Refractories and Industrial Ceramics Vol. 43, Nos.5–6, 2002 EQUIPMENT FILTRATION OF DUST-AND-GAS FLOWS IN THE PRODUCTION OF BUILDING MATERIALS 1 1 1 1 S. V. Éntin, N. M. Anzheurov, Yu. V. Krasovitskii, and S. Yu. Panov Translated from Ogneupory i Tekhnicheskaya Keramika, No. 5, pp. 35 – 36, May, 2002. The duration of stage II is chiefly determined by the The typical mass concentration of dust in the waste pro- mass concentration, dust dispersivity, and filtering rate. cess gases or particulate emissions in the industry of building At stage III, the “nonstationary” filtration through the materials is z 1gm . The filtration of aerosols results in em earlier formed dust self-filter layer occurs, which results in the deposition of a dust layer on the surface of the filtering further increase of the dust-layer thickness and, correspond material, which causes an increase in the hydraulic resistance ingly, in a linear increase of hydraulic resistance at the virtu of the filter (assuming the filtration rate to be constant) . ally constant dust breakthrough ratio. This constancy of Industrial dust filtration at high dust concentrations and breakthrough ratio is due to the steady removal of particles the efficiency of different mechanisms
Refractories and Industrial Ceramics – Springer Journals
Published: Oct 13, 2004
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