Particle Size Measurement Volume 1 (Particle Technology Series)

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Particle Size Measurement

From this it can be concluded that the wide distribution results depend on the way in which the force is applied Axelson, Ph. In spite of this, the results of itself and that attempts to improve grinding efficiency by weakening large mill tests can often be correlated within 25 to 50 percent by a sim- the particles will result in coarser fragments which may require a fur- ple test, such as the number of drops of a particular weight needed to ther break to reach the desired size.

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Different mills are designed to apply the force in different ways Two methods having particular application for coal are known as [Rumpf, Chem. In the ball-mill method, the rel- ]. The detailed prediction of grinding rates and product-size dis- ative amounts of energy necessary to pulverize different coals are tribution from mills awaits the development of a simulation model determined by placing a weighed sample of coal in a ball mill of a based on the physics of fracture. An initial attempt is that of Buss and specified size and counting the number of revolutions required to Shubert Third European Symposium on Size Reduction, op.

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The grindability index in percent is equal to the quotient of of breakage events which are similar to single-particle breakage exper- 50, divided by the average of the number of revolutions required iments in the laboratory. The versity of Karlsruhe, Germany. Hildinger [Freiberg.

Technical Specifications

Chandler [Bull. Coal Util. The chief purpose of a study of with caution. So many Manufacturers of various types of mills maintain laboratories in variables affect grindability that this concept can be used only as a which grindability tests are made to determine the suitability of their rough guide to mill sizing; it says nothing about product-size distribu- machines. When grindability comparisons are made on small equip- tion or type or size of mill. This is better than relying on a grindability coefficient or work index discussed later.

This more precise con- index obtained in a ball mill to estimate the size and capacity of dif- cept is limited by the inadequacies of these laws but often provides the ferent types such as hammer or jet mills. The finer stages of comminution result in the most wear, because particle size referred to the fraction of that size present. Parameters that affect wear fall under three categories: 1 the tant in determining grindability. Grindability is related to modulus of ore, including hardness, presence of corrosive minerals, and particle elasticity and speed of sound in the material [Dahlhoff, Chem.

It is a fairly good indication of the International J. Mineral Processing, 22, — ]. Arranged in increasing order or hardness, the metal lost furnishes a useful indication. Rough values are quoted in Mohs scale is as follows: 1, talc; 2, gypsum; 3, calcite; 4, fluoride; 5, Table The use of hard-surfacing techniques by welding and by inserts has Materials of hardness 1 to 3 inclusive may be classed as soft; 4 to 7, contributed greatly to better maintenance and lower downtime [Lutes as intermediate; and the others, as hard. Examples are: and Reid, Chem. Soft Materials 1 Talc, dried filter-press cakes, soapstone, In wet grinding a synergy between mechanical wear and corrosion waxes, aggregated salt crystals; 2 gypsum, rock salt, crystalline salts results in higher metal loss than with either mechanism alone [Iwasaki, in general, soft coal; 3 calcite, marble, soft limestone, barites, chalk, International J.

This is due to brimstone.

Wear rate limestone; 5 apatite, hard phosphate, hard limestone, chromite, is higher at lower solids content, since ball coating at high solids pro- bauxite; 6 feldspar, ilmenite, orthoclase, hornblendes. This indicates that the mechanism is different Hard Materials 7 Quartz, granite; 8 topaz; 9 corundum, from dry grinding. The rate without corrosion can be measured with an sapphire, emery; 10 diamond. Insertion of marked balls A hardness classification of stone based on the compressive into a ball mill best measures the wear rate at conditions in industrial strength of 1-in cubes is as follows, for loadings in pounds-force per mills, so long as there is not a galvanic effect due to a different compo- square inch: very soft, 10,; soft, 15,; medium, 20,; hard, sition of the balls.

Mechanical sieving

The mill must be cleared of dissimilar balls before a 25,; very hard, 30, Sulfide ores promote corrosion due to gal- Grindability Methods Laboratory experiments on single parti- vanic coupling by a chemical reaction with oxygen present. Increasing cles have been used to correlate grindability. In the past it has usually the pH generally reduces corrosion.

Wear-resistant materi- Trans. Ni-hard 2 is a Alnico 1 0. It is suited to small-section components involving low- Cement clinker 2 12, Grade 4 Ni-hard Cement raw material 4 This alloy Chrome ore 1 10, 9. It is more suited to thicker sec- Copper ore 12 12, Coral rock 1 0. They have become standard Gold ore 2 Granite 11 15, These alloys form a metastable austenite structure on casting.

Particle Measurement

Gravel 2 This depletes the austenite of Iron ore misc. The chromium carbide results in a slightly higher level of tough- Magnesite 3 14, Molybdenum may be added to in- Manganese ore 1 Elimination of austenite in the Nickel ore 2 Hardness can range from 52 to 65 Rockwell. For ball Pumice 1 The Quartz 7 In wet Rare earths 1 0. For ring-roll mills, high-chromium molybde- Schist-biotite 1 Slag 1 Rubber, due to its high resilience, is extremely Sulfur 1 It is inert to corrosive wear in Trap rock 11 14, It is susceptible to cutting abra- Average 13, The product averages 80 energy savings, ease of installation, and sound-proofing qualities.

