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Four-layer particles

One final example of multiple layer MPL was presented by Karman, Cindrella, and Munukutla [172]. A four-layer MPL was fabricated by using nanofibrous carbon, nanochain Pureblack carbon, PIPE, and a hydrophilic inorganic oxide (fumed silica). The first three layers were made out of mixtures of the nanofibrous carbon, Pureblack, carbon, and PTFE. Each of these three layers had different quantities from the three particles used. The fourth layer consisted of Pureblack carbon, PTPE, and fumed silica to retain moisture content to keep the membrane humidified. Therefore, by using these four layers, a porosity gradient was created that significantly improved the gas diffusion through the MEA. In addition, a fuel cell with this novel MPL showed little performance differences when operated at various humidity conditions. [Pg.246]

These diagrams demonstrate that the SMNs should be well dispersed in the continuous phase, monodis-perse, and small in size. This can be visualized if one assumes that the SMNs in the diagrams are 5 nm particles. Thus, there would be four layers of particles between the dispersed phase regions. If one replaces the 5 nm particles with 20 nm particles, then a single 20 nm particle will essentially take up the same space (linearly) as four 5nm particles. Replacing the 5nm particles with 20 nm particles makes the path to coalesce or flocculation less tortuous. Also, at equal weights of particles, there are fewer 20 nm particles than 5 nm particles. It is well known that the viscosity... [Pg.1804]

Nucleation is a crucial step in the whole process of carbonaceous particle formation. According to Frenklach and Wang (1990, 1994), nucleation is controlled mainly by the sticking of PAH sheets during their collisions. Physically bound clusters of PAH are then formed and successively evolve toward aerosol, solid particles and crystallites. As shown in Fig. 25, different polycyclic aromatic layers can form more or less regularly ordered graphite structures, all of which have interlayer distances of about 0.35 nm. These two to four-layer structures are assumed as the threshold of the formation of the solid phase particle inception typically takes place at molecular masses of 1,000-2,000 amu. [Pg.122]

Fissile materials are contained in small particles coated with three or four layers of PyC and SiC, thus making reprocessing to extract pure fissile materials by aqueous methods difficult ... [Pg.327]

Apart firom this internal swelling, swelling between particles can also exist. Kao-linitic clays e.g. show swelling without detectable changes in the lattice and in mont-morillonitc the swelling may proceed much farther than corresponds to the uptake of the four layers of water that are indicated by X-ray diffraction... [Pg.362]

Flotation. Flotation (qv) is used alone or in combination with washing and cleaning to deink office paper and mixtures of old newsprint and old magazines (26). An effective flotation process must fulfill four functions. (/) The process must efficiently entrain air. Air bubble diameter is about 1000 p.m. Typically air bubbles occupy 25—60% of the flotation cell volume. Increa sing the airRquid ratio in the flotation cell is said to improve ink removal efficiency (27). (2) Ink must attach to air bubbles. This is primarily a function of surfactant chemistry. Air bubbles must have sufficient residence time in the cell for ink attachment to occur. (3) There must be minimal trapping of cellulose fibers in the froth layer. This depends on both cell design and surfactant chemistry. (4) The froth layer must be separated from the pulp slurry before too many air bubbles coUapse and return ink particles to the pulp slurry. [Pg.8]

Where there is available ground and the specific resistivity of soil in the upper layers is low, the anodes are laid horizontally [3]. A trench 0.3 to 0.5 m wide and 1.5 to 1.8 m deep is dug with, for example, an excavator or trench digger (see Fig. 9-2). A layer of coke 0.2-m thick is laid on the bottom of the trench. The impressed current anodes are placed on this and covered with a 0.2-m layer of coke. Finally the trench is filled with the excavated soil. No. IV coke with a particle size of 5 to 15 mm and specific gravity of 0.6 t m" is backfilled at a rate of 50 kg per meter of trench. The anodes are connected in parallel and every three to four anode cables are connected to the anode header cable by a mechanical cable crimp encapsulated in an epoxy splice kit to give an economical service life at high current output. [Pg.244]

Transfer matrix calculations of the adsorbate chemical potential have been done for up to four sites (ontop, bridge, hollow, etc.) or four states per unit cell, and for 2-, 3-, and 4-body interactions up to fifth neighbor on primitive lattices. Here the various states can correspond to quite different physical systems. Thus a 3-state, 1-site system may be a two-component adsorbate, e.g., atoms and their diatomic molecules on the surface, for which the occupations on a site are no particles, an atom, or a molecule. On the other hand, the three states could correspond to a molecular species with two bond orientations, perpendicular and tilted, with respect to the surface. An -state system could also be an ( - 1) layer system with ontop stacking. The construction of the transfer matrices and associated numerical procedures are essentially the same for these systems, and such calculations are done routinely [33]. If there are two or more non-reacting (but interacting) species on the surface then the partial coverages depend on the chemical potentials specified for each species. [Pg.452]

SynChropak size exclusion supports are composed of spherical uniformly porous silica that has been derivatized with a suitable layer. SynChropak GPC supports are available in six pore diameters ranging from 50 to 4000 A and particle diameters from 5 to 10 /zm. SynChropak CATSEC supports are available in four pore diameters. Table 10.1 details the physical characteristics of the product lines. [Pg.306]


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See also in sourсe #XX -- [ Pg.673 ]




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