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Filling densities

Photoelectron spectroscopy provides a direct measure of the filled density of states of a solid. The kinetic energy distribution of the electrons that are emitted via the photoelectric effect when a sample is exposed to a monocluomatic ultraviolet (UV) or x-ray beam yields a photoelectron spectrum. Photoelectron spectroscopy not only provides the atomic composition, but also infonnation conceming the chemical enviromnent of the atoms in the near-surface region. Thus, it is probably the most popular and usefiil surface analysis teclmique. There are a number of fonus of photoelectron spectroscopy in conuuon use. [Pg.307]

As shown in Figures 1.36(a) and 1.36(b), the glycine nitrate process-derived powder is highly porous. The pore size ranges from tens of nanometers to several micrometers. The powder is thus named as foam powder, which shows extremely low fill densities of less than 1/100 of the theoretical density value. The low fill density makes it possible to prepare thin films of doped ceria by dry pressing, in which the films are processed by means of punches in a hardened metal die. Figures 1.36(c) and 1.36(d) show a cross-sectional view of an 8 /tm-thick GDC film fabricated by dry pressing. [Pg.46]

Arkhipov VI, Heremans P, Emelianova EV, Adriaenssens GJ, Bassler H (2002) Weak-field carrier hopping in disordered organic semiconductors the effects of deep traps and partly filled density-of-states distribution. J Phys Condens Matter 14 9899... [Pg.61]

The bulk density of the powder inside the die is called the fill density, Djm. A high fill density reduces both the air content in the powder and the distance the punch needs to travel to further compress the powder during pressing. Poor powder flowability... [Pg.711]

Particle Size (pm) Organics (vol%) Granule Size (pm) Granule Density (%) Fill Density (%)... [Pg.714]

For most ceramic pressing, a CR < 2.0 is desired since it rednces both the punch displacement and the compressed air in the compact. As indicated in Eq. (7.15), a high fill density leads to a low CR. For comparison, the CR in metal powder pressing is typically much greater than 2.0 dne to the dnctility of the particles. [Pg.715]

The amount of the material loaded into the container is 1.8 kg what corresponds to the filling density of 3 g/cm3. [Pg.379]

The filled capillary tnbes are monnted in a weU-stirred, temperature-regulated water bath that can be warmed or cooled and whose temperature can be measured accurately. If a tube contains less than a critical amonnt of CO2, the meniscus between the liquid and vapor will fall toward the bottom of the tube on warming. At a certain temperature, say To, the meniscus in a given tnbe will reach the bottom thus the filling density in that tube will equal the density of the satnrated vapor at the temperature Tq. This density is the total mass of CO2 in the tnbe (which is known) divided by the internal volume of the tube (= cross-sectional area X length of capillary). [Pg.230]

Fixation of other finishes, for example stiffening with water-soluble hand builders Fabrics with low warp and fill densities, knitted dress fabrics, denim articles, mattress duck, awning fabrics... [Pg.52]

The ASTM method is based on using liquid systems to fill density-gradient columns, or tubes. Examples of such liquid systems are shown in Table 6.15. [Pg.220]

Temperature of thermal treatment, °C Filling density, g/cm3 Pycnometric density, g/cm3 Specific surface, m2/g Crystallite size, nm... [Pg.348]

The performance of the ACF solvent recovery process can be summarized as follows Since ACF has lager surface area and smaller bulk density than particulate activated carbon, PAC, ACF s filling density becomes 1/10 of PAC s. [Pg.1551]

The f omula is valid in linear approximation of ideal incompressible liquid as well as in the case of long waves. Let us apply this expression to our case. Taking into account the curve existence relation as well as the fact that at critical filling density the layer heights are equal h - fin and pi -+Ph = BPa after substitung in (2) we obtain... [Pg.241]

The main problem with the density bottle method was eliminating any air entrained on the fiber and many techniques were used to effect removal including centrifuging, the application of vacuum in a desiccator and ultrasonics. Another problem was that technicians tended to carry the filled density bottle by the neck and the warmth of their fingers was sufficient to expand the solvent, with immediate loss through the capillary stopper en-route to the balance room. The solution was to fold a filter paper and wrap around the density bottle neck, gripping the ends of the folded paper. [Pg.663]

After the acquisition of Enpac in 1998 and the subsequent agreement with Novamont, National Starch is licensing two technologies for the production of loose fills one from hydroxypropilated high amylose starch and a second from almost unmodified starch. The loose fills densities range from 6 to 10 kg/m. The main licensees are Unisource, American Excelsior, Storopack, and Flow Pack in the United States. [Pg.7812]


See other pages where Filling densities is mentioned: [Pg.33]    [Pg.713]    [Pg.715]    [Pg.716]    [Pg.12]    [Pg.231]    [Pg.44]    [Pg.621]    [Pg.1213]    [Pg.325]    [Pg.856]    [Pg.1338]    [Pg.411]    [Pg.135]    [Pg.84]    [Pg.382]    [Pg.299]    [Pg.480]    [Pg.239]    [Pg.852]    [Pg.865]    [Pg.872]    [Pg.358]    [Pg.109]    [Pg.110]    [Pg.116]    [Pg.125]    [Pg.130]    [Pg.131]    [Pg.133]    [Pg.176]    [Pg.292]    [Pg.399]   


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