Flash Flotation with Closed Circuit Grinding

The reason why you need Flash Flotation in a Closed Grinding Circuit relates to “Recovering your mineral as soon as free” which has long been recognized in ore dressing practice. This not only applies to gravity treatment but also to flotation. For this application the Flash Flotation Cell was developed for use in the grinding circuit and has done a remarkable job in many plants.

Flash Flotation with Closed Circuit Grinding

4 Options for Flash Flotation in a Closed Circuit Grinding Plant

A greater amount of granular higher grade concentrates can be produced and, in general, overall plant recovery is improved by reducing slime losses due to overgrinding and colliding of high specific gravity minerals.

Closed Circuit Grinding Flowsheets with Flash Flotation Embedded

Typical flowsheets are shown to indicate a few of the possible applications of Flash Cells in grinding circuits. In recent years the successful application of hydraulic cyclones, rubber lined pumps, and two stage grinding circuits have enhanced the feasibility of unit cell applications. Cyclones in particular have increased the flexibility of such applications by permitting positive and continuous gravity flow of unit cell tailings to subsequent treatment steps.

Closed Circuit Grinding FLOWSHEET #1

In this flowsheet the Unit Cell is placed between the ball mill and classifier to remove mineral which is free and ready to float.

Molded rubber wearing parts are used exclusively in unit cells. If wear is severe due to coarse abrasive solids, a special molded soft rubber compound is available which greatly extends the impeller and wearing plate life. Conical disk impellers and wearing plates are standard for unit cell applications.

A mineral cone in the bottom of the unit cell is advisable. It acts as a trap for high specific gravity coarse mineral, grinding media fragments and other foreign material.

Closed Circuit Grinding FLOWSHEET #2

Two stage classification is shown in this flowsheet with a Unit Cell between the classifiers. The primary classifier may overflow as coarse as 20 mesh and at densities up to 50% solids. This is ideal feed for the unit cell. Unit cell tailings are classified through a cyclone and the oversize returned to the ball mill for further grinding. The cyclone classifier overflow, 65 mesh or finer, is treated by regular bulk or selective flotation.

With this two stage classification system the unit cell can be conveniently located to deliver a positive gravity discharge of pulp to the pump feeding the cyclone. The pump sump box can be made a part of the unit cell tank if desired.

Closed Circuit Grinding FLOWSHEET #3

Two stage grinding and classification is provided in this flowsheet which is generally applicable to larger tonnage installations in which a substantial percentage of the values can be recovered directly from the grinding circuit. The primary Rod Mill in open circuit will reduce crushed ore to approximately minus 10 mesh. A Mineral Jig is recommended if coarse mineral and metallics are present.

The spiral or rake classifier overflow passes to the unit cell and on to classification and regrinding. High grade unit cell concentrates can be produced with this system, and on low ratio of concentration ores a substantial increase in mill capacity is possible. Slime losses are greatly minimized with this combination jig and unit cell circuit.

Closed Circuit Grinding FLOWSHEET #4

The trend in many of the large tonnage milling circuits is to completely eliminate conventional rake or spiral classifiers by going to two stage grinding with a rod and ball mill  in series. The rod mill discharge goes direct to the ball mill and then on to a pump and hydraulic cyclone classifier. These modern grinding and classification circuits are ideal for including the unit cell as the primary mineral recovery step.

One large copper operation with two stage grinding and cyclone classification, actually treats cyclone underflow, — 20 plus 100 mesh, through Unit Cells. The unit cells recover a substantial percentage of the total copper in final concentrate form. The unit cell tailings at 55% solids return by gravity to the regrind ball mill feed. Since incorporating the unit cells and by careful checking between parallel circuits, it has been established by “recovering the mineral as soon as free” that final mill tailings were reduced by ¼ lb. copper per ton.


Unit Flash Cell flotation tests should be made before planning an installation. This will establish if the ore will respond to such treatment to advantage. A 100 lb. representative sample of the ball mill feed is sufficient for the unit cell flotation tests.

