Coal-Fired Power Generation Handbook. James G. Speight

Coal-Fired Power Generation Handbook - James G. Speight


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standards.

      Thus, the coal delivered to the coal preparation plant consists of coal, rocks, minerals, and any other form of material that is not coal. The coal also varies widely in size, ash content, moisture content, and sulfur content. Thus, coal preparation serves several purposes. One important purpose is to increase the heating value of the coal by mechanical removal of impurities. This is often required in order to find a market for the product. Run-of-mine coal from a modern mine may incorporate as much as 60% reject materials.

      Thus, after coal is mined it generally goes through a process known as preparation or coal cleaning to (i) remove the impurities in order to boost the heat content of the coal and thereby improve power plant capacity, which also reduces maintenance costs at the power plant and extends plant life, and (ii) to reduce potential air pollutants, especially sulfur dioxide – the extent to which sulfur dioxide emissions can be reduced varies, depending upon the amount of sulfur in the coal and the form of its occurrence.

      Briefly, the grade of a coal establishes its economic value for a specific end use. Grade of coal refers to the amount of mineral matter that is present in the coal and is a measure of coal quality. Sulfur content, ash fusion temperature (measurement of the behavior of ash at high temperatures), and quantity of trace elements in coal are also used to grade coal. Although formal classification systems have not been developed around grade of coal, grade is important to the coal user.

      Coal preparation (coal cleaning) is the means by which impurities such as sulfur, ash, and rock are removed from coal to upgrade its value (Speight, 2013). In the process, the undesirable material is removed from the run-of-mine (ROM) coal by employing separation processes which are able to differentiate between the physical and surface properties of the coal and the impurities. The result is a relatively clean uniform coal product.

      Furthermore, since transportation costs are usually charged on a ton-per-mile basis (which does not distinguish between coal substance and moisture content), it is preferential to remove as much as possible of the extraneous mineral matter and water prior to shipping thereby reducing transportation costs for an “inferior” grade of coal and providing a higher energy material to the consumer.

Coal type Carbon (%) Hydrogen (%) Limits of volatile matter (%) Fixed carbon (%) Calorific value (Btu/lb)
Lignites 73–78 5.2–5.6 45–50 50–55 <8,300
Subbituminous 78–82.5 5.2–5.6 40–45 55–60 8,300–11,500
High-volatile bituminous 82.5–87 5.0–5.6 30–40 60–70 11,500–14,000
Medium-volatile bituminous 87–92 4.6–5.2 20–30 70–80 >14,000
Low-volatile bituminous 91–92 4.2–4.6 15–20 80–85 >14,000
Anthracite 95–98 2.9–3.8 5–10 91–95 >14,000

      In fact, long-range transportation of lignite, more than one-third of which consists of water, can more than triple the initial mine-mouth costs calculated on an energy basis. There may, however, be some trade-off in transportation costs if the low-rank coal is sufficiently low in sulfur which, in turn, means a lower cost in terms of stack gas clean-up (Nowacki, 1980).

      The need for coal cleaning can be reduced by choice of suitable mining methods, many mines include the methods by which oversize coal is reduced in size but the cleaning of run-of-mine coal is, more often than not, a separate operation which is performed as a surface operation that is usually close to the mine-mouth. However, the term coal preparation includes, by definition, not only sizing (i.e., crushing and breaking) methods but also all of the handling and treatment methods that are required to prepare the coal for the market.

      Thus, by providing a higher concentration of heat in the fuel (lower mineral matter and moisture content), the associated costs of transportation, handling, crushing, pulverizing and residual waste (fly ash) disposal in the electricity generation are reduced because fewer weight units per kilo-watt hour generation will be required.

      Coal preparation processes are categorized as either physical cleaning or chemical cleaning. Physical coal cleaning processes, the mechanical separation of coal from its contaminants using differences in density, are by far the major processes in use in modern coal-cleaning plants. Physical coal cleaning techniques take advantage of the differences in specific gravity of the coal and its impurities. Hydrocyclones and gravity concentration devices are examples of such systems. When coal is finely ground, physical processes that take advantage of the surface properties of the coal materials can be used. For example, froth flotation exploits the hydrophilic surface characteristics of mineral impurities and the hydrophobic nature of coal particles to achieve separation.

      Chemical coal cleaning processes are currently being developed, but their performance and cost are undetermined at this time. For example, some of the sulfur in coal is actually chemically connected to the carbon backbone of coal instead of existing as separate particles. Several process have been tested to mix the coal with chemicals that break the sulfur away from the coal backbone but most of these processes have proven too expensive and have not been applied to commercial coal cleaning operations (Speight, 2013).

      The direct objectives of coal-cleaning practices are reduction (within predetermined limits) of size, moisture, ash, as well as sulfur (Williams, 1981; Couch, 1991). However, coal properties have a direct bearing not only on whether but also on how coal should be cleaned. Indeed, coal rank (rank being a complex property that is descriptive of the nature of the coal and its properties) (Chapters 2, 5, 6) can, and usually does, play


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