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Ostwald

German silver, platinoid, or manganin, the last is the best on account of its low temperature coefficient. The wire must be calibrated. For high resistances (itooo-200,000 Ohms) the special form of resistance [Pg.54]

The apparatus is arranged in the form of Kirchhoff s modification of the Wlieatstone bridge (Fig. 8), the connections being made with stout copper wire. The induction coil is enclosed in a sound tight case, or is [Pg.56]

The value of k is determined by measuring the conductivity of N/50 solution of potassium chloride, for which Kohlrausch found the values  [Pg.57]

A method has been described for determining the basicity of acids based on the alterations which they exhibit in electrolytic conductivity on the addition of alkali. Instead of the telephone and induction coil, a double [Pg.58]

A neat form of apparatus much smaller than Kohl-rausch s, consists of an ebonite cup and rod fitted with platinum electrodes prepared in the usual manner. The rod can be moved vertically over the cup by means of micrometer screws, and the distance between the electrodes read off on a divided scale by a vernier. Quantities of solutions as small as 3 cc maybe employed. [Pg.58]


Ostwald ripeniDg A process of crystal growth in which a mixture of coarse and fine crystals of a substance are left in contact with a solvent. This results in a growth of the large crystals and the ultimate disappearance of the fine crystals. [Pg.291]

At equilibrium, crystal growth and dissolving rates become equal, and the process of Ostwald ripening may now appear, in which the larger crystals grow at the expense of the smaller ones. The kinetics of the process has been studied (see Ref. 103). [Pg.341]

In principle, then, small crystals should show a higher solubility in a given solvent than should large ones. A corollary is that a mass of small crystals should eventually recrystallize to a single crystal (see Ostwald ripening. Section IX-4). [Pg.348]

A3.3.4 LATE-STAGE GROWTH KINETICS AND OSTWALD RIPENING... [Pg.745]

Eigen M 1996 Die unmessbar schnellen Reaktionen (Ostwalds Klassiker der exakten Naturwissenschaften) vol 281 (Thun und Frankfurt Harri Deutsch)... [Pg.2146]

A definition of catalysis similar to that given above was stated first in about 1895 by Wilhelm Ostwald, whose work on catalysis was recognized with a Nobel prize. Sixty years before, Jakob Berzelius had coined the tenn... [Pg.2697]

Since zeolites are metastable crystallization products tliey are subject to Ostwald s mle which states tliat metastable phases are initially foniied and gradually transfonii into tlie tlieniiodynaniically most stable product. The least stable zeolitic phase (tliat witli tlie lowest framework density) is tlierefore foniied first and consumed with furtlier syntliesis time at tlie expense of a more stable phase due to a continuous crystallization/redissolution equilibrium. [Pg.2783]

Ostwald W 1917 Theoretical and Applied Colloid Chemistry (London Chapman and Hall)... [Pg.2914]

A common choice of functional relationship between shear viscosity and shear rate, that u.sually gives a good prediction for the shear thinning region in pseudoplastic fluids, is the power law model proposed by de Waele (1923) and Ostwald (1925). This model is written as the following equation... [Pg.6]

The basic design is that of the Ostwald viscometer a U-tube with two reservoir bulbs separated by a capillary, as shown in Figure 24a. The Hquid is added to the viscometer, pulled into the upper reservoir by suction, and then allowed to drain by gravity back into the lower reservoir. The time that it takes for the Hquid to pass between two etched marks, one above and one below the upper reservoir, is a measure of the viscosity. In U-tube viscometers, the effective pressure head and therefore the flow time depend on the volume of Hquid in the instmment. Hence, the conditions must be the same for each measurement. [Pg.180]

Fig. 24. (a) Ostwald glass capillary viscometer, (b) Cannon-Fenske viscometer, and (c) Ubbelohde viscometer. [Pg.180]

The original Ostwald viscometer has been modified in many ways, and a number of different versions are on the market (Table 4) (21). Most are available with a wide choice of capillary diameters and therefore a number of viscosity ranges. A number of viscometers are described in ASTM D445, which also Hsts detailed recommendations on dimensions and methods of use. [Pg.180]

