Patent Description:
A froth flotation arrangement is used for treating mineral ore particles suspended in slurry. An example of such arrangements are the <NPL>).

An object of the present invention is to provide a froth flotation arrangement and a method for treating mineral ore particles suspended in slurry. The objects of the invention are achieved by a method and an arrangement which are characterized by what is stated in the independent claims. The preferred embodiments of the invention are disclosed in the dependent claims.

The invention is based on an arrangement for treating mineral ore particles suspended in slurry, comprising a flotation cell for separating the slurry into an underflow and an overflow. The arrangement comprises.

the froth collection launders (<NUM>) are positioned in radial direction (r) of the tank (<NUM>) and an average froth transport distance (dtr) is less than <NUM>.

The invention is based on a froth flotation method for treating mineral ore particles suspended in slurry, and in the method separating the slurry in a flotation cell into an underflow and an overflow, the method comprising the steps of:.

An effect of the method and arrangement of the invention is that reduced available froth area on the top of the tank leads to a good froth recovery since the transport distance of the fragile bubble particle aggregate to a froth collection launder is reduced. Further, the reduced horizontal transport distance takes more relevance for the recovery of coarse particles. <CIT> proposes an active mechanism for controlling the flooding and displacement of the foam within the flotation tank.

<FIG> shows a top view of a froth flotation arrangement for treating mineral ore particles suspended in slurry. <FIG> shows a side view of the arrangement shown in <FIG>. The froth flotation arrangement comprises a flotation cell <NUM> which separates the slurry <NUM> into an underflow <NUM> and an overflow <NUM>.

Froth flotation is a physical separation method for separating particles based on differences in the ability of air bubbles to selectively adhere to specific mineral surfaces in a mineral/water slurry. If a mixture of hydrophobic and hydrophilic particles are suspended in water, and air is bubbled through the suspension, then the hydrophobic particles will tend to attach to the air bubbles.

The tank <NUM> of the flotation cell <NUM> contains slurry <NUM> which is a mixture of solid particles in a carrier liquid, e.g. mineral particles in water. The bubble-particle aggregates move up in the froth flotation cell <NUM> by buoyancy forming a froth <NUM> layer on the surface. The froth <NUM> comprises water, bubbles and particles.

The tank <NUM> is mechanically agitated. The tank <NUM> comprises an impeller <NUM> within the tank <NUM> and a gas supply <NUM>. The agitator <NUM> disperses air in the slurry <NUM>, pumps slurry <NUM>, keeps solids in the suspension and provides an environment in the cell tank <NUM> for interaction of bubbles and hydrophobic particles and their subsequent attachment and therefore separation of valuable mineral particles from the undesired gangue mineral particles. The agitator <NUM> comprises an impeller <NUM> and a drive assembly for rotating the impeller <NUM>. Further, the agitator <NUM> may also comprise a stator <NUM> for providing a more stable air dispersion. The drive assembly may comprise a motor <NUM> and a drive shaft <NUM>.

A gas supply <NUM> to the froth flotation cell <NUM> comprises pressurized or self-aspirating gas supply. Examples of pressurized gas supply systems are pipes or tubes delivering gas to the bottom part of the tank <NUM> at least partly under the impeller <NUM>. Gas may be supplied to the impeller <NUM> area also through conduits formed to the agitator <NUM> comprising the impeller <NUM>.

The tank <NUM> volume is preferably large and comprises at least <NUM><NUM>. The tank <NUM> volume comprises the volume of the tank <NUM> surrounding the slurry <NUM> measured from the bottom <NUM> of the tank <NUM> to height h2 of a froth overflow lip <NUM> of the froth collection launder <NUM>. The tank <NUM> may comprise smaller cylindrical containers within it. Large tank <NUM> volumes have benefits such as lower capital, operating and maintenance costs.

The tank <NUM> further comprises a froth collection launder <NUM> comprising a froth overflow lip <NUM>. The froth collection launder <NUM> is capable to receive the overflow <NUM>. <FIG> shows a perspective view of two froth collection launders <NUM>. The froth collection launder <NUM> collects the froth <NUM> from the surface, i.e. the overflow <NUM>, and transports it out of the tank <NUM> of the froth flotation cell <NUM>. The froth collection launder <NUM> is an inclined drainage module. The froth <NUM> layer level is generally above the froth overflow lip <NUM> of the launder <NUM> permitting the froth <NUM> to flow over the overflow lip <NUM>. The froth collection launder <NUM> comprises a subsurface discharge pipe <NUM> for carrying the froth <NUM> or concentrate product, i.e. the overflow <NUM>, from the launder <NUM> to outside of the tank <NUM>, for instance.

