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Layers lower

Polysilicon. Polysihcon is used as the gate electrode material in MOS devices, as a conducting material for multilevel metallization, and as contact material for devices having shallow junctions. It is prepared by pyrolyzing silane, SiH, at 575—650°C in a low pressure reactor. The temperature of the process affects the properties of the final film. Higher process temperatures increase the deposition rate, but degrade the uniformity of the layer. Lower temperatures may improve the uniformity, but reduce the throughput to an impractical level. [Pg.348]

Boiling poiat of azeotrope, °C Alcohol ia azeotrope, wt % Upper layer Lower layer... [Pg.371]

A 100-200-mL volume of 5% NaCl aqueous solution and 100 mL of n-hexane are added to the extracts prepared in Section 2.2.1, and the mixed solution is shaken vigorously for 5 min. The n-hexane layer is separated and a further 50 mL of n-hexane are added to the aqueous layer (lower layer) and shaken again. The n-hexane layers are collected, dehydrated with ca 20 g of anhydrous Na2S04, and concentrated using a vacuum rotary evaporator below 40 °C, and the residue is dried under a gentle stream of pure nitrogen and dissolved in ca 20 mL of n-hexane. [Pg.454]

Once again separate the chloroform layer (lower) and measure its absorbance in a 1 cm absorption cell at 520 nm Vs an identically treated blank, and... [Pg.407]

Figure 3.8 A, Schematic structure of porous stationary phase a, support b, bonded phase and c, adsorbed solvent layer. B, detailed view of eluent components in surface layer , lower phase molecules Q, upper phase molecules. Figure 3.8 A, Schematic structure of porous stationary phase a, support b, bonded phase and c, adsorbed solvent layer. B, detailed view of eluent components in surface layer , lower phase molecules Q, upper phase molecules.
Now let us examine some of the properties of the spread monolayer that we have described. It was seen in the preceding chapter (e.g., Equation (6.48)) that the presence of an adsorbed layer lowers the surface tension of an interface. The phenomenon is quite general, so we redefine tt (no subscript) in the following symbols ... [Pg.301]

Crude methyl 4-(ferf-butoxycarbonylamino)-l-methylpyrrole-2-carboxylate (6) from the previous step was dissolved in MeOH (700 mL) 2M NaOH (700 mL) was added and the soln was heated at 60 °C for 6h. The mixture was cooled to rt and washed with Et20 (4x1 L), the pH of the aqueous layer lowered to ca. 3 with 10% H2S04, and the mixture was extracted with EtOAc (4 x 2000 mL). The combined EtOAc extracts were dried (Na2S04) and concentrated under reduced pressure to provide a tan foam. The foam was dissolved in CH2C12 (500 mL) and petroleum ether (2 L) added, and the resulting slurry was concentrated. The residue was redissolved and concentrated three additional times to provide 7 as a fine white powder yield 320 g (75% from 5). [Pg.665]

Fig. 12 Layer and director structure in 2D phases which occur due to the preference of the system to polarization splay. Upper line, side view on the layer lower line, top view on the layer. Red arrows show the polar director. Blue nails show the projection of the nematic director to the smectic plane. There is no blue nail in the centre of the wall, meaning that the cone angle is reduced to zero... Fig. 12 Layer and director structure in 2D phases which occur due to the preference of the system to polarization splay. Upper line, side view on the layer lower line, top view on the layer. Red arrows show the polar director. Blue nails show the projection of the nematic director to the smectic plane. There is no blue nail in the centre of the wall, meaning that the cone angle is reduced to zero...
Insoluble polar molecules (e.g., long chain fatty acids) exhibit an extreme kind of adsorption at liquid surfaces. That is, they can be made to concentrate in one molecular layer at the surface. These interfacial films often provide the stabilizing influence in emulsions since they can both lower interfacial tension and increase the interfacial viscosity. The latter provides a mechanical resistance to coalescence. Such systems also lend themselves to the study of size, shape, and orientation of molecules at an interface. Having an adsorbed layer lowers the surface tension (to Ysolution) by the surface pressure jt= ysoivent - y solution as already noted. [Pg.79]

When the anode is first charged, it slowly approaches the lithium potential and begins to react with the electrolyte to form a film on the surface of the electrode. This film is composed of products resulting from the reduction reactions of the anode with the electrolyte. This film is called the solid electrolyte interphase (SEI) layer [30], Proper formation of the SEI layer is essential to good performance [31-34], A low surface area is desirable for all anode materials to minimize the first charge related to the formation of SEI layer. Since the lithium in the cell comes from the lithium in the active cathode materials, any loss by formation of the SEI layer lowers the cell capacity. As a result, preferred anode materials are those with a low Brunauer, Emmett, and Teller (BET) surface area... [Pg.424]

