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Mixing horizontal cylinders

Effect of flow direction on the temperature field around a heated cylinder. (From Krause, J.R., "An Interferometric Study of Mixed Convection from a Horizontal Cylinder to a Cross Flow of Air , M.E.Sc. Thesis, The University of Western Ontario. London. Ontario. Canada. 1985. By... [Pg.429]

A fundamental study of solids mixing is given, with experimental data for a rotating horizontal cylinder containing salt and sand. Theoretical random equilibrium mixture, chi-square test, and sampling considerations are discussed. Also rate equations and segregating effects are covered. [Pg.255]

Fig. 38. Relation between degree of mixing and number of revolutions for various conditions of baffling. 20 cm. X 40 cm. horizontal cylinder rotating at 25 rpm. Black and white particles of about 1.3 mm. diameter mixed. Degree of mixing measured photometrically. Total weight of solid is 8 kg. h = height of baffle plate, R = radius of cylinder (04). Fig. 38. Relation between degree of mixing and number of revolutions for various conditions of baffling. 20 cm. X 40 cm. horizontal cylinder rotating at 25 rpm. Black and white particles of about 1.3 mm. diameter mixed. Degree of mixing measured photometrically. Total weight of solid is 8 kg. h = height of baffle plate, R = radius of cylinder (04).
Fig. 43. Axial concentration gradient after a long period of mixing (W2). System —40 to +50 (U.S.) mesh sand and salt in a horizontal cylinder rotating at 45 rpm approximately one-third full. Fig. 43. Axial concentration gradient after a long period of mixing (W2). System —40 to +50 (U.S.) mesh sand and salt in a horizontal cylinder rotating at 45 rpm approximately one-third full.
Horizontal Cylinders. For a heated horizontal cylinder in perpendicular cross flow, the angle of the approaching stream, ( > in Fig. 4.47, greatly affects the heat flow in the mixed convection regime. For ( > = 0 the forced flow assists the natural convection and the dependence of the average Nus-selt number on Re resembles path A in Fig. 4.44. For = 90° there is a sharper transition from natural to forced convection than when 4> = 0, while for opposed flow (( > = 180°) there is a minimum as shown by path B in Fig. 4.44. For a cooled cylinder the same description applies except that ( > is measured from the vertical axis extending upward from the cylinder. [Pg.278]

B. Gebhart and L. Pera, Mixed Convection From Long Horizontal Cylinders, J. Fluid Mech. (45) 49-64,1970. [Pg.293]

Now place 35 ml. of the mixed solvent (C) in the clean cylinder E, and suspend the strip, as described above, to the horizontal arm of G (Fig. 25(A)) adjust the position of the strip so that, when the bung is firmly in position, the bottom of the paper-strip is about 5 mm. above the solvent. Place the cylinder for 5-8 hours in a draught-free place, such as a cupboard, where the temperature is reasonably constant. [Pg.53]

The entire QSL process takes place in a single reactor as shown in Figure 6 (15). The reactor consists of an almost horizontal, refractory-lined cylinder, which can be tilted by 90° when operation is intermpted. Concentrates, fluxes, recirculated flue dust, and normally a small amount of coal, depending on the type of concentrate, are pelletized. The pelletizer ensures that the raw materials are mixed to the required degree of uniformity. [Pg.38]

In another variation of the process, the foaming mix is fed to the bottom of a cylinder and the foaming mixture is pushed upwards (the Vertifoam process). The mass of material above the reacting foam can be used to control density, whilst in addition volatiles and gases find it more difficult to escape from the system. The solidified cylinder of foam may then be sliced horizontally into large discs. [Pg.793]

Consistency is tested on a measured volume of freshly mixed cement in the form of a cylinder. This specimen is placed between two horizontal plates using the apparatus illustrated in Figure 10.1 and subjected to a vertically applied load. The cement then flows out rapidly to form a disc. This radial flow ceases almost instantaneously because the applied stress decreases as the disc expands and rapidly reaches the yield stress, at which point outward flow ceases. This is the behaviour expected for a plastic body. [Pg.378]

For the surface modification of silica and carbon black, a radiofrequency (13.56 MHz) electrode-less tumbler plasma reactor at the University of Cincinnati was used. The schematic reactor design is shown in Fig. 5. It consists of a Pyrex cylinder chamber of 40 cm in length and 20 cm in diameter, with a motor-driven shaft at its center, and two vanes running in opposite directions. The reactor is based on a horizontal mixing principle and is capable of treating 350 g per batch. The powdery materials to be coated are placed at the bottom of the chamber. The plasma... [Pg.181]

PEBBLE MILL. A jacketed steel cylinder rotating on a horizontal axis and containing flint or porcelain pebbles as the grinding medium. Its operation is similar to that of a ball mill. It is used for grinding and mixing of dry chemicals, pigments, food products, and the like. Pebble mills are usually lined with alumina, buhrsione, or similar material to protect the walls from wear. [Pg.1220]


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