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Evaporation and

Separation of a volatile liquid from an involatile component. This is a common operation carried out by Evaporation and drying. These processes are considered in some detail later. [Pg.75]

Drying refers to the removal of water from a substance through a whole range of processes, including distillation, evaporation, and even physical separations such as with centrifuges. Here, consideration is restricted to the removal of moisture from solids and liquids into a gas stream (usually air) by heat, namely, thermal drying. Some of the types of equipment for removal of water also can be used for removal of organic liquids from solids. [Pg.89]

As with distillation and absorption, when evaporators and dryers are chosen, no attempt should be made to carry out any optimization at this stage in the design. [Pg.92]

Figure 15.1a shows a single-stage evaporator represented on both actual and shifted temperature scales. Note that in shifted temperature scale, the evaporation and condensjftion duties are shown at different temperatures even though they are at the same actual temperature. Figure 15.16 shows a similar plot for a three-stage evaporator. [Pg.355]

Like distillation, the appropriate placement of evaporators and dryers is that they should be above the pinch, below the pinch, but not across the pinch. The grand composite curve can be used to assess appropriate placement quantitatively. [Pg.362]

Distillation columns, evaporators, and dryers should be above the... [Pg.403]

The physical chemist is very interested in kinetics—in the mechanisms of chemical reactions, the rates of adsorption, dissolution or evaporation, and generally, in time as a variable. As may be imagined, there is a wide spectrum of rate phenomena and in the sophistication achieved in dealing wifli them. In some cases changes in area or in amounts of phases are involved, as in rates of evaporation, condensation, dissolution, precipitation, flocculation, and adsorption and desorption. In other cases surface composition is changing as with reaction in monolayers. The field of catalysis is focused largely on the study of surface reaction mechanisms. Thus, throughout this book, the kinetic aspects of interfacial phenomena are discussed in concert with the associated thermodynamic properties. [Pg.2]

An interesting consequence of covering a surface with a film is that the rate of evaporation of the substrate is reduced. Most of these studies have been carried out with films spread on aqueous substrates in such cases the activity of the water is practically unaffected because of the low solubility of the film material, and it is only the rate of evaporation and not the equilibrium vapor pressure that is affected. Barnes [273] has reviewed the general subject. [Pg.146]

The derivation that follows is essentially that given by Langmuir [9] in 1918, in which one writes separately the rates of evaporation and of condensation. The surface is assumed to consist of a certain number of sites S of which S are occupied and Sq = S - S arc free. The rate of evaporation is taken to be proportional to 5, or equal tokiSi, and the rate of condensation proportional to the bare surface So and to the gas pressure, or equal to k PSo. At equilibrium. [Pg.604]

The basic assumption is that the Langmuir equation applies to each layer, with the added postulate that for the first layer the heat of adsorption Q may have some special value, whereas for all succeeding layers, it is equal to Qu, the heat of condensation of the liquid adsorbate. A furfter assumption is that evaporation and condensation can occur only from or on exposed surfaces. As illustrated in Fig. XVII-9, the picture is one of portions of uncovered surface 5o, of surface covered by a single layer 5, by a double-layer 52. and so on.f The condition for equilibrium is taken to be that the amount of each type of surface reaches a steady-state value with respect to the next-deeper one. Thus for 5o... [Pg.619]

The fonnation of clusters in the gas phase involves condensation of the vapour of the constituents, with the exception of the electrospray source [6], where ion-solvent clusters are produced directly from a liquid solution. For rare gas or molecular clusters, supersonic beams are used to initiate cluster fonnation. For nonvolatile materials, the vapours can be produced in one of several ways including laser vaporization, thennal evaporation and sputtering. [Pg.2388]

Evaporation and crystallisation of the sodium sulphite solution gives crystals of the heptahydrate NajSOj.THjO. However, on evaporation of the hydrogensulphite solution, the solid obtained is chiefly sodium pentaoxodisulphate(IV) ( metabisulphite ) Na2S20j, and contains little if any of the hydrogensulphite. However, the hydrogen sulphite ion is obtained when the solid redissolves in water ... [Pg.293]