Polyurethane has similar resilient characteristics.

Its fluidity at the for- mation stage makes it suitable for the production of the wearing sur- face of screens, diaphragms, grates, classifiers, and pump and flotation alloyed cast irons, and 3 nonmetallics [Durman, International J. The low heat tolerance of elastomers limits their use in dry Mineral Processing, 22, — ]. Manganese steel, containing 12 to 14 percent manganese and 1 to Ceramics fill a specialized niche in comminution where metallic 1.

Therefore ceramics are used for bined with adequate wear resistance, and enhanced by the austenitic milling cements and pigments. Ceramic tiles have been used for lining microstructure having the ability to work harden. Although the rela- roller mills and chutes and cyclones, where there is a minimum of tively low yield strength can lead to problems of spreading in service, impact.

Applications are generally and plastics is often not appreciated Hartmann and Nagy, U. Explosions and fires may be initiated loading, such as jaw-crusher elements, gyratory cone-crusher mantles, by discharges of static electricity, sparks from flames, hot surfaces, and and primary hammer-mill parts.

Metal powders present a hazard because of For medium- to high-impact applications a wide range of low-alloy their flammability. Their combustion is favored during grinding steels are produced containing some chromium, molybdenum, phos- operations in which ball, hammer, or ring-roller mills are employed phorus, and silicon.

Economy of manufacture is a benefit for selection and during which a high grinding temperature may be reached. Many finely divided metal powders in suspension in air are poten- Low-alloy steel production falls into two metallurgical types. The tial explosion hazards, and causes for ignition of such dust clouds traditional approach is heat treatment to produce a pearlitic micro- are numerous [Hartmann and Greenwald, Min. The other is to add sufficient alloying constituents to permit ]. Concentration of the dust in air and its particle size are thermal processing to produce a martensitic structure.

Typical appli- important factors that determine explosibility. Below a lower limit of cations are ball mill liners and grinding balls. Many of these compo- concentration, no explosion can result because the heat of combustion nents are consumed in high tonnages, and this combines with is insufficient to propagate it.

Above a maximum limiting concentra- metallurgical characteristics to favor production by forging. Low-alloy tion, an explosion cannot be produced because insufficient oxygen is steel liners, grates, and balls are also produced as castings. The finer the particles, the more easily is ignition accom- Alloyed white cast irons fall into the second category. This group plished and the more rapid is the rate of combustion. This is illus- includes the nickel-chromium grades known as Ni-hards Durman, trated in Fig.

(PDF) PARTICLE-SIZE ANALYSIS Particle-Size Distribution | Usman Ali Hashmi -

It reviews these areas with an extensive bibliography. Hart- mann, Nagy, and Brown, U. Stainless steel has less sparking where E is the work done, X is the particle size, and C and n are con- tendency than ordinary steel or forgings. The is a means for preventing dust explosions in equipment Brown, U. Aufbereitungskunde, Ernst and Korn, Berlin, Its dust is explosive [Twiss Trans. Summary data are given in Table The work index may be found experimentally from laboratory The fineness to which a material is ground has a marked effect on its crushing and grinding tests or from commercial mill operations.

Some production rate. Figure is an example showing how the capacity rules of thumb for extrapolating the work index to conditions different decreases and the specific energy and cost increase as the product is from those measured are that for dry grinding the index must be ground finer. Also for Washington, ; available National Technical Information Service, a jaw or gyratory crusher the work index may be estimated from Springfield, Va.

The report recommends that five areas be considered to to yield a starting point for further development of understanding of save energy: classification-device design, mill design, control, addi- milling. They are mainly of historical interest. With present particle-size-analysis techniques applic- crystal. Kuznetzov ranks other materials by a relative wear test. His able to the finest sizes, such confusion is no longer necessary. The results substantiate the efficiencies given earlier.

Particle Size Analyzers

Attempts to measure relation of energy expenditure to the size distribution produced has efficiency of the grinding process by calorimetry involve errors that been thoroughly examined [Arbiter and Bhrany, Trans. Practical energy efficiency is defined as the efficiency of techni- Trans. London , cal grinding compared with that of laboratory crushing experiments. Grinding Efficiency The energy efficiency of a grinding opera- Am. Usually time of grind- The theoretical energy efficiency of grinding operations is 0.

The energy coefficient may also be expressed as tons per Trans.

Particle Size Measurement Volume 1 (Particle Technology Series) Particle Size Measurement Volume 1 (Particle Technology Series)
Particle Size Measurement Volume 1 (Particle Technology Series) Particle Size Measurement Volume 1 (Particle Technology Series)
Particle Size Measurement Volume 1 (Particle Technology Series) Particle Size Measurement Volume 1 (Particle Technology Series)
Particle Size Measurement Volume 1 (Particle Technology Series) Particle Size Measurement Volume 1 (Particle Technology Series)
Particle Size Measurement Volume 1 (Particle Technology Series) Particle Size Measurement Volume 1 (Particle Technology Series)
Particle Size Measurement Volume 1 (Particle Technology Series) Particle Size Measurement Volume 1 (Particle Technology Series)
Particle Size Measurement Volume 1 (Particle Technology Series) Particle Size Measurement Volume 1 (Particle Technology Series)

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