The froth flotation cell <NUM> can have one or more froth collection launders <NUM> which can be either internal or external, double, radial, depending on the capacity of the froth collection launder <NUM> necessary for the froth <NUM> removal. An internal launder means a froth collection launder <NUM> which is positioned at least partially above the pulp area Apulp.

In the arrangement in the froth flotation cell <NUM> the ratio between an available froth surface area and the pulp area A froth/A pulp is less than <NUM>,<NUM>, where the pulp area A pulp is calculated as an average from the cross sectional areas of the tank <NUM> at the height of the impeller h1. The available froth surface area A froth is the horizontal area at the top of the tank <NUM> which is open for the froth <NUM> to flow at the height h of the lip <NUM> of the froth collection launder <NUM>. The available froth surface area A froth is the dashed froth <NUM> areas shown in <FIG>, <FIG> and <FIG>. This reduced available froth surface area Afroth on the top of the tank <NUM> shortens the transport distance of the fragile bubble particle aggregate to a froth collection launder or launders <NUM>. Solid particles are an important component of the froth <NUM> structure and adequate solid particles will also lead to a high froth <NUM> stability and a better transportation of the froth <NUM> to the launder lip. A better particle recovery is then obtained and especially with coarse particles. Additionally, the reduced available froth surface area A froth stabilizes the froth <NUM> by creating a thicker froth <NUM> layer as a flotation cell <NUM> with a high froth surface area could lead to a situation where insufficient material with solid particles is present to stabilize the froth <NUM>.

The ratio between a height h from a bottom <NUM> of the tank <NUM> to the lip <NUM> of the froth collection launder <NUM> and the diameter D of the tank <NUM> at the height of the impeller h/D is less than <NUM>,<NUM>. This means the tank <NUM> is relatively shallow.

The third flotation cell 1or subsequent flotation cell <NUM> in the series of connected flotation cells <NUM> has a ratio between the available froth surface area and the pulp area A froth/A pulp less than <NUM>,<NUM>.

The arrangement provides a high concentrate content to the overflow <NUM> of the flotation cell <NUM> even when the slurry <NUM> fed to the flotation cell <NUM> is diluted, i.e. the flotation cell <NUM> receives an underflow <NUM> resulting from a multiple of previous flotation cells <NUM>. A shallow tank <NUM> having a relatively large pulp area A pulp provides a long residence time for the particles in the slurry <NUM> to meet air bubbles and create air bubble particle aggregates. The significance of the residence time increases with decreasing concentrate content of the inlet slurry <NUM>. The reduced available froth surface area A froth creats a thicker froth <NUM> layer and results in a more pure froth <NUM>. In an embodiment the ratio between a height h from a bottom of the tank <NUM> to the froth overflow lip <NUM> of the froth collection launder <NUM> and the diameter D of the tank h/D is less than <NUM>,<NUM>. This means the tank <NUM> is shallow.

In an embodiment the ratio between the available froth surface area and the pulp area A froth/A pulp is from <NUM>,<NUM> to <NUM>,<NUM>. The decrease in the available surface area A froth for the froth <NUM> to flow causes the rising particles to flow also in a horizontal direction. In order to keep the froth <NUM> layer stabile the ratio is preferably not below the lower limit.

The periphery shape of the froth collection launder <NUM> shape may correspond the tank <NUM> periphery shape. The shape of the froth collection launder <NUM> may be circular or rectangular, for instance.

The reduction of the available froth surface area A froth is preferably made at the periphery of the tank <NUM>. This is advantageous as in the middle of the tank <NUM> are more gas bubbles than in the periphery. The reduction of the available froth surface area A froth can be implemented by means of an internal peripheral launder <NUM>, or a froth blocker <NUM>, for instance. An internal peripheral type of a froth collection launder <NUM> extends around the inside top of the sidewall of the tank <NUM> as shown in <FIG>.

If the tank <NUM> comprises either an internal peripheral launder <NUM> or a peripheral froth blocker <NUM>, the available froth surface area A froth may be defined by subtracting a launder area A launder which is the area covered by froth collection launders <NUM> at the height h2 of the froth overflow lip <NUM>, and a blocker area which is the area not available for the froth <NUM> and not covered by the froth collection launders <NUM> at the height h2 of the lip <NUM> of the froth collection launder <NUM> from the pulp area A pulp.

As an example, the ratio between the area of the internal peripheral launder and the pulp area A int launder/A pulp, or the ratio between the area of the peripheral froth blocker and the pulp area A blocker/A pulp, is more than <NUM>,<NUM>, preferably more than <NUM>,<NUM> and less than <NUM>,<NUM>. The angle of ascent for the air bubble particle aggregates limits the amount of the froth surface area which can be reduced. If the angle of descent becomes too low-gradient the air bubble particle aggregates start forming air pockets causing the particles to drop back.