It is also possible to simulate liquid droplets by surrouridiu g a solute by a fin ite ii urn ber of water moleeu les an d perform in g the sim -ulalion without a periodic box. The water, of course, eventually evaporates and moves away from the solute when periodic boundary con ditioii s arc n ot im posed. If the water is in itially added via periodic boundary con dition s, you rn ust edit the resu Itin g H IN file to remove th e periodic boti ruiary con ditioii s, if a droplet approach is desired. [Pg.201]

Kestner Laboratory Stirrer supplied by Kestner Evaporator and Engineering Co. Ltd. [Pg.62]

Remove the condenser, then with the aid of a funnel add the water slowly, keep stirring. If the solution is too hot the water will evaporate and make a big mess. As the water is added you will notice that loads of stodgy crapp will form, this is normal, connect the condenser for the distillation with a receiving flask at least 500ml in capacity. [Pg.220]


See other pages where Evaporation and is mentioned: [Pg.76]    [Pg.87]    [Pg.88]    [Pg.204]    [Pg.249]    [Pg.250]    [Pg.250]    [Pg.355]    [Pg.357]    [Pg.359]    [Pg.359]    [Pg.361]    [Pg.362]    [Pg.330]    [Pg.929]    [Pg.277]    [Pg.324]    [Pg.162]    [Pg.392]    [Pg.568]    [Pg.899]    [Pg.1]    [Pg.21]    [Pg.121]    [Pg.170]    [Pg.95]    [Pg.143]    [Pg.183]    [Pg.13]    [Pg.123]   
See also in sourсe #XX -- [ Pg.287 ]




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Airflow and Water Evaporation

Batch Distillation and Evaporation

Boiling and Evaporation in Microchannels

Casting and Evaporating

Chemical Interactions to the Adhesion Between Evaporated Metals and Functional Croups of Different Types at Polymer Surfaces

Condensation and evaporation

Condensation and evaporation mass flux

Condensation, Evaporation, and Dynamic Equilibrium

Controlling the Growth Speed Evaporation Rate and Temperature Dependence

Cooling and evaporation

Design of Evaporators and Condensers

Distillation and evaporation

Drop evaporation theory for spherical and ellipsoidal drops

Droplet Deformation and Evaporation on a Hot Surface

Dynamics and Pattern Formation in Evaporating Polymer Solutions

Dynamics of Evaporators and Separators

Evaporating and Drying

Evaporating and Drying Equipment

Evaporation and Condensation of Liquids

Evaporation and Crystallization

Evaporation and Growth

Evaporation and Precipitation Balance

Evaporation and Sputtering

Evaporation and Vaporization

Evaporation and condensation during

Evaporation and condensation effects

Evaporative drying principles and practice

Evaporator Base Sections and Accumulators

Evaporator Types and Applications

Evaporators backward and forward feed

Eyre North and South monthly evaporation rates

Film Deposition by Evaporation and Condensation in High Vacuum

Flash and Evaporation

Flash and evaporation models

Forest Evaporation, Tree Life Form and Nitrogen

General mass burning considerations and the evaporation coefficient

Heat Integration of Evaporators and Dryers

Heat Integration of Evaporators and Dryers—Summary

Heat of Liquid Surface Formation and Evaporation

Heat of Surface Formation and Evaporation

Heat transfer in nucleate boiling and convective evaporation

Isotopic Fractionation During Evaporation and Some Hydrological Applications

Liquids evaporation and

Loss of plasticizer from material due to the chemical decomposition reactions and evaporation

Melting and evaporation

Methanol Evaporator and Hydrogen Combustor

Non-evaporable and bound water

Phase evaporation and

Pressure and Rate of Evaporation (Total)

Refining and Evaporation

Refrigeration evaporation and

Shrinkage, swelling and evaporation

Solute and evaporation

Surface Evaporation Mass Flux and Bulk Superheat

Surface Evaporation of Cryogenic Liquids, Including LNG and LPG

Surface Evaporation, the Only Way of Dissipating Superheat and Thermal Overfill

Temperature evaporation and

Thermal processing annealing and evaporation

Transport phenomena, evaporation, and

Transport phenomena, evaporation, and thermal stability

Types of Evaporation Equipment and Operation Methods

Urea Thermolysis and Evaporation

Verification Liquidation and Evaporation

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