2017
DOI: 10.15587/2312-8372.2017.112791
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Investigation of the treatment efficiency of fine-dispersed slime of a water rotation cycle of a metallurgical enterprise

Abstract: влияние консТрукции завихриТеля входного ПоТока на гидродинамику и эФФекТивносТь рабоТы Исследовано влияние конструкции завихрителя и места его установки в газоходе для подачи газопылевого потока на эффективность работы вихревого аппарата. Доказано, что кон-струкция завихрителя при соответствующих условиях позво-ляет закрученному потоку добиваться максимально возможной для данной конструкции угловой скорости вращения газового потока. Разработана принципиальная конструкция вихревого пылеуловителя, которая позво… Show more

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Cited by 2 publications
(6 citation statements)
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“…It is also quite clearly seen in Fig. 2, 6 and is consistent with earlier studies involving actual sludge from wet gas treatment [20,21].…”
Section: Discussion Of Results Of Studying the Flocculation Of Sludgesupporting
confidence: 91%
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“…It is also quite clearly seen in Fig. 2, 6 and is consistent with earlier studies involving actual sludge from wet gas treatment [20,21].…”
Section: Discussion Of Results Of Studying the Flocculation Of Sludgesupporting
confidence: 91%
“…Waste water after wet gas treatment devices is characterized by the non-uniform composition and constant fluctuations in the solid phase concentration [20]. This in turn changes the effectiveness of cleaning.…”
Section: Literature Review and Problem Statementmentioning
confidence: 99%
“…1. The results of the study of the optimal operating conditions of the module An analysis of wastewater containing a polydisperse solid phase of various concentrations using the example of a metallurgical enterprise [20,21] and a coal preparation plant [19] makes it possible to construct the following relationships shown in Fig. 2.…”
Section: The Results Of a Study Of The Effectiveness Of Cleaning And Dehydration Of Fine Sludgementioning
confidence: 99%
“…According to the methodology described in publications [19][20][21], flocculant expenditures are tested to achieve V 1 ≥6-7 mm/s (the condition for the effective operation of this thin-layer sedimentation tank); V 2 ≥2-3 mm/s (condition for the effective operation of this centrifuge).…”
Section: Conducting Flocculation Tests and Determining The Costs Of Flocculantsmentioning
confidence: 99%
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