Surrounding the core, the mantle has a thickness of about 2900 km. Its mass is estimated at 4 x 1024 kg. It is composed mainly of high-density silicates of Mg and Fe. It is divided into three layers lower (2000 km), transition (500 km), and upper mantle (360 km). The lower mantle is predominantly formed by Mg-perovskite, Mg-wurstite, and Ca-perovskite, which contain water in their crystal structures. Incredibly as it may seem, because of this water content the lower mantle is believed to contain more water than the oceans. [Pg.78]

Point Compound Azeo. Temp. Azeo. Vapors Upper Layers Lower Layers Volume, °/o ... [Pg.121]

In porous composite membranes, the support layer(s) can play an important role in the reactor performance. This, for example, is the case with consecutive reactions such as partial oxidations where intermediate products are desirable. Harold et al. [1992] presented a concept in which two reactants are introduced to a two-layer membrane system from opposite sides ethylene on the membrane side while oxygen on the support side. The mass transfer resistance of the support layer lowers the oxygen concentration in the catalytic zone and directs the preferred intermediate product, acetaldehyde, toward the membrane side. Thus the support layer structure enhances the yield of acetaldehyde. [Pg.390]

Figure 2 A high-resolution TEM photomicrograph of the amorphous altered layer (lower left) developed on crystalhne lahradorite (hulk material, upper right) after dissolution at pH 1. The hlurry lattice fringes at the interface reflect the varying boundary orientation with respect to the ultrathin section. Interface thickness is 0.5-2 nm. Energy filtered (EE) TEM was also used to chentically characterize the alteration zone, which was found to he depleted in Ca, Na, K, and Al, and enriched in H, O, and Si. The sharp structural interface shown here and the sharp chemical interface observed with EFTEM are interpreted by the authors to indicate that the alteration layer is formed by dissolution-precipitation. Such amorphous altered layers are often high in porosity and yield high BET surface areas (reproduced by permission of Springer from Phys. Figure 2 A high-resolution TEM photomicrograph of the amorphous altered layer (lower left) developed on crystalhne lahradorite (hulk material, upper right) after dissolution at pH 1. The hlurry lattice fringes at the interface reflect the varying boundary orientation with respect to the ultrathin section. Interface thickness is 0.5-2 nm. Energy filtered (EE) TEM was also used to chentically characterize the alteration zone, which was found to he depleted in Ca, Na, K, and Al, and enriched in H, O, and Si. The sharp structural interface shown here and the sharp chemical interface observed with EFTEM are interpreted by the authors to indicate that the alteration layer is formed by dissolution-precipitation. Such amorphous altered layers are often high in porosity and yield high BET surface areas (reproduced by permission of Springer from Phys.
The process is shown diagrammatically in Fig. 4-16 for a case in which the distribution coefficient is unity and equal volumes of solution and extracting solvent are used. Each box represents one funnel, and the numbers inside the box give the concentration of the solute in the upper layer (upper number) and the lower layer (lower number) at equilibrium. The numbers on the side indicate which series of extractions is referred to, and the arrows represent the transfer of the lower layer after equilibration. Thus, in the first series, the solute is partitioned between the two solvents in the first funnel, the lower layer is transferred to funnel 2, and fresh solvent is added to funnel 1. In the second series, the lower layer of funnel 2 (containing 0.188 of the solute) is transferred to funnel 3, that of funnel 1 is transferred to funnel 2, and fresh solvent is added to funnel 1. This is continued as shown, and the lower layers from funnel 4 are collected next. After the operation has been completed, 0.727 of the solute will be in this solution. [Pg.185]

Figure 4 on the right shows the average over potential in the region 0 < z < 30m of the casing for different electrolyte conductivity of the first layer. Lower conductivity in the subsurface layer translates into more negative over potentials. [Pg.52]

Figure 21. In situ image showing potential induced formation of iodide layer. Lower part of frame presents the Au(llO) pattern, and upper part of frame presents ordered iodide layer alter potential change. Reprinted with permission from Ref. 200, Copyright (1995) American Chemical Society. Figure 21. In situ image showing potential induced formation of iodide layer. Lower part of frame presents the Au(llO) pattern, and upper part of frame presents ordered iodide layer alter potential change. Reprinted with permission from Ref. 200, Copyright (1995) American Chemical Society.

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