Blogs

Base Metal Ore Processing Plant & Equipment (Copper & Lead+)

These 5 following estimates on flotation mills cover standard practice as used on base metal and non-metallic ores where the majority of values are recoverable by flotation, and where there is sufficient freed mineral in the ball mill discharge to warrant recovery by means of process Equipment like either a Unit Flash Flotation Cell, a concentrating table, or a jig,

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Small Gold Ore Processing Plant

These five illustrated flowsheets fully described in the article “Small Gold Ore Processing Plants” follow a natural sequence. These start with a very simple. Flowsheet AA, and then by the addition of the more extensive equipment, it is possible to take care of slight changes in the ore as well as improve recovery. The following tables include the tonnage handled

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Electrolytic Oxygen in Cyanide Solutions

There are two conditions generally prevailing upon the earth—those within atmospheric influence, tending towards oxidation, and those away from atmospheric influence, tending towards reduction. Practically all mineral substances from mines of any depth are in a reducing condition. Since the cyanide process, in order to dissolve silver or gold, requires that the prevailing conditions under which it operates shall be

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Mineral Jigs for Concentration of Lead Ores

The following notes are taken from results obtained on a standard 25-ft. Hancock jig tested during regular operation. The object of the tests was to determine the conditions for most effective work, and the nature of products that could be made. The material treated was sized between 9-mm. and 2-mm. round- hole screens, and was constant throughout the experiments. Three

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Ball Mill Crushing

Table of ContentsIntroduction of Marcy MillTest of Hardinge vs. Marcy MillFine CrushingReversing Feed to Hardinge Mill Until the advent of the porphyry coppers and the introduction of flotation which soon followed, crushing and grinding for many years proceeded along somewhat stereotyped lines, without important alteration in type of machinery. For the finer crushing and grinding, stamps, rolls, and various patterns

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Cyanide Processing Equipment and Plant Configuration Options

Table of ContentsFlotation and Cyanidation VS Whole Ore Cyanidation LeachBatch CyanidationCyanidation—Sand Leaching The Jig, placed between the ball mill and classifier, is one of the most valuable and affordable improvements in cyanidation in recent years and was developed by the metallurgical engineering and Mining Equipment Companies. This Mineral Jig has the marked advantage of removing a large portion of the metallic

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Gravity Recovery OR Flotation Circuits ahead of Gold Cyanide Leaching

Process Flowsheet NO. CY-3 is shown one of the outstanding improvements made in cyanidation whereby the coarse metallic minerals are removed from the grinding circuit by means of the Mineral Jig. The hutch product from this jig is amalgamated with a Amalgamator or Clean-Up Pan and thus the coarse mineral values, such as metallic gold, are removed from the circuit before

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Counter Current Decantation Cyanide Gold Leaching

The Process Flowsheet CCD CY-1 shows (below) the continuous counter-current decantation system, in which all the ore is first reduced to a very fine state in the grinding mill-classifier circuit, in a cyanide solution. The slime overflow of the classifier, usually 70%—200 mesh, or finer, is sent to the first thickener, known as the primary thickener. Here the pregnant solution, containing

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Gold Cyanidation Circuits

The principle of dissolving gold and silver values in solutions of potassium or sodium cyanide is old and has been thoroughly carried out in practice for many years. There have been only a few changes in the chemical procedure and also few changes in the type of equipment used. The gold and silver are dissolved by the chemical solution, usually

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Peripheral Discharge Ball Mills -Theory and Practice

Table of ContentsCrushing Action of Ball-MillConditions Determining Fineness of CrushingConditions Affecting Ball-Mill CapacityConditions Affecting Ball-Mill PowerSpecial Applications For Ball-Mill CrushingBall-Mill FeedingConsistency of PulpBall ConsumptionConsumption of Liners These notes are based on observations made while on a recent trip through the West, for the purpose of studying the practical operation of the ball-mill. The writer takes this opportunity to express his

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Basic Principles & Variables Affecting Froth Flotation

