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Grinding of materials

Grindability is a measure of the rate of grinding of material in a particular mill (discussed later). [Pg.1828]

Grinding of material takes place over this distance in the grinder... [Pg.125]

Oversize material is returned to the mill for further size reduction. Closed circuit grinding is suitable for either wet or dry grinding of materials. [Pg.2745]

Particulates may be emitted from processing equipments, such as reactors, furnaces, kilns, and dryers from industrial sources or from incineration of municipal and industrial wastes. These may also be generated dnring the crushing and grinding of materials. Spink (1988) has described the use of a Waterloo scrubber for removal of particulates from waste gases. Water droplets 15-20 times the diameter of the particles were injected into the gas stream and a fan provided turbulent mixing to effect interactions between particles and droplets and cause complete removal... [Pg.715]

Grinding of Materials. The mechanical disintegration of a soUd leads to the formation of a new surface. The formation of this surface begins with the rupture of interatomic bonds and is concluded with an ordering of structure of the layer near the surface. As a rule, the formation of the new surface is accompanied by dissipation of excess energy as evidenced by the evolution of heat, the emission of electrons, ions, or neutral particles, luminescence, and other phenomena. [Pg.57]

Equip a 500 ml. three-necked flask with an efficient stirrer (e.g., a Hershberg stirrer. Fig. II, 7, 8) and a reflux condenser stopper the third neck. Place a solution of 30 g. of sodium hydroxide in 100 ml. of water, and also 20-5 g. (17-1 ml.) of pure nitrobenzene in the flask, immerse it in a water bath maintained at 55-60°, and add 21 g. of anhydrous dextrose in small portions, with continuous stirring, during 1 hour. Then heat on a boiUng water bath for 2 hours. Pour the hot mixture into a 1 litre round-bottomed flask and steam distil (Fig. II, 40, 1) to remove aniline and nitrobenzene. When the distillate is clear (i.e., after about 1 htre has been collected), pour the residue into a beaker cooled in an ice bath. The azoxybenzene soon sohdifies. Filter with suction, grind the lumps of azoxybenzene in a mortar, wash with water, and dry upon filter paper or upon a porous plate. The yield of material, m.p. 35-35-5°, is 13 g. Recrystallise from 7 ml. of rectified spirit or of methyl alcohol the m.p. is raised to 36°. ... [Pg.631]

Micropowders are added to a wide variety of material used in industry, where they provide nonstick and sliding properties. They are incorporated into the product by blending and grinding. To disperse weU, the powder must have good flow properties. Conditions that make the powder sticky should be avoided. [Pg.355]

A high, moisture content necessitates finer grinding of coal for rapid water release. For such coals, the classifier in the pulverizer is set to return more of the oversize material for further grinding. [Pg.157]

A wide apphcation of electrochemical grinding is the production of tungsten carbide [12070-12-1] cutting tools (see Carbides Tool materials). ECG is also useful in the grinding of fragile parts such as hypodermic needles and thinwaH tubes. [Pg.311]

Each basic operation can be divided into one or more unit operations. Size reduction involves cnishing and grinding depending on the size of material handled, and these may be carried out in stages. Separations can be either soHds from soHds, based on size or mineral composition, or soHds from Hquids, ie, dewatering (qv). Size separation or classification is an integral part of any flow sheet, not only to meet product size specifications, but also to ensure a narrow size distribution for subsequent minerals separation circuits and to decrease the load and improve the efficiency of size reduction units which are energy intensive. [Pg.394]

Grinding is a continuous process. It may be either wet or dry, but wet grinding (at 50—80% soHds) is most common and requires less power per ton of material ground. Media consumption is significantly higher, however. Wet grinding is also the choice when subsequent processing is wet. In certain... [Pg.397]

Typically, ore bodies are relatively low in iron content. Iron minerals are finely divided in a gangue matrix. Wet grinding is usually required to Hberate the iron minerals, although some beach sands may have Hberated iron mineral values. Wet dmm separators are limited to the treatment of material <10 mm. The magnetic dmm separators appHed are usually related to the grinding circuit required to Hberate the iron mineral, and are typically designated by appHcation as cobbers, roughers, or finishers. [Pg.424]

Roller Mills Pendulum, Table, and Bowl Type. This is a group of machines commonly applied for grinding of mineral powders down to approximately 97% below 75 p.m, or even finer in some instances. The mills operate at medium speed, up to approximately 30 m/s, and can handle materials with up to Mohs hardness 5 before wear rates become prohibitive. Many different designs are available the two most commonly encountered variants are pendulum mills and the table roUer mill. [Pg.142]


See other pages where Grinding of materials is mentioned: [Pg.132]    [Pg.343]    [Pg.343]    [Pg.343]    [Pg.343]    [Pg.299]    [Pg.113]    [Pg.218]    [Pg.670]    [Pg.130]    [Pg.176]    [Pg.130]    [Pg.395]    [Pg.351]    [Pg.132]    [Pg.343]    [Pg.343]    [Pg.343]    [Pg.343]    [Pg.299]    [Pg.113]    [Pg.218]    [Pg.670]    [Pg.130]    [Pg.176]    [Pg.130]    [Pg.395]    [Pg.351]    [Pg.506]    [Pg.88]    [Pg.26]    [Pg.171]    [Pg.398]    [Pg.401]    [Pg.80]    [Pg.544]    [Pg.155]    [Pg.306]    [Pg.142]    [Pg.145]    [Pg.248]    [Pg.126]    [Pg.194]    [Pg.198]    [Pg.155]    [Pg.410]    [Pg.292]    [Pg.293]    [Pg.299]   
See also in sourсe #XX -- [ Pg.57 ]




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Grinding material

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