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Solvent vaporization

Normally, Henry s constant for solute 2 in solvent 1 is determined experimentally at the solvent vapor pressure Pj. The effect of pressure on Henry s constant is given by... [Pg.22]

Discuss the dependence of the friction phase diagram on temperature, mono-layer density, velocity, load and solvent vapor. Explain why each of these variables will drive one to the right or left in Fig. XII-8. [Pg.458]

Setup your glassware for simple distillation with a claisen adapter, three way adapter, pressure-equalized addition funnel, water cooled condenser, vacuum adapter and receiver flask to catch any condensed solvent vapors. [Pg.268]

These factors make it necessary to reduce the amount of solvent vapor entering the flame to as low a level as possible and to make any droplets or particulates entering the flame as small and of as uniform a droplet size as possible. Desolvation chambers are designed to optimize these factors so as to maintain a near-constant efficiency of ionization and to flatten out fluctuations in droplet size from the nebulizer. Droplets of less than 10 pm in diameter are preferred. For flow rates of less than about 10 pl/min issuing from micro- or nanobore liquid chromatography columns, a desolvation chamber is unlikely to be needed. [Pg.107]

In a concentric-tube nebulizer, the sample solution is drawn through the inner capillary by the vacuum created when the argon gas stream flows over the end (nozzle) at high linear velocity. As the solution is drawn out, the edges of the liquid forming a film over the end of the inner capillary are blown away as a spray of droplets and solvent vapor. This aerosol may pass through spray and desolvation chambers before reaching the plasma flame. [Pg.142]

Having assisted desolvation in this way, the carrier gas then carries solvent vapor produced in the initial nebulization with more produced in the desolvation chamber. The relatively large amounts of solvent may be too much for the plasma flame, causing instability in its performance and, sometimes, putting out the flame completely. Therefore, the desolvation chamber usually contains a second section placed after the heating section. In this second part of the desolvation chamber, the carrier gas and entrained vapor are strongly cooled to temperatures of about 0 to -10 C. Much of the vapor condenses out onto the walls of the cooled section and is allowed to drain away. Since this drainage consists only of solvent and not analyte solution, it is normally directed to waste. [Pg.152]

The droplets, which carry positive or negative charges depending on the sign of the applied potential, pass into and along a small evaporation region. Much of the excess of solvent vapor is allowed to pass to atmosphere or can be gently exhausted to waste. [Pg.390]

Nebulizers convert bulk liquid into an aerosol, consisting of a mix of small droplets of various sizes and solvent vapor. Such devices are used to transfer analyte solutions into the flame of a plasma torch. [Pg.399]

The large quantities of solvent vapor produced from the evaporating droplets must be removed before reaching the plasma flame, which is done by having cooling tubes sited after the heated desolvation chamber to condense the vapor into liquid. This condensed liquid is run to waste. [Pg.400]

Control of sonochemical reactions is subject to the same limitation that any thermal process has the Boltzmann energy distribution means that the energy per individual molecule wiU vary widely. One does have easy control, however, over the energetics of cavitation through the parameters of acoustic intensity, temperature, ambient gas, and solvent choice. The thermal conductivity of the ambient gas (eg, a variable He/Ar atmosphere) and the overaU solvent vapor pressure provide easy methods for the experimental control of the peak temperatures generated during the cavitational coUapse. [Pg.262]

Lamination Inks. This class of ink is a specialized group. In addition to conforming to the constraints described for flexo and gravure inks, these inks must not interfere with the bond formed when two or more films, eg, polypropylene and polyethylene, are joined with the use of an adhesive in order to obtain a stmcture that provides resistance properties not found in a single film. Laminations are commonly used for food applications such as candy and food wrappers. Resins used to make this type of ink caimot, therefore, exhibit any tendency to retain solvent vapor after the print has dried. Residual solvent would contaminate the packaged product making the product unsalable. [Pg.252]

The solvent vapor also serves as a blanket in the reactor. The processing solvent is usually left in the product as part of the dilution solvent. [Pg.39]

The areas for the reactors and storage tanks should be separated by fire walls, and must be adequately ventilated. Storage tanks should be blanketed by inert gas. A slight positive pressure of inert gas should be maintained in the reactor or storage tanks during the discharging of the resin or resin solution to prevent air from being sucked into the vessel to form an explosive mixture with the solvent vapor. [Pg.41]

