Wills and NapierMunn (2006) describe the design and operation of SAG mills. SAG mills are currently the technology of choice in hard rock milling operations for reducing primarycrushed ore to ball mill feed. In recent years, the trend has been towards largersized SAG mills with diameters of m
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WhatsApp: +86 18838072829In practice, circulating loads between ball mills and classifiers are rarely less than 200 per cent and frequently exceed 700 per cent. It may appear strange at first sight that the circulating load between a mill and classifier producing, for example, 100 tons of finished product per day can be as much as 400 tons or more, but this will be ...
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WhatsApp: +86 18838072829Production of a sample for fl otation in a design or geometallurgy batch fl otation program often involves crushing or rolls crushing followed by ball or rod milling to achieve a target size P80. ... scale ball mills, for instance, are usually about 4 to 5 m in diameter, which is much larger than the m mill used in Armstrong's comparative ...
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WhatsApp: +86 18838072829In Grinding, selecting (calculate) the correct or optimum ball size that allows for the best and optimum/ideal or target grind size to be achieved by your ball mill is an important thing for a Mineral Processing Engineer AKA Metallurgist to do. Often, the ball used in ball mills is oversize "just in case".
WhatsApp: +86 18838072829The basic parameters used in ball mill design (power calculations), rod mill or any tumbling mill sizing are; material to be ground, characteristics, Bond Work Index, bulk density, specific density, desired mill tonnage capacity DTPH, operating % solids or pulp density, feed size as F80 and maximum 'chunk size', product size as P80 and maximum a...
WhatsApp: +86 18838072829Grindability Index Test Method Procedure. The Levin test appears to be underused for sizing regrind ball mills. Examples of the results are shown in Table 6. The requirement of 2030 kg may be a prohibitive factor. The Levin test is a modified Bond Ball test, but makes use of finer screen sizes, and finer feed sizing.
WhatsApp: +86 18838072829In the meantime, the 50% increase of daily mill output from the original 2000 to 3000 tons necessitated finer fourth stage crushing and the addition of an extra grinding mill. The fine ore actual handled today is a rollcrusher product of 5/32″ in size with a moisture content of 2% to 3%.
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WhatsApp: +86 18838072829When the test ball mill is run in open circuit the design feed rate is tonnes/hour. Figure 4 compares the predicted size distributions from the open circuit ball mill with feed rates of, and tonnes/hour respectively. As might be expected, the larger the feed rate the coarser the grinding mill discharge product.
WhatsApp: +86 18838072829The ore is first ground in a ball mill which operates in closed circuit with a cyclone or similar sizing device. This is done to produce a feed suitably sized so that subsequent leaching is rapid. The ground ore overflowing the sizing device generally runs at 25 to 35 percent solids.
WhatsApp: +86 18838072829WR = R (WS) (CW)/ (DR) (TpH) In addition to wear speed, ball size and recharge practice, charge volume, and feed rate are significant factors affecting the actual production wear rate. Wear speeds are largely independent of ball size and ball charge volume. The wear rate exponent for SAG milling was experimentally determined to be n =
WhatsApp: +86 18838072829Assuming your ore is AGamenable: 7 TPH to 15 TPH is a comfortably production average for a 13′ x ′ AG Mill. A 13′ x 6′ SAG Mill has a reasonable range of: 20 to 30 TPH for gold ore SAG Ball Mill duty. 25 to 40 t/h for copper porphyry SAG Ball Mill duty. In Single Stage SAG duty, the approximate capacity reduces to only 8 to 13 ...
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WhatsApp: +86 18838072829ing design inefficiency factors into the reference Bond Standard Circuit, assume m diameter overflow mills, and use a rod mill F80 of 16,000 µm and a rod mill P80 of 1,000 µm. Note that—in order for no correction factor for ball mill product fineness to apply—the ball mill circuit P80 should be no less than approximately 70 µm ...
WhatsApp: +86 18838072829A side by side study: RoM ball and AG mill with F80 around 50 mm and a mill product P80 of around 250um, indicated the OWI is also considerably higher, and although it is known to be biased against finer products, the difference is sufficiently large to indicate that the RoM ball mill is less efficient than AG milling.
WhatsApp: +86 18838072829You also need a rod mill work index to design a ball mill operating on a coarse feed, above about 4 mm. Q1: You design for a typical percentage of critical speed, usually 75% of critical. Then you iterate the mill diameter using a Morrell Cmodel or Nordberg equation to get the RPM that corresponds to 75% for that mill diameter.
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WhatsApp: +86 18838072829The Azzaroni equation indicates that the correct ball size for the m mill is 81 mm. Years of experience show that a 76 mm ball grinds the coarse particles most effectively. Ball size distribution is governed by the wear law of the mill and by the wear characteristics through the crosssection of the balls charged to the mill.
WhatsApp: +86 18838072829The third step in crushing, or tertiary reduction, depends upon what is required. Twoinch or smaller pieces from the secondary crushers may be fed direct to stamps, rod mills, or ball mills, but it is more usual to use a third dry crusher to reduce the ore to ½ or 5/8in. size before wet crushing, particularly in the case of ball milling.
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