolyte solutions (ITIES) is formed between two liqnid solvents of a low mutual miscibility (typically, <1% by weight), each containing an electrolyte. One of these solvents is usually water and the other one is a polar organic solvent of a moderate or high relative dielectric constant (permittivity). The latter requirement is a condition for at least partial dissociation of dissolved electrolyte(s) into ions, which thus can ensure the electric conductivity of the liquid phase. A list of the solvents commonly used in electrochemical measurements at ITIES is given in Table 32.1. [Pg.607]

The comprehensive review by Gocan et al. [25] focused specifically on lipophilic-ity measurements by liquid chromatography, including reversed phase, thin-layer, micellar, RP-ion-pair and countercurrent chromatography. [Pg.416]

Whenever corrosion resistance results from the formation of layers of insoluble corrosion products on the metallic surface, the effect of high velocity may be to prevent their normal formation, to remove them after they have been formed, and/or to preclude their reformation. All metals that are protected by a film are sensitive to what is referred to as its critical velocity i.e., the velocity at which those conditions occur is referred to as the critical velocity of that chemistry/temperature/veloc-ity environmental corrosion mechanism. When the critical velocity of that specific system is exceeded, that effect allows corrosion to proceed unhindered. This occurs frequently in small-diameter tubes or pipes through which corrosive liquids may be circulated at high velocities (e.g., condenser and evaporator tubes), in the vicinity of bends in pipelines, and on propellers, agitators, and centrifugal pumps. Similar effects are associated with cavitation and mechanical erosion. [Pg.9]

The theory of sublimation, t.e. the direct conversion from the vapour to the solid state without the intermediate formation of the liquid state, has been discussed in Section 1,19. The number of compounds which can be purified by sublimation under normal pressm-e is comparatively small (these include naphthalene, anthracene, benzoic acid, hexachloroethane, camphor, and the quinones). The process does, in general, yield products of high pm-ity, but considerable loss of product may occur. [Pg.154]

Liquid surfaces and liquid-liquid interfaces are very common and have tremendous significance in the real world. Especially important are the interfaces between two immiscible liquid electrolyte solutions (acronym ITIES), which occur in tissues and cells of all living organisms. The usual presence of aqueous electrolyte solution as one phase of ITIES is the main reason for the electrochemical nature of such interfaces. [Pg.17]

Fortunately the microinterfaces between two immiscible electrolytes seem to be a very useful experimental model of small liquid-liquid systems. The formation and investigation of the micro-ITIES is continuously perfected [74-76]. The smallest diameter so far achieved was 5 jiva. The main utilization of micro-ITIES is developed, in parallel with application of ultramicroelectrodes. [Pg.36]

As mentioned earlier, a great deal of literature has dealt with the properties of heterogeneous liquid systems such as microemulsions, micelles, vesicles, and lipid bilayers in photosynthetic processes [114,115,119]. At externally polarizable ITIES, the control on the Galvani potential difference offers an extra variable, which allows tuning reaction paths and rates. For instance, the rather high interfacial reactivity of photoexcited porphyrin species has proved to be able to promote processes such as the one shown in Fig. 3(b). The inhibition of back ET upon addition of hexacyanoferrate in the photoreaction of Fig. 17 is an example of a photosynthetic reaction at polarizable ITIES [87,166]. At Galvani potential differences close to 0 V, a direct redox reaction involving an equimolar ratio of the hexacyanoferrate couple and TCNQ features an uphill ET of approximately 0.10 eV (see Fig. 4). However, the excited state of the porphyrin heterodimer can readily inject an electron into TCNQ and subsequently receive an electron from ferrocyanide. For illumination at 543 nm (2.3 eV), the overall photoprocess corresponds to a 4% conversion efficiency. [Pg.227]

Despite the fact that the electrodeposition of copper and silver at the water-DCE and the water-dichloromethane interfaces has been generally regarded as the first experimental evidence for heterogeneous ET at externally biased ITIES [171], a very limited amount of work has dealt with this type of process. This reaction has also theoretical interest because the molecular liquid-liquid interface can be seen as an ideal substrate for electrochemical nucleation studies due to the weak interactions between the interface and the newly formed phase and the lack of preferential nucleation sites always present at metallic electrodes. [Pg.229]

Since the first use of SECM to study ET kinetics at a liquid-liquid interface in 1995 [47], the methodology has been proven a powerful approach for investigating the dependence of ET rate constants on the Galvani potential drop across an ITIES. [Pg.314]

In this chapter, we describe some of the more widely used and successful kinetic techniques involving controlled hydrodynamics. We briefly discuss the nature of mass transport associated with each method, and assess the attributes and drawbacks. While the application of hydrodynamic methods to liquid liquid interfaces has largely involved the study of spontaneous processes, several of these methods can be used to investigate electrochemical processes at polarized ITIES we consider these applications when appropriate. We aim to provide an historical overview of the field, but since some of the older techniques have been reviewed extensively [2,3,13], we emphasize the most recent developments and applications. [Pg.333]

The electrolyte dropping electrode [63] method, introduced in 1976, and subsequently used in conjunction with the four-electrode potentiostat [64], is a hydrodynamic technique, offering controlled convective transport. In essence, this approach is identical to the dropping mercury electrode [65] however, the drop consists of a flowing electrolyte liquid phase which forms a polarized ITIES with an immiscible continuous (receptor) phase. In... [Pg.346]


See other pages where Liquid ITIES is mentioned: [Pg.14]    [Pg.381]    [Pg.1138]    [Pg.1434]    [Pg.1435]    [Pg.1481]    [Pg.1743]    [Pg.337]    [Pg.31]    [Pg.338]    [Pg.658]    [Pg.188]    [Pg.233]    [Pg.385]    [Pg.386]    [Pg.386]    [Pg.252]    [Pg.617]    [Pg.197]    [Pg.503]    [Pg.17]    [Pg.190]    [Pg.194]    [Pg.202]    [Pg.212]    [Pg.229]    [Pg.231]    [Pg.233]    [Pg.290]    [Pg.295]    [Pg.332]    [Pg.379]   
See also in sourсe #XX -- [ Pg.317 ]




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