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Shaped face temperature

Whereas the OVD, PCVD, and MCVD processes build a refractive index profile layer by layer, the VAD process uses gaseous constituents in the flame to control the shape and temperature distribution across the face of the growing soot boule. [Pg.256]

Installed alone as a semi-refractory material, the foamed borosilicate glass block lining withstands hot face temperatures up to 960°F. It may also be used with refractory, chemical-resistant masonry or monolithic internal linings at temperatures above 960°F providing a unique combination of corrosion protection and heat conservation with little added weight and a lesser overall lining thickness. The foamed glass block may also be fabricated into nozzles, T-sec-tions, elbows, liner inserts and other custom shapes. [Pg.192]

Figures 9,10 show the effect of disc size on minimum film thickness and maximum local face temperature. The disc size has a negligible effect on performance below 4 MPa, but sudden collapse occurs above 4 MPa with the smaller disc supports. This Is due to excessive thermal crowning. The "failure" occurs by a ratcheting mechanism in which the Inefficient film shape causes excessive heating, which causes further crowning. The thermal and elastic deformations can be made to cancel using larger diameter disc supports (curves c,d In Figs. 9,10). Figures 9,10 show the effect of disc size on minimum film thickness and maximum local face temperature. The disc size has a negligible effect on performance below 4 MPa, but sudden collapse occurs above 4 MPa with the smaller disc supports. This Is due to excessive thermal crowning. The "failure" occurs by a ratcheting mechanism in which the Inefficient film shape causes excessive heating, which causes further crowning. The thermal and elastic deformations can be made to cancel using larger diameter disc supports (curves c,d In Figs. 9,10).
Figure 11 shows isobars of. face temperature, pressure and film thickness for a small disc (A/B = 0.08) at P = 4.34 MPa and for a large disc (A/B 0.91) at P 6.42 MPa. For the case of the small disc, the crowning Is excessive, giving a most Inefficient film shape as shown by the Isobars for pressure. A very small increase in load will cause complete collapse. With the larger disc, the crowning is moderate and the pressure distribution is more efficient... [Pg.102]

Crystal Morphology. Size, shape, color, and impurities are dependent on the conditions of synthesis (14—17). Lower temperatures favor dark colored, less pure crystals higher temperatures promote paler, purer crystals. Low pressures (5 GPa) and temperatures favor the development of cube faces, whereas higher pressures and temperatures produce octahedral faces. Nucleation and growth rates increase rapidly as the process pressure is raised above the diamond—graphite equiUbrium pressure. [Pg.563]

In the Premier Mill the rotor is shaped hke the frustrum of a cone, similar to that in Fig. 20-53. Surfaces are smooth, and adjustment of the clearance can be made from 25 [Lm (0.001 in) upward. A small impeller helps to feed material into the rotor gap. The mill is jacketed for temperature control. Direct-connected hquid-type mills are available with 15- to 38-cm (6- to 15-in) rotors. These mills operate at 3600 r/min at capacities up to 2 mVh (500 gal/h). They are powered with up to 28 kW (40 hp). Working parts are made of Invar alloy, which does not expand enough to change the grinding gap if heating occurs. The rotor is faced with Stellite or silicon carbide tor wear resistance. For pilot-plant operations, the Premier Mill is available with 7.5- and 10-cm (3- and 4-in) rotors. These mills are belt-driven and operate at 7200 to 17,000 r/min with capacities of 0,02 to 2 mVh (5 to 50 gal/h). [Pg.1864]

Where heat transfer is taking place at the saturation temperature of a fluid, evaporation or condensation (mass transfer) will occur at the interface, depending on the direction of heat flow. In such cases, the convective heat transfer of the fluid is accompanied by conduction at the surface to or from a thin layer in the liquid state. Since the latent heat and density of fluids are much greater than the sensible heat and density of the vapour, the rates of heat transfer are considerably higher. The process can be improved by shaping the heat exchanger face (where this is a solid) to improve the drainage of condensate or the escape of bubbles of vapour. The total heat transfer will be the sum of the two components. [Pg.12]

Crystals composed of the R and S enantiomers of the same racemic mixture must be related by mirror symmetry in terms of both their internal structure and external shape. Enantiomorphous crystals may be sorted visually only if the crystals develop recognizable hemihedral faces. [Opposite (hid) and (hkl) crystal faces are hemihedral if their surface structures are not related to each other by symmetry other than translation, in which case the crystal structure is polar along a vector joining the two faces. Under such circumstances the hemihedral (hkl) and (hkl) faces may not be morphologically equivalent.] It is well known that Pasteur s discovery of enantiomorphism through die asymmetric shape of die crystals of racemic sodium ammonium tartrate was due in part to a confluence of favorable circumstances. In the cold climate of Paris, Pasteur obtained crystals in the form of conglomerates. These crystals were large and exhibited easily seen hemihedral faces. In contrast, at temperatures above 27°C sodium ammonium tartrate forms a racemic compound. [Pg.18]


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See also in sourсe #XX -- [ Pg.217 ]




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