In an embodiment the tank <NUM> is circular in cross section at the froth overflow lip height h2 of the tank <NUM> as shown in <FIG>. Further, the froth collection launders <NUM> are circular shaped and positioned coaxially as shown in <FIG>. A circular tank <NUM> provides a more stable air bubble dispersion causing a more stable froth layer as the impeller <NUM> is positioned in the middle of the tank <NUM> producing a circular shaped air bubble zone.

<FIG> presents an embodiment comprising two froth collection launders <NUM>, and the first launder <NUM> is arranged within the second launder <NUM> at a distance apart d<NUM>. The froth collection launders <NUM> comprise circular peripheries.

The average froth transport distance dtr is less than <NUM> and more than <NUM> with circular shaped and coaxially positioned froth collection launders <NUM>. The average froth transport distance dtr is the distance the froth <NUM> has to travel in horizontal direction before reaching the froth overflow lip <NUM>. The average froth distance dtr is calculated as a ratio between the sum of the transport distances between the froth collection launders <NUM> and the number of the froth collection launders <NUM> (d<NUM>+d<NUM>+. If two launders <NUM> have overflow lips <NUM> facing each other the transport distance is half of the distance between the two launders <NUM>, e.g. half of the distance between the froth overflow lips <NUM>. When two launders <NUM> have an overflow lip <NUM> and a launder side wall facing each other the transport distance is the distance between the two launders <NUM>, e.g. the distance between the froth overflow lip <NUM> and the side wall.

If the average froth transport distance dtr is too long some particles of the air bubble agglomerates may detach and flow downwards. This froth drop back reduces the froth recovery to the froth collection launders <NUM>.

The tank <NUM> may comprise at least three separate froth collection launders <NUM>, and the number of froth overflow lips <NUM> in the froth collection lounders <NUM> is five as shown in <FIG>. The outer froth collection launder <NUM> comprises an internal peripheral launder with one froth overflow lip <NUM>. The other two internal froth collection launders <NUM> comprise two froth overflow lips <NUM> each. This arrangement reduces the drop back of the air bubble particle agglomerates as the transport distance to a froth collection launder <NUM> is shorter compared to a case where there is only one froth collection lauder <NUM>.

<FIG> shows an embodiment where the froth flotation cell <NUM> comprises two froth collection launders <NUM> and a froth blocker <NUM>, a cone blocker in the middle of the tank <NUM>. The available froth surface area A froth is further reduced with a peripheral froth blocker <NUM>. The outer froth collection launder <NUM> has two froth overflow lips <NUM>. The inner froth collection launder <NUM> has one froth overflow lip <NUM> facing the froth blocker <NUM>.

In another embodiment the froth collection launders <NUM> are positioned in radial direction r of the tank <NUM> as shown in <FIG>.

The average froth transport distance dtr is less than <NUM> and more than <NUM> with froth collection launders <NUM> positioned in radial direction r of the tank <NUM>. The average froth distance is calculated as a ratio between the sum of the transport distances between the froth collection launders <NUM> and the number of the froth collection launders (d<NUM>+d<NUM>+. The transport distance between two launders <NUM> having overflow lips <NUM> facing each other is half of the distance between the two launders. The transport distance between two launders <NUM> having an overflow lip <NUM> and a launder side wall facing each other is the distance between the two launders. The distance between two launders <NUM> is an average of the distances between the first ends and the second ends of the two radially directed r launders <NUM>.

Further, in an embodiment comprising froth collection launders <NUM> in a peripheral direction of the tank <NUM> a ratio between the average transport distance dtr and a froth collection launder <NUM> average width in radial direction dtr/w is <NUM>,<NUM>-<NUM>,<NUM>. This ratio provides adequate size for the froth collection launder <NUM> to receive the flowing froth <NUM> overflow. If the froth collection launder <NUM> is too narrow compared to the amount of the overflowing froth <NUM> the transporting capacity of the launder is exceeded and the launder is clogged <NUM>. In <FIG> the average transport distance dtr is d<NUM>/<NUM>.

