Coal-Fired Power Generation Handbook. James G. Speight

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СКАЧАТЬ of a screen to separate fines and small particles to avoid extra fine generation in crushing, and (ii) incorporation of a magnetic separator to separate iron pieces in coal, which may damage the crusher.

The fines in coal produced during the crushing (sizing) operation can present problems in combustion on account of segregation effects. Segregation of fines from larger coal pieces can be reduced to a great extent by conditioning coal with water. Water helps fine particles to stick to the bigger lumps due to surface tension of the moisture, thus stopping fines from falling through grate bars or being carried away by the furnace draft. While tempering the coal, care should be taken to ensure that moisture addition is uniform and preferably done in a moving or falling stream of coal. If the percentage of fines in the coal is high, wetting of coal can decrease the percentage of unburned carbon and the excess air level required to be supplied for combustion. In cases where the sized coal has an excessive amount of fine coal, blending with predominantly lump coal (depending upon the coal-fired system) may be an option. This may thus help to limit the extent of fines in coal being fired to not more than a specified maximum. In fact, blending of coals of different quality may also help to supply a uniform coal feed to the boiler (Chapters 7, 8).

      The size of a coal particle is defined in terms of a surface opening through which the particle will barely pass or will not pass at all. In sizing a material, the individual particles are presented to the surface openings numerous times. However, the size of a particle mut be recognized because a three-dimensional particle is presented to a two-dimensional opening. In the case of a narrow, elongated particle, the particle will be sized according to the orientation of the particle with respect to the surface opening (ASTM D431) defines the top size or upper limit of a quantity of material as the smallest sieve (smallest opening) upon which is retained a total of less than 5% of the sample. In practice, the term nominal top size is used extensively when describing the output range of a size reduction device. The nominal top size of a quantity of material is the smallest sieve (smallest opening) upon which is retained a total of 5 to 20% of the sample.

      Reduction ratio is the ratio between the feed top size and the product top size, or the ratio between the feed and product sizes at which a specific percentage of the material passes. For size reduction units that produce a product top size larger than 1 mm, size reduction ratios are normally of the order of 8-to-1 while for units where the product top size is smaller than 1 mm, size reduction ratios can range from 200-to-1 and higher.

      The top size upper limit of the crushed (sized) material is defined by the smallest sieve opening upon which is retained a total of less than 5% of the sample (ASTM D431). The term nominal top size is used to describe the product of a size reduction operation and is the smallest sieve opening upon which is retained a total of 5 to 20% of the sample. The reduction ratio is the ratio between the feed top size and the product top size or the ratio between the feed and product sizes at which a determined percentage of the material passes. The relative ease with which a coal can be comminuted (reduced in top size) by mechanical action affects the design of a size reduction unit or operation. The term used to refer to this relative ease is the grind ability index of the coal.

      The specific energy for size reduction is proportional to the grindability index of the coal (Hardgrove grindability index, ASTM D409) and is also a function of the reduction ratio. Thus, the energy required for the size reduction of coal increases with increasing throughput as well as with the reduction ratio. For a “standard” throughput of coal, the energy required varies with the reduction ratio and the relationship between the specific energy and the grindability is dependent upon the type of device (Speight, 2013).

      Moisture in coal is not just an issue in terms of whether the coal is dry or not and whether the transportation costs warrant coal drying. Indeed, moisture content is a factor that must be taken into account when considering the energy requirements of a size reduction unit. Excessive moisture, but more particularly excessive surface moisture, can cause a lesser efficiency in fines removal (due to fines agglomeration) and the formation of emulsions can also be a problem in the selective agglomeration process (Bensley et al., 1977).

      In general, five types of equipment are used for the size reduction of run-of-mine coal: (i) rotary breakers, (ii) roll crushers, (iii) hammer mills, also called ring mills, (iv) impactors, and (v) tumblers. At best, the crushing operation produces the desired (sized) product in a single stage. However, there are cases where the size reduction of coal entails multiple stage size reduction units. The final stage of coal pretreatment is to screen it into size fractions convenient for handling by the various process streams.

      3.4.1 Rotary Breaker

      The rotary breaker essentially consists of an outer cylinder with an inner rotating perforated cylinder fitted with lifters which is operated at the lowest speed that will cause a small particle on the liner to centrifuge (Speight, 2013). Coal is fed into one end of the rotating cylinder where it breaks because of the tumbling action due to gravity fall, and pieces less than the hole sizes [typically 1% in. (38 mm)] pass out to a bottom collection trough, giving a product with positive upper size control. The flow rate through the breaker is adjusted so that pure coal has broken through and rock passes through the exit; in practice, some coal will pass out with the rock. Large pieces of hard, dense rock will also act as grinding media. Because of the relatively mild breakage action, the production of fines is minimized. For hard coal, the length-to-diameter ratio is increased, and the diameter is increased to give a higher force due to the greater fall.

      The raw coal from the rotary breaker can be utilized directly, undergo further size reduction, or the quality of the product can be upgraded in a coal-washing facility (Speight, 2013).

      3.4.2 Roll Crusher

      Roll crushers are size reduction devices that shear and (or compress) the material that is to be reduced in size. The single-roll crusher is a popular piece of equipment and primarily consists of a heavy cast iron or steel fabricated frame on which are mounted the crushing roll and the stationary breaker plate. The breaker plate is provided with renewable wear plates bolted to the breaker plate. The roll usually has a series of long teeth spaced at intervals and various short teeth covering the entire crushing surface. The coal is squeezed between the revolving roll and the breaker plate. The long teeth act as feeders and also penetrate the lumps of coal, splitting them into smaller pieces, while the smaller teeth make the proper size reduction (Roman, 1967).

      Double-roll crushers consist of two rolls that rotate in opposite directions. A double roll crusher can reduce run-of-mine coal (maximum top size 36 inches, 0.9 m) to a product with a top size in the range of 14 inches (350 mm) to 3/4 inch (19 mm). The roll size can vary from 12 x 18 inches to 60 x 60 inches and capacity may vary up to 2,000 tons/hour. Double-roll crushers generally produce minimal amounts of fines (Roman, 1967).

      3.4.3 Hammer Mill

      The hammer mill is a device in which the feed coal is contacted (impacted) by rotating hammers and then further impacted by contact with grid breaker plates. The grinding that occurs in the hammer mill results from the rubbing action of feed material between two hardened surfaces i.e., the hammers and the grid or screen plates. The hammer mill usually produces a relatively high proportion of fine material (Roman, 1967). The fineness obtained can be varied by adjustments of revolutions per minute or the spacing between the hammer tips and the grate bars.

The ring-type hammer mill is a modification of the hammer mill which was developed to help minimize the amount of fines in the product. In these units, the hammers have been replaced by rings (alternately toothed and plain) which revolve and cause size reduction by a rolling compression action СКАЧАТЬ