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Crushing Plant

Crushing Plant

The combination crusher is a new generation high efficiency crushing machine designed and researched by integrating the domestic and foreign crusher technology with the same kinds and optimizing the main technical parameters.
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lime slaking equipment - mineral processing & metallurgy

A lime slaking and addition system can consists of two systems to control the pH in the rougher and cleaner flotation circuits. A pebble lime silo will dose dry lime to the SAG mill feed belt; a hydrated lime make down system will provide slurry lime to multiple addition points in the flotation circuit. Other lime delivery options are detention slakers and Verti-mill slakers. The proposed system is the lowest capital cost option available. The operating costs are dependent on the slaker efficiency, hydrated lime consumption, proportion of pebble lime used, and slaker grit loss. Due to the increased reagent usage and cost of hydrated lime to achieve the same pH impact, the proposed lime addition system will have the highest operating costs of the three possible systems

Initial flotation test work conducted included a box statistical study that compared grind size, reagent schemes, and pH. This test work indicates improved copper and molybdenum recovery and concentrate grade at a rougher pH of 10.8

An earlier proposed lime addition system was changed from a verti-mill slaker to the currently proposed pebble lime / hydrated lime system. The revived cost estimate carried extra cost for a milk of lime tank and showed the verti-mill and 500 ton silo at zero cost. For a copper concentrator which will have one primary grinding line, so the primary pH control could be accomplished with pebble lime addition to the SAG mill feed belt. A smaller supplemental system would then be required for final pH control of the rougher and cleaner flotation circuits. Test work has indicated that adding reagents to the grinding mill increases recovery. The pebble lime addition and hydrated lime systems were considered to be cleaner and easier to operate

Calcium hydroxide particle size, and the resulting surface area, is dependent on the lime slaking temperature. The lime to water ratio and temperature in a SAG mill environment are not optimal to produce fine calcium hydroxide particles. Lime particles will continue to react under non-optimum conditions until a coating forms on the particle surface. There is no hard data on how much the lime consumption would increase compared to using slaked lime, but a chemist with on the project estimates lime consumption would increase 5 – 10%

lime slaking equipment - mineral processing & metallurgy

An economic comparison of the three lime addition systems was done. Budgetary quotations were obtained for a dual 2 ½ ton per hour (TPH) detention slaker and a 3 TPH Verti-mill slaker. Installation costs for each system was assumed to be 50% of the capital cost. Hydrated lime cost is estimated to be 20% more than pebble lime; no allowance for the additional trucking cost of hydrated lime was made. The pebble lime usage proportion of the pebble / hydrated system was assumed to be 90%, and a 10% lime consumption increase was applied to the pebble lime usage. For the detention slaker, the grit would be disposed of in the grinding circuit, and a 5% increase in lime consumption was applied. For the Verti-mill slaker, it was assumed that all the lime was converted to hydroxide. The results of the economic comparison for the first 10 years of mine life shown

If lime slaking efficiency is removed from the economic analysis, the higher cost and reagent consumption of hydrated lime still justifies the installation of a slaker. The proportion of pebble lime to hydrated lime was varied to find the breakeven point between the two slaker systems. For the detention slaker, the proportion was 94% pebble lime, and for the Verti-mill slaker, the proportion was 88%

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