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Dust Control Handbook for Industrial Minerals Mining and Processing

Dust Control Handbook for Industrial Minerals Mining and Processing

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times. When considering the depth of loading onto felted fabrics, the filter bag is actually actingas a support <strong>for</strong> the dust cake. <strong>Dust</strong> is allowed to penetrate into the fabric to <strong>for</strong>m a layer of duston the bag. Thus, the dust creates a "porous" cake with much smaller air passages, allowing thedust to filter itself. Without this cake, the filter would bleed through <strong>and</strong> never obtain acceptableoutlet emissions. There<strong>for</strong>e, in the design <strong>and</strong> operation of a baghouse using felted media, it isimportant to use appropriate air to cloth ratios, cleaning cycles, <strong>and</strong> cleaning pressures. Theoptimum collector operation maintains a constant pressure drop of 3–6 inches wg <strong>and</strong> minimizescleaning cycles <strong>and</strong> compressed air usage. This does not mean that a system running higher thana 6-inch pressure drop is not operating satisfactorily. Some systems can operate effectively athigher pressure drops. The system is operating correctly as long as the pressure drop is constant<strong>and</strong> the required air volume is being achieved.Surface loaded media do not require a dust cake to achieve optimum per<strong>for</strong>mance. As the nameimplies, the dust is collected on the very surface of the fabric. Some surface loaded media usemembranes composed of a very thin layer (1 mil) of PTFE (polytetrafluoroethylene) materialthat is laminated to a substrate. This substrate material is a conventional felt. The laminate isapplied in a special process that controls the size of the pore openings; thereby the collectionefficiency is predictable. These pore openings are so small that they will only allow extremelysmall submicron particles to pass, making these fabrics extremely efficient.<strong>Dust</strong> collectors using felted media typically run higher pressure drops than those operating withsurface-loaded media because the filter or dust cake adds resistance to the system. As previouslymentioned, the pressure drop tends to range from 3–6 inches wg, while surface-loaded mediaoperating without a filter cake typically run in the 2–4 inches wg range.The st<strong>and</strong>ard fabrics used in shaker collectors are woven cotton <strong>and</strong> polyester sateens <strong>and</strong>lightweight felts. Pulse jet <strong>and</strong> reverse air collectors use felts ranging in weight from 14 to asheavy as 22 ounces. Woven fabrics are not used in the last two types of collectors because thecleaning system is much more aggressive than shaking. Pulsing woven fabrics opens up theweave <strong>and</strong> causes leakage <strong>and</strong> undesirable emission levels. Cartridge filters typically usecellulose/synthetic blends <strong>and</strong> spun-bonded polyester media.When matching fabric choice to dust collection needs, the basic criteria are temperature, inletloading, particle size distribution, gas composition, abrasion, static charge, release, <strong>and</strong>efficiency requirements. The following are some basic guidelines <strong>for</strong> each criterion.1. Temperature. Inlet gas temperature should be matched with a fabric capable ofcontinuous operation at or above the maximum temperature the system might experience.2. Inlet loading. Inlet grain loading (normally expressed in grains/dry st<strong>and</strong>ard cubic feet)is especially important when the loading is very light. Light loadings can make itdifficult <strong>for</strong> the media to operate with sufficient dust cake.3. Particle size distribution. Finer particle size distributions often require using higherefficiency media.4. Gas composition. The designer must make sure that if corrosive compounds orhydrocarbons are present in the airstream, then the media selected will be able towithst<strong>and</strong> that environment.Fundamentals of <strong>Dust</strong> Collection Systems 47

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