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Nucleation chemical

PloB, R. and Mersmann, A., 1989. A New Model of the Effect of Stirring Intensity on the Rate of Secondary Nucleation. Chemical Engineering Technology, 12, 137-146. [Pg.318]

Polymer blends and alloys have more complex behavior in the presence of fillers than the binary mixtures of polymer and filler. The same factors, such as filler distribution, filler-matrix interaction, filler-matrix adhesion, particle orientation, nucleation, chemical reactivity, etc. have influence on properties, but this influence is complicated by the fact that there are two or more polymers present which compete for the same filler particles. These complex interactions result in many interesting phenomena discussed below. [Pg.717]

Another technique proposed for the inside process is plasma chemical vapor deposition (PCVD). In this version of the process, a low-pressure plasma is generated inside the tube that does not lead to soot generation, but rather allows a heterogeneously nucleated chemical reaction to occur at the inner surface of the tube, so that the glass is built up in molecular-scale layers. This is a true chemical vapor deposition (CVD) process. More layers are required than with soot, but the process can be controlled more precisely. Unfortunately, the process has not yet proved commercially economical. [Pg.519]

An increase in the time required to form a visible precipitate under conditions of low RSS is a consequence of both a slow rate of nucleation and a steady decrease in RSS as the precipitate forms. One solution to the latter problem is to chemically generate the precipitant in solution as the product of a slow chemical reaction. This maintains the RSS at an effectively constant level. The precipitate initially forms under conditions of low RSS, leading to the nucleation of a limited number of particles. As additional precipitant is created, nucleation is eventually superseded by particle growth. This process is called homogeneous precipitation. ... [Pg.241]

Wet preparation of red iron oxides can involve either a hydrothermal process (see Hydrothermal processing) or a direct precipitation and growth of iron oxide particles on specially prepared nucleating seeds of Fe202- In the hydrothermal process, iron(II) salt is chemically oxidized to iron(III) salt, which is further treated by alkahes to precipitate a hydrated iron(III) oxide gel. The gel can be dehydrated to anhydrous hematite under pressure at a temperature around 150°C. [Pg.12]

Precipitatioa (2,13—17) techniques employ a combination of nucleation and growth iaduced by adding a chemical precipitant, or by changing the temperature and/or pressure of the solution. Chemical homogeneity is controlled by controlling the rate of precipitation. FFeterogeneous precipitation iavolves the precipitation of a soHd of different composition from the solution, and the composition of the precipitate may change as precipitation continues. Coprecipitation iavolves the simultaneous precipitation of similar size cations ia a salt as a soHd solutioa. [Pg.305]

Over the years emphasis has been placed on obtaining greater uniformity in silver haUde crystal size and habit in the grain population, in the behef that the chemical sensitization process can then yield a higher average imaging efficiency. One way of doing this is to adjust the nucleation conditions so... [Pg.468]


See other pages where Nucleation chemical is mentioned: [Pg.373]    [Pg.183]    [Pg.190]    [Pg.157]    [Pg.373]    [Pg.183]    [Pg.190]    [Pg.157]    [Pg.340]    [Pg.526]    [Pg.754]    [Pg.1762]    [Pg.2409]    [Pg.2669]    [Pg.2765]    [Pg.3067]    [Pg.212]    [Pg.259]    [Pg.373]    [Pg.208]    [Pg.289]    [Pg.290]    [Pg.290]    [Pg.290]    [Pg.321]    [Pg.322]    [Pg.325]    [Pg.325]    [Pg.499]    [Pg.172]    [Pg.178]    [Pg.448]    [Pg.452]    [Pg.452]    [Pg.455]    [Pg.135]    [Pg.293]    [Pg.47]    [Pg.41]    [Pg.507]    [Pg.527]    [Pg.521]    [Pg.529]    [Pg.345]    [Pg.346]    [Pg.383]    [Pg.395]    [Pg.400]   
See also in sourсe #XX -- [ Pg.244 , Pg.249 ]




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