Measured ia 95% ethanol at 25°C usiag an Ostwald-Cannon-Fenske viscometer. [Pg.451]

A catalyst is a substance that iacreases the rate of approach to equiUbrium of a chemical reaction without being substantially consumed itself. A catalyst changes the rate but not the equiUbrium of the reaction. This definition is almost the same as that given by Ostwald ia 1895. The term catalysis was coiaed ia ca 1835 by Ber2eHus, who recognized that many seemingly disparate phenomena could be described by a single concept. For example, ferments added ia small amounts were known to make possible the conversion of plant materials iato alcohol and there were numerous examples of both decomposition and synthesis reactions that were apparendy caused by addition of various Hquids or by contact with various soHds. [Pg.160]

E. Jacobson, Basic Color. An Interpretation of the Ostwald Color System, P. Theobald, Chicago, lU., 1948. [Pg.424]

A further problem is possible if the reinforcements are very small. Coarsening of the particles or whiskers may occur driven by Ostwald ripening, in which large particles grow through diffusional transport at the expense of smaller ones. This can be minimized by choosing matrices in which the reinforcement elements have very low solid solubilities and diffusion coefficients. Platelets, however, have been shown to be more resistant to coarsening than particles or whiskers. [Pg.58]

P. E. Ostwald, Engineering Cost Estimating 3rd ed., Prentice-Had, Englewood Cliffs, N.J., 1992. [Pg.452]

There aie a number of major indusuial problems in the operation of the steam reforming of metlrane. These include the formation of carbon on the surface of the catalyst, the sulphidation of the catalyst by the H2S impurity in commercial natural gas, and die decline of catalytic activity due to Ostwald ripening of the supported catalyst particles by migration of catalyst atoms from the smaller to tire larger particles, as the temperamre is increased. A consideration of tire thermodynamics of the principal reaction alone would suggest that the reaction shifts more favourably to the completion of the reaction as the temperature is increased. [Pg.131]

Greenwood (1956) described the behaviour of an assembly of n groups of particles undergoing Ostwald ripening by solution-diffusion controlled transfer between particles according to a general relationship... [Pg.209]

Figure 6.7 The model for atom transfer during Ostwald ripening, showing the flux of atoms from the smaller particle to the larger... Figure 6.7 The model for atom transfer during Ostwald ripening, showing the flux of atoms from the smaller particle to the larger...
In the total particle size distribution, some particles of small diameter decrease in radius, and those in the larger diameter range increase in radius during Ostwald ripening. There will therefore be a radius at which particles neither decrease nor grow in size and if [Pg.210]


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Acid-Base Equilibria in Water Ostwalds Dilution Law

Affinity Ostwald

Ageing and Ostwald ripening

Aging Ostwald ripening

Alloys Ostwald ripening

Ammonia Ostwald process

Ammonia oxidation Ostwald process

Arrhenius-Ostwald acid-base theory

Catalyst degradation Ostwald ripening

Coarsening Ostwald ripening

Colloidal Ostwald ripening

Crystal Growth (Ostwald Ripening)

Droplet size Ostwald ripening

Effect of Ostwald Ripening on Initial Droplet Size

Effect of the Interfacial Layer in Slowing Ostwald Ripening

Electrochemical Ostwald ripening

Emulsion polymerization Ostwald ripening

Emulsion polymerization Ostwald ripening effect

Energetics Ostwald

Entropy Ostwald

Experimental determination of the dissociation equilibrium constant. Ostwalds dilution law

Freundlich-Ostwald-Boedecker (FOB)

