1996
DOI: 10.1016/0032-5910(95)03051-4
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A study on grinding and energy input in stirred media mills

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Cited by 56 publications
(30 citation statements)
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“…), and p=media density (g/cm 3 ). A similar equation was given by Gao et al [8], based on experiments using a 6-liter, horizontal, disk-type stirred ball mill using operating conditions of media density: 2.5-5.4 g/ cm 3 , slurry density: 65-75 wt.%, and stirrer speed: 805-2253 rpm. A dispersant was used at a level of 0.5-1.5% of the solids.…”
Section: Mill Powermentioning
confidence: 85%
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“…), and p=media density (g/cm 3 ). A similar equation was given by Gao et al [8], based on experiments using a 6-liter, horizontal, disk-type stirred ball mill using operating conditions of media density: 2.5-5.4 g/ cm 3 , slurry density: 65-75 wt.%, and stirrer speed: 805-2253 rpm. A dispersant was used at a level of 0.5-1.5% of the solids.…”
Section: Mill Powermentioning
confidence: 85%
“…[8] studied the energy efficiency of stirred media mills with pin-type stirrers in the grinding of limestone with glass beads. It was found that as the impeller speed was increased, the product surface area and energy input increased, but energy efficiency declined.…”
Section: Energy Efficiencymentioning
confidence: 99%
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“… bilya şekli ve türü,  karıştırma hızı,  bilya yoğunluğu,  bilya çapı ve şarj oranı,  pülp yoğunluğu ve  viskozitedir [1, 11,12]. Aşağıda bunlardan bazıları açıklanmaktadır.…”
Section: İşlem Parametreleriunclassified