Table of ContentsWhat are the Variables and Factors of Flotation’s OperationOre Characteristic & MineralogyParticle SizeOil/FrotherWhy use FrothersGrind SizeThe effect of slurry densityThe quantity of oil necessary in any froth-flotation operation depends upon:The following relations between quantity of oil and size to which the ore is ground are experimentally proven:Pulp-BodypH Modifiers AKA Minor AgentsPulp or Slurry Temperature The basic factors, principles and variables affecting

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Round Concentrating Tables

Table of ContentsRound Table PracticesEarly Use of Revolving Round Table in Butte DistrictUse of the Round Table at Great Falls for Sand-Slime FeedThe Round Table for Fine SlimeConstruction of Slime PlantTests on Wood, Linoleum, and Cement DecksCentral Feed Apron RemovedRe-treatment of Round-Table TailingDetermination of Conditions for Round-Table Treatment of SlimesVariation in Slope of Round-Table DeckThe Steel-Frame Cement-Deck Round TableTests on

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Bulk Storage Hopper Flow & Feeder

Table of ContentsFlow Regime:Flow stoppagesForm of containerConverging sectionFeedersMitigating Segregation The performance of Bulk storage hoppers and silos is sensitive to the nature of their contents so consideration must first be given to the physical properties with respect to the operational requirements of the system. See the I.Mech.E publication: – ‘Guide to the specification of bulk solids for storage and handling

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Mineral Concentrate Marketing – Treatment Charges & Penalties

Table of ContentsGOLD & SILVER MarketingBASE METAL CONCENTRATE MarketingMILLINGGROSS VALUE OF CONCENTRATESMELTER Treatment Charges & PenaltiesGeneral Provisions:What to do why CONCENTRATESDrying:Sacking:Freight Rates:Weighing:Sampling:Metallics:SMELTING BUSINESSZINC CONCENTRATE MARKETINGIRON CONCENTRATE MARKETINGCOLLECTORS FOR GOLD AND SILVERCOPPER SMELTERLEAD SMELTERConcentrate Penalties and Premiums:SULPHURLEADSMELTER SLAGZINCARSENIC, ANTIMONY, TINBISMUTHMANGANESEMAGNESIUM OXIDECADMIUMSmelting ProcessesCOPPER SMELTINGLEAD SMELTINGZINC SMELTINGTHE IMPERIAL SMELTING PROCESSHandling and Shipment of ConcentratesSmelter FEE SchedulesGENERAL CONDITIONS:SMELTER CHARGESTypical Smelter Treatment ChargesTypical Smelter SchedulesNon-Metallic MineralsMajor Metals The object

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Flotation Principles

Table of ContentsSURFACE TENSIONBULK-OILOIL AND AIRBUBBLESCOAGULATIONFROTH Flotation, in its latest phase, is a process of concentrating ores by frothing. When crushed ore, previously mixed with water and a relatively minute addition of oil, is agitated violently in the presence of air, a froth is formed. This froth, rising to the surface of the liquid mixture, is laden with sulphides or

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Rock Crushing Theory and Formula using Kick & Rittinger’s Law

Table of ContentsThe Two Laws:What about Bond?Rittinger’s Law:The Crushing-Surface Diagram:Kick’s Law:Method of Tests:Record of Tests:Summary of Results:Appendix: Rittinger’s theory and law of the energy expended in crushing of rock is that the work of crushing is proportional to the reduction in diameter; or, as I have more fully expressed it: “The work done in crushing is proportional to the surface

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Designs for Small Portable and Mobile Gold Leaching Plant

    Agitation capacity based on 36 to 48 hours of agitation time. Thickener area based on 6 to 7 square feet per ton of dry solids per 24 hours. Pregnant cyanide solution (Primary Thickener Overflow) is treated in a Precipitation System which includes: Clarifier, Vacuum Tank, Vacuum Pump, Clarifier Pump, Zinc Dust Feeder, Zinc Mixing Tank with Pump, and

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Flotation Deinking Paper Recycling De-Inking Waste Paper

The pulping consisted of disintegration of the wastepaper structure and dispersion of the fibers. The disintegration was accomplished by conditioning 250 grams of wastepaper, under moderate agitation, with hot steam (84 to 90 °C), de-ionized water and reagent as desired. After disintegration the pulp was further dispersed in a high speed blender. All pulping experiments were done at a consistency

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