SRL pump feeding

Flotation in a Grinding Circuit

The simplest flotation circuit is a comparatively recent innovation. It consists of the introduction of a flotation cell into the grinding circuit between ball mill and classifier as shown below. The discharge end of the mill is fitted with a trommel screen with openings about 4 mesh in size to separate out coarse material, which is laundered direct to the classifier ; the remainder of the pulp passes to the flotation cell where most of the mineral which has been released from the gangue is taken off as a concentrate, the necessary reagents having been added at some previous point in the circuit, usually at the mill feed box. Flotation can be carried out in a pulp containing as much as 65% of solids, but water is added in most cases to bring the W/S ratio to about 1/1. In such a thick, heavy pulp it is possible to float particles as coarse as 10 mesh. At this size, however, only pure mineral will adhere to a bubble, for which reason the concentrate is generally of unusually high grade.Flotation Cell in Tube Mill

The advantage of this method of flotation is that the valuable minerals are removed from the circuit as soon as they have been released from the gangue, so that their accumulation in the classifier is prevented and the possibility of overgrinding them is reduced. Moreover, the granular nature of the particles floated assists considerably in the subsequent filtration of the combined flotation concentrate. It is a simple matter to instal the cell in the ball mill circuit, since it fits readily into the space between mill and classifier and occasions no loss of head. The only disadvantage is the heavy wear to which the interior of the cell is subjected by the coarse material passing through it, but the modern method of lining both moving and stationary parts with rubber reduces this difficulty to minor proportions.

Mcintyre Porcupine Mines, Ltd., was one of the first companies to practise flotation in the grinding circuit. Their installation is described later in the paragraph headed “Flotation of Gold and Silver Ores . Others soon also adopted the method. In their plant grinding is carried out in a Hardinge Ball Mill in closed circuit with a Dorr Classifier, and a “ Sub-A” Cell is employed as the flotation unit between the two, the pulp being maintained at a density of 65% solids. Under normal operating conditions 60-70% of the copper and 40% of the nickel are recovered in the grinding circuit. Subsequent flotation in “ Sub-A” Machines gives a total recovery of nearly 99% of the copper and over 94% of the nickel. No attempt is made to separate the copper from the nickel minerals.

The process can be adapted to the selective flotation of complex ores. Another mill for instance, where a lead-zinc ore is treated by two-stage selective flotation, the method being very similar to the standard procedure described in the paragraph entitled “ Flotation of Lead-Zinc Ores ”, the installation of a cell between ball mill and classifier has resulted in the removal of most of the galena before the pulp passes to the main flotation circuit. The sphalerite in the ore is so finely intermixed with a portion of the galena that, although a large proportion of the latter mineral is actually liberated at a comparatively coarse mesh, it is necessary to reduce the whole tonnage to 87% minus 200 mesh in order to separate the two minerals at all completely. Before flotation in the grinding circuit was tried, three stages of cleaning were required to make a high- grade lead concentrate, and 96% of the finished product would pass through a 325-mesh screen, only a trace remaining on 200 mesh. The introduction of a “ Sub-A” Cell into the grinding circuit enabled over 70% of the lead to be recovered in one operation without cleaning in a concentrate running 65-70% lead. The concentrate contains only 53% of minus 325-mesh material, 25% remaining on 200 mesh, and, being more granular than that obtained in the main flotation circuit, it gives better filtration. The total recovery remains much the same as before. Reagents are added in the ball mill feed box, and the pulp is maintained in the cell at about 58% solids.

There is no necessity to limit the size of the flotation machine between ball mill and classifier to a single cell, through the use of a multi-cell or a long pneumatic machine would involve changing the relative positions of the three units from the present standard arrangement. The trend of progress indicates that the flotation machine may become in some cases as important a factor in the proper classification of the ore during grinding as the classifier itself is at present.


Source: This article is a reproduction of an excerpt of “In the Public Domain” documents held in 911Metallurgy Corp’s private library.

By | 2018-04-01T10:14:49+00:00 April 14th, 2016|Categories: Ball Mills, Classification, Flotation, Flowsheets & Flowcharts, Grinding|Comments Off on Flash Flotation with Closed Circuit Grinding

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