With the ever increasing awareness of the need of environment protection, the emission of solvent vapors and organic fumes into the atmosphere should be prevented by treating the exhaust through a proper scmbber. The solvent used for cleaning the reactor is usually consumed as part of the thinning solvent. Aqueous effluent should be properly treated before discharge. [Pg.41]

Toxicity. 1,1-Dichloroethane, like all volatile chlorinated solvents, has an anesthetic effect and depresses the central nervous system at high vapor concentrations. The 1991 American Conference of Governmental Industrial Hygienists (ACGIH) recommends a time-weighted average (TWA) solvent vapor concentration of 200 ppm and a permissible short term exposure level (STEL) of 250 ppm for worker exposure. The oral LD q of... [Pg.7]

Entry into a tank that has contained any chlorinated or any easily evaporated solvent requires special procedures to ensure worker safety. The heavier vapors tend to concentrate in unventilated spaces. The proper tank entry procedure requires positive ventilation, testing for residue solvent vapor and oxygen levels, and the use of respiratory equipment and rescue harness. Monitoring the tank from outside is also important. The use of an appropriate gas mask is permissible in vapor concentrations of less than 2% and when there is no deficiency of atmospheric oxygen, but not for exposures exceeding one-half hour. Skin exposure to 1,1,1-trichloroethane can cause irritation, pain, bHsters, and even burning. Eye exposure may produce irritation, but should... [Pg.10]

Recently several patents have been issued (16—18) describing the use of 1,2-dichloroethylene for use in blends of chlorofluorocarbons for solvent vapor cleaning. This art is primarily driven by the need to replace part of the chlorofluorocarbons because of the restriction on their production under the Montreal Protocol of 1987. Test data from the manufacturer show that the cleaning abiUty of these blends exceeds that of the pure chlorofluorocarbons or their azeotropic blends (19). [Pg.20]

Whereas conductive and radiative heating are useful techniques for some appHcations, convective heating is by far the most common means of supplying the energy needed to evaporate the solvent, because convection is the only means of heating that also provides a means of transporting solvent vapor away from the surface of the coating. [Pg.314]


See other pages where Solvent vaporization is mentioned: [Pg.56]    [Pg.72]    [Pg.77]    [Pg.106]    [Pg.138]    [Pg.139]    [Pg.139]    [Pg.150]    [Pg.152]    [Pg.263]    [Pg.915]    [Pg.262]    [Pg.262]    [Pg.43]    [Pg.89]    [Pg.308]    [Pg.427]    [Pg.546]    [Pg.548]    [Pg.299]    [Pg.42]    [Pg.43]    [Pg.403]    [Pg.392]    [Pg.339]    [Pg.483]    [Pg.259]    [Pg.315]    [Pg.496]    [Pg.123]    [Pg.1149]    [Pg.1177]   
See also in sourсe #XX -- [ Pg.189 ]




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Carbon, activated bead, solvent vapor removal

Debris solvent vapor

Differential solvent vapor sorption

Early solvent vapor exit, injection

Flame solvent vapor entering

Humidity charts for solvent vapors

Poly solvent vapor treatment

Recovery of Solvent and Other Vapors

Single solvent vapor degreaser

Solvent cleaning ultrasonic vapor degreasing

Solvent cleaning vapor degreasing

Solvent heat of vaporization

Solvent organic, vapors

Solvent polymer vapor-liquid equilibria

Solvent vapor annealing

Solvent vapor exit

Solvent vapor molecules

Solvent vapor phase

Solvent vapor pressure

Solvent vapor pressure effects

Solvent vapor recovery

Solvent vapor recovery adsorption

Solvent vapor removal

Solvent vapors, capturing

Solvent-Vapor Annealing of Conjugated Oligomers

Solvents, mixed aqueous vapor pressure

Superheated solvent vapor

Vapor Sorption and Solvent Probe Techniques

Vapor degreasing, solvent

Vapor degreasing, solvent application

Vapor permeation solvent recovery using

Vapor pressures of solvents

Vapor-liquid equilibria in presence of solvents

Vapor-liquid equilibrium data butane/2-butene in solvents

Vapor-liquid equilibrium data cyclohexane/benzene in solvents

Vapor-liquid equilibrium data heptane/methylcylohexane in solvents

Vapor/liquid equilibrium solute/solvent systems

Vapors solvent

Vapors solvent

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