In a froth flotation method for mineral ore particles suspended in slurry <NUM> are treated. In the method the slurry <NUM> in a flotation cell <NUM> is separated into an underflow <NUM> and an overflow <NUM>. The method comprises the steps of: connecting at least three flotation cells <NUM> in series for creating a primary line <NUM>, feeding the slurry <NUM> to a tank <NUM> of the flotation cell <NUM>, wherein each subsequent flotation cell <NUM> is receiving the underflow <NUM> from the previous flotation cell <NUM>, introducing gas into the tank <NUM> through a gas supply <NUM>, mixing the slurry <NUM> and the gas with an impeller <NUM> within the tank <NUM>, providing the tank <NUM> with a volume of at least <NUM> m3, receiving the overflow <NUM> in a froth collection launder <NUM> provided in the flotation cell <NUM>, receiving the overflow <NUM> over a froth overflow lip <NUM> provided in the froth collection launder <NUM>, forming an available froth surface area A froth in the flotation cell <NUM>, the flotation cell <NUM> having a pulp area A pulp, where the pulp area A pulp is calculated as an average from the cross sectional areas of the tank <NUM> at the height h1 of the impeller <NUM>, providing the tank <NUM> with a ratio between a height h from a bottom <NUM> of the tank <NUM> to the froth overflow lip <NUM> of the froth collection launder <NUM> and the diameter D of the tank <NUM> at the height h1 of the impeller <NUM> of a pulp area h/D being less than <NUM>,<NUM>, feeding the underflow <NUM> to the third flotation cell <NUM> or subsequent flotation cell <NUM> in the series wherein a ratio between an available froth surface area and the pulp area A froth/A pulp comprises less than <NUM>,<NUM>.

Further, in the froth flotation method the ratio between a height h from a bottom <NUM> of the tank <NUM> to the froth overflow lip <NUM> of a froth collection launder <NUM> and the diameter D of the tank is less than <NUM>,<NUM>, for instance.

<FIG> shows a primary line <NUM> in a froth flotation arrangement. The primary line <NUM> comprises at least three flotation cells <NUM> connected in series as shown in <FIG>. Each flotation cell <NUM> separates the slurry <NUM> into an underflow <NUM> and an overflow <NUM>. Each subsequent flotation cell <NUM> is arranged to receive the underflow <NUM> from the previous flotation cell <NUM>.

The presented arrangement and method are suitable for a slurry <NUM> comprising copper (Cu), for instance. The slurry <NUM> fed to the third flotation cell <NUM> or subsequent cell in the series may comprise copper (Cu) less than <NUM>,<NUM> weight %.

It will be obvious to a person skilled in the art that, as the technology advances, the inventive concept can be implemented in various ways. The invention and its embodiments are not limited to the examples described above but may vary within the scope of the claims.

Part list: <NUM> a flotation cell; <NUM> slurry, <NUM> an underflow; <NUM> an overflow; <NUM> a tank; <NUM> a froth; <NUM> an impeller; <NUM> a gas supply; <NUM> an agitator; <NUM> a stator; <NUM> a motor; <NUM> a drive shaft; <NUM> a bottom; <NUM> an overflow lip; <NUM> a froth collection launder; <NUM> a discharge pipe; <NUM> a froth blocker; <NUM> a primary line.

Claim 1:
A froth flotation arrangement for treating mineral ore particles suspended in slurry, comprising a flotation cell (<NUM>) for separating the slurry (<NUM>) into an underflow (<NUM>) and an overflow (<NUM>), wherein the arrangement comprises:
- a primary line (<NUM>) comprising at least three flotation cells (<NUM>) connected in series, wherein each subsequent flotation cell (<NUM>) is arranged to receive the underflow (<NUM>) from the previous flotation cell (<NUM>),
- the flotation cell (<NUM>) comprising a tank (<NUM>), and the flotation cell (<NUM>) comprising an impeller (<NUM>) within the tank (<NUM>), and
- the flotation cell (<NUM>) comprising g a gas supply (<NUM>) within the tank (<NUM>),
- the tank (<NUM>) comprising a volume of at least <NUM><NUM>,
- the flotation cell (<NUM>) comprising a froth collection launder (<NUM>) capable to receive the overflow (<NUM>),
- the froth collection launder (<NUM>) comprising a froth overflow lip (<NUM>),
- the flotation cell (<NUM>) having an available froth surface area (A froth),
- the flotation cell having a pulp area (A pulp), where the pulp area (A pulp) is calculated as an average from the cross sectional areas of the tank (<NUM>) at the height (h1) of the impeller (<NUM>),
- a ratio between a height (h) from a bottom (<NUM>) of the tank (<NUM>) to the froth overflow lip (<NUM>) of the froth collection launder (<NUM>) and the diameter (D) of the tank (<NUM>) at the height (h1) of the impeller (<NUM>) (h/D) is less than <NUM>,<NUM>,
- characterized in that the third flotation cell (<NUM>) or subsequent flotation cell (<NUM>) in the series has a ratio between an available froth surface area and the pulp area (A froth/A pulp) less than <NUM>,<NUM>; and that
the froth collection launders (<NUM>) are positioned in radial direction (r) of the tank (<NUM>) and an average froth transport distance (dtr) is less than <NUM>.