Features

Declining ore grades require finer grind size for maximum mineral recovery

Global ore grades are declining while commodity demands continue to rise.

These ore bodies are increasingly complex, requiring a finer grind size for maximum mineral recovery and grade and are setting new challenges, particularly for grinding technology.

Energy efficiency is a major driving force and another challenge to address.

The High Intensity Grinding (HIG) mill has been designed specifically to manage these types of complex, fine grained ore-bodies that are rapidly becoming more economically viable.

While this technology has been utilised and proven for more than 30 years, further development, backed by intensive testwork, has resulted in the HIG mill now being available in the minerals processing industry.

The adaptability of the mill means it is suitable for a wide variety of processes and offers other benefits such as minimised energy usage of up to 40-50% compared with traditional ball mills.The adaptability of the mill means it is suitable for a wide variety of processes.

This offers other benefits such as minimised energy usage of up to 40-50% compared with traditional ball mills (see graph alongside).

In a typical application, the HIG process begins with the circuit feed being pumped to a scalping cyclone upstream of the mill.

The defined underflow is then mixed with water to optimal grinding density and pumped into the mill at base level.

The slurry enters a grinding chamber containing grinding media and rotating discs which provide momentum to stir the charge against a series of static discs.

As the flow transfers upwards, the ore slurry passes through the rotating discs and the free space between the static counter discs lining the wall.As the flow transfers upwards, the ore slurry passes through the rotating discs and the free space between the static counter discs lining the wall (see figure alongside).

Due to the vertical arrangement of the mill, classification is conducted simultaneously throughout the grinding process with larger particles remaining longer at the peripheral, while smaller particles move upwards.

The process is typically a single pass with no external classification necessary.

With the grinding media evenly distributed, the ore particles remain in constant contact, significantly increasing grinding efficiency.

Gravity keeps the media compact during operation, ensuring high intensity, inter-bead contact and efficient, even-energy transfer throughout the volume.

The disc configuration and the whole chamber geometry have been optimised for efficient energy transfer to the bead mass, internal circulation and classification.

Largest industrial units in operation

With installed power up to 5,000kW, the mill is the largest fine grinding unit in the market place to date.

This technology comes in various drum diameters and the mill heights can be varied to optimise the media load and power input for specific applications.

Chamber volumes range from 400 to 27,500 litres with corresponding drives from 132 to 5,000kW.

It is the only ultrafine grinding technology in commercial use that has the capability to use small size high density grinding media in mill sizes above 3,000kW.

Over 260 mills have been commissioned and proven in the marketplace.

Online particle size optimisation to maximise process

The HIGmill is able to optimise product fineness on-line. The energy efficiency remains constant through a wide shaft speed range.The HIGmill is able to optimise product fineness on-line. The energy efficiency remains constant through a wide shaft speed range.

The figure on the left depicts three different flow rates with specific grinding energy (SGE) versus product fineness.

Each SGE point has been generated by varying the shaft speed.

A feedback control principle is to measure the particle size distribution by an Outotec PSI on-line particle analyser and the shaft speed adjusted to maintain constant product size (see figure below).

A feedback control principle is to measure the particle size distribution by an Outotec PSI on-line particle analyser and the shaft speed adjusted to maintain constant product size.

In addition to feed back control feed forward control could be used to measure scalping cyclone feed quantity and adjust the mill shaft speed to reach target energy per total feed flow.

Compact and simple installation

The benefit of high power intensity and vertical installation is a very small footprint. The head room over the mill is small and the flanged, split shell construction reduces the space needed for maintenance.

The top-supported hanging arrangement keeps the floor and sides clear, simplifying maintenance and emptying the beads.

Gravity, together with an internal hydroclassifier, prevents the grinding media from escaping the mill by pushing the grinding beads back down into the milling process, letting through only the fine ground slurry.

Adaptability

A wide range of grinding applications can be addressed due to the excellent flexibility the mill has in adapting to fluctuating process conditions.

Typical application for the mill is the regrinding of concentrates (e.g. magnetic, flotation). The flows from these types of upstream processes can vary considerably due to fluctuations in ore grade and quality, as can the target fineness due to variations in the ore mineralogy.

Flow fluctuations in the mill can be dampened by maintaining the net energy constant via control of the mill shaft speed. Product fineness is also controlled by adjusting the shaft speed and thus power input.

If the conditions permanently change so that the current operational range is no longer optimal, the range can be optimised by changing volumetric media filling, bead size and/or bead material.

Both ceramic and steel beads can be used. In ultrafine grinding the typical bead diameter is 1-3mm and in coarser grinding 3-6mm.

Long maintenance intervals

The drum segments and wear components have been specifically designed to make maintenance simple and quick.

The casing is flanged vertically so that it can be split down the centre into two halves that can be moved apart on a railing system.

After exposing the internals, changing individual discs and liner segments can be performed by two skilled mechanical trade personnel.

Wear of the discs is even around the circumference. The wear is faster in the bottom part of the mill and typically the lowest discs have to be replaced a few times before the total set is changed.

For a complete change, a spare shaft ready for installation is an option available. Wear components can be lined with polyurethane, metal hard facing or natural rubber depending on application.

HIGmill delivery

The Mills are available with or without a mounting frame. Mills in brown field projects are typically supplied with a frame, while mills in green field projects are integrated into the concentrator building.

Typical delivery includes:

  • Scalping cyclone with feed pump
  • Feed, mixing and storage tanks
  • Feed pump
  • Media addition systems for grinding media
  • Motor and drive components
  • Gearbox and oil supply system
  • All instrumentation, controls and the motor control centre
  • PLC control with human machine interface (HMI)
  • Vertical process package engineering and plant model

Summary

This innovative and unique grinding technology provides advanced, energy efficient fine and ultra-fine grinding – particularly important for today’s more challenging ore bodies.

Suitable in either green or brownfield applications with its small footprint and high adaptability to process variations, HIG technology, at up to 5,000kW, delivers the highest installed power in the market place to date.

[Mattias Åstholm recently joined Outotec, taking on the role of Technology manager (HIGmills). Mattias has a Bachelor degree in Mining from the School of Mining, Filipstad, Sweden.

Andres Paz has a Bachelor degree in Engineering (Chemical Engineering) from Curtin University, Perth, Australia.  Since 2008 Andres has had various roles for Outotec in Process Equipment Testwork and Sales.  Andres’ current role is Process Engineer (Comminution) for the Grinding Mill product line.

Eddie Jamieson has a Bachelor degree in Science (Extractive Metallurgy) from Murdoch University of Perth, Australia.  Since 2003 Eddie has had various roles for Outotec in Metallurgy, Project Management and Sales having previously spent a number of years as a Metallurgist on various sites in Australia and overseas.  Eddie is currently the Principal Metallurgist (Comminution) for the Grinding Mill product line.]

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