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Mass size fractions are not conserved through grinding devices (SAG mill and ball mills). Therefore there is no mass conservation equation for size fractions around the grinding devices and consequently there is no node for grinding devices in mass size fraction networks. The same reasoning applies to Cubysize fractions.
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The energy efficiency of ball mills for use in finish grinding is relatively low, consuming up to 3042 kWh/ton clinker depending on the fineness of the cement (Cembureau, 1997Marchal, 1997).
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