Gases Ostwald solubility coefficient

Gibbs-Freundlich-Ostwald equation

Growth Ostwald ripening

Heterogeneous reactions Ostwald ripening

Industrial manufacture Ostwald Process

Industrial processes Ostwald process

Irreversible process Ostwald ripening

Kelvin equation Ostwald ripening

Measurements Ostwald ripening

Monolayer Ostwald ripening

Nano Ostwald ripening

Nano-emulsions Ostwald ripening

Nanoparticle Ostwald ripening

Nitric Acid Ostwald

Nitric acid Ostwald process

Nitric acid manufacture Ostwald Process

Nobel Prize winners Ostwald

Nucleation Ostwald limit

Of Ostwald

Ostwald 1902 ammonia oxidation

Ostwald Ripening (Disproportionation)

Ostwald Ripening in Emulsions Containing Two Disperse Phase Components

Ostwald absorption coefficient

Ostwald ammonia synthesis

Ostwald application

Ostwald assessment

Ostwald biography

Ostwald coefficient

Ostwald coefficient Table)

Ostwald complexes

Ostwald convention

Ostwald de-Waale

Ostwald dilution law

Ostwald energetic chemistry

Ostwald energetic theory

Ostwald flocculation assessment

Ostwald growth laws

Ostwald isolation method

Ostwald measurements

Ostwald method

Ostwald nanoemulsions

Ostwald ous

Ostwald ous suffix

Ostwald prevention

Ostwald process

Ostwald process (manufacture

Ostwald process pharmaceuticals

Ostwald process pollution

Ostwald process polymerization

Ostwald process polymers

Ostwald process porous catalysts

Ostwald process pressure drop

Ostwald process production rate

Ostwald reaction principle

Ostwald ripening

Ostwald ripening and coalescence

Ostwald ripening calculation

Ostwald ripening colloid stability

Ostwald ripening crystals

Ostwald ripening destabilization process

Ostwald ripening drops

Ostwald ripening effect

Ostwald ripening emulsion concentrates

Ostwald ripening emulsions

Ostwald ripening foams

Ostwald ripening fraction

Ostwald ripening liquid-phase sintering

Ostwald ripening mechanism

Ostwald ripening model

Ostwald ripening particle growth

Ostwald ripening particle size distribution

Ostwald ripening polymeric surfactant stabilization

Ostwald ripening polymeric surfactants

Ostwald ripening process

Ostwald ripening silicate

Ostwald ripening stability

Ostwald ripening theory

Ostwald ripening, description

Ostwald ripening, miniemulsion

Ostwald rule

Ostwald rule of stages

Ostwald s Klassiker

Ostwald s, solubility

Ostwald second rule

Ostwald solubility

Ostwald solubility coefficient

Ostwald stage rule

Ostwald step rule

Ostwald systems

Ostwald theory

Ostwald viscometer

Ostwald viscometer capillary

Ostwald viscosimeter

Ostwald, Friedrich

Ostwald, Friedrich Wilhelm

Ostwald, Walter

Ostwald, Wilhelm

Ostwald, Wilhelm color system

Ostwald, William

Ostwald, Wolfgang

Ostwald-Freundlich equation

Ostwald-Volmer rules

Ostwald-de Izaguirre equation

Ostwald-de Waele

Ostwald-de Waele equation

Ostwald-de Waele law

Ostwald-de Waele model

Ostwald-de Waele power law

Ostwald-deWaele

Ostwald-ripening phenomenon

Ostwald’s Step Rule

Ostwald’s dilution law

Ostwald’s isolation method

Ostwald’s law

Ostwald’s law of Dilution

Ostwald’s law of stages

Ostwald’s rule of stages

Ostwald’s rules

Ostwald’s stage rule

Other Ways of Slowing Ostwald Ripening

Physical chemist Ostwald

Platinum catalysts ostwald ripening

Prevention of Ostwald Ripening (Crystal Growth)

Rate of Ostwald ripening

Reversed Ostwald ripening

Stabilization Ostwald ripening

Successive Ostwald rule

Supersaturation Ostwald ripening

Surfaces Ostwald ripening

The Ostwald Process

The Power Law or Ostwald de Waele Model

Time-Dependent Ostwald Ripening

Viscometry Ostwald

Wald and Ostwald

Wilhelm Ostwald process

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