Bauxite tailings
Bauxite tailings, also known as bauxite residue, red mud, red sludge, or alumina refinery residues, is a highly alkaline waste product composed mainly of iron oxide that is generated in the industrial production of alumina. It is important to differentiate between the alkaline waste generated in the Bayer process and the tailings generated during the mining of bauxite. This article specifically covers the alkaline waste generated when operating the Bayer process. The scale of production makes the waste product an important one, and issues with its storage are reviewed and every opportunity is explored to find uses for it.
Over 95% of the alumina produced globally is through the Bayer process; for every tonne of alumina produced, approximately 1 to 1.5 tonnes of bauxite tailings/residue are also produced. Annual production of alumina in 2018 was approximately 126 million tonnes resulting in the generation of over 160 million tonnes of bauxite tailings/residue.
Production
Red mud, or bauxite residue, is a side-product of the Bayer process, the principal means of refining bauxite en route to alumina. The resulting alumina is the raw material for producing aluminium by the Hall–Héroult process. A typical bauxite plant produces one to two times as much red mud as alumina. This ratio is dependent on the type of bauxite used in the refining process and the extraction conditions.There are over 60 manufacturing operations across the world using the Bayer process to make alumina from bauxite ore. Bauxite ore is mined, normally in open cast mines, and transferred to an alumina refinery for processing. The alumina is extracted using sodium hydroxide under conditions of high temperature and pressure. The insoluble part of the bauxite is removed, giving rise to a solution of sodium aluminate, which is then seeded with an aluminium hydroxide crystal and allowed to cool which causes the remaining aluminium hydroxide to precipitate from the solution. Some of the aluminium hydroxide is used to seed the next batch, while the remainder is calcined at over 1000 °C in rotary kilns or fluid flash calciners to produce aluminium oxide.
The alumina content of the bauxite used is normally between 45 - 50%, but ores with a wide range of alumina contents can be used. The aluminium compound may be present as gibbsite, boehmite or diaspore. The tailings/residue invariably has a high concentration of iron oxide which gives the product a characteristic red colour. A small residual amount of the sodium hydroxide used in the process remains with the tailings, causing the material to have a high pH/alkalinity, normally >12. Various stages in the solid/liquid separation process are introduced to recycle as much sodium hydroxide as possible from the residue back into the Bayer Process in order to make the process as efficient as possible and reduce production costs. This also lowers the final alkalinity of the tailings making it easier and safer to handle and store.
Composition
Red mud is composed of a mixture of solid and metallic oxides. The red colour arises from iron oxides, which comprise up to 60% of the mass. The mud is highly basic with a pH ranging from 10 to 13. In addition to iron, the other dominant components include silica, unleached residual alumina, and titanium oxide.The main constituents of the residue after the extraction of the aluminium component are insoluble metallic oxides. The percentage of these oxides produced by a particular alumina refinery will depend on the quality and nature of the bauxite ore and the extraction conditions. The table below shows the composition ranges for common chemical constituents, but the values vary widely:
Chemical | Percentage composition |
Fe2O3 | 5–60% |
Al2O3 | 5–30% |
TiO2 | 0–15% |
CaO | 2–14% |
SiO2 | 3–50% |
Na2O | 1–10% |
Mineralogically expressed the components present are:
Chemical name | Chemical formula | Percentage composition |
Sodalite | 3Na2O⋅3Al2O3⋅6SiO2⋅Na2SO4 | 4–40% |
Cancrinite | Na3⋅CaAl3⋅Si3⋅O12CO3 | 0–20% |
Aluminous-goethite | α-OOH | 10–30% |
Hematite | Fe2O3 | 10–30% |
Silica | SiO2 | 5–20% |
Tricalcium aluminate | 3CaO⋅Al2O3⋅6H2O | 2–20% |
Boehmite | AlO | 0–20% |
Titanium dioxide | TiO2 | 0–10% |
Perovskite | CaTiO3 | 0–15% |
Muscovite | K2O⋅3Al2O3⋅6SiO2⋅2H2O | 0–15% |
Calcium carbonate | CaCO3 | 2–10% |
Gibbsite | Al3 | 0–5% |
Kaolinite | Al2O3⋅2SiO2⋅2H2O | 0–5% |
In general, the composition of the residue reflects that of the non-aluminium components, with the exception of part of the silicon component: crystalline silica will not react but some of the silica present, often termed, reactive silica, will react under the extraction conditions and form sodium aluminium silicate as well as other related compounds.
Environmental hazards
Discharge of red mud is hazardous environmentally because of its alkalinity, though it should be stressed that all disposal to rivers or sea has now stopped.In 1972 there was a red mud discharge off the coast of Corsica by the Italian company Montedison. The case is important in international law governing the Mediterranean sea.
In October 2010, approximately one million cubic meters of red mud from an alumina plant near Kolontár in Hungary was accidentally released into the surrounding countryside in the Ajka alumina plant accident, killing ten people and contaminating a large area.
All life in the Marcal river was said to have been "extinguished" by the red mud, and within days the mud had reached the Danube. However, the long-term environmental effects of the spill have been minor.
Residue storage areas (RSA)
Tailings storage methods have changed substantially since the original plants were built. The practice in early years was to pump the tailings slurry, at a concentration of about 20% solids, into lagoons or ponds sometimes created in former bauxite mines or depleted quarries. In other cases, impoundments were constructed with dams or levees, while for some operations valleys were dammed and the tailings deposited in these holding areas.It was once common practice for the bauxite residue/tailings to be discharged into rivers, estuaries, or the sea via pipelines or barges; in other instances the residue was shipped out to sea and disposed of in deep ocean trenches many kilometres offshore. All disposal in the sea, estuaries and rivers has now stopped.
As residue storage space ran out and concern increased over wet storage, since the mid-1980s dry stacking has been increasingly adopted. In this method, tailings are thickened to a high density slurry, and then deposited in a way that it consolidates and dries.
An increasingly popular treatment process is filtration