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Material Composition % Copper 2-10 Zinc 6-15 Aluminium 0-40 Lead 0-2 Iron 0-16 Stainless steel 0-0.2 Rubber 20-30 Glass 30-50 As a next step the non-magnetic fraction is either hand-sorted or passed through a variety of automated processes (described in section 2.3) to separate copper, brass, zinc, magnesium, aluminium and non-magnetic steel from the non-metallic part, which contains road dirt

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01.11.2012Separation processes using engineered osmosis are disclosed generally involving the extraction of solvent from a first solution to concentrate solute by using a second concentrated solution to draw the solvent from the first solution across a semi-permeable membrane. Enhanced efficiency may result from using low grade waste heat from industrial or commercial sources.

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The refrigerant vapor passes into a refrigerated condenser, condenses, and is pumped back to the freezer. When the drain column is packed full of ice the process is stopped and the ice is washed and melted. The concentrate drains out of the ice back to the crystallizer, and is saved for additional testing. Since only about 50% of the water in

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Vanadium extraction from vanadiumtitanium magnetite concentrate 2 Experimental 21 Materials The vanadiumtitanium magnetite ore used in the experiment was from Chaoyang China After crushing and grinding the particle size of the ore was 0074 mm accounting for . more. Separation Of Vanadium And Titanium From Iron Ore . Separation of vanadium and titanium from iron ore separation of vanadium

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The conducting fraction, which contained the metals was then subjected to magnetic separation where 42% was found to be magnetic and 58% non-magnetic. This series of separation steps effectively helped to concentrate the valuable metal fraction and it was the final nonmagnetic fraction that was subjected to chemical leaching. The main leachant solution was a solution of 2 M sulphuric acid and

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This work presents data toward the development of a new zero-liquid discharge (ZLD) system, the aim of which is to concentrate a liquid effluent thereby recovering process water. The crystallization technology used in this work is clathrate hydrate crystal formation. A screening of clathrate hydrate formers was performed and three were chosen, propane, carbon dioxide, and a 30-70 mol% propane

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A selective recirculation circuit has a loading stage, a stripping stage and a filtering stage for use in processing a feed stream or slurry containing mineral particles. The stripping stage forms a first loop with the loading stage, and a second loop with the filtering stage. The loading stage has a loading mixer and a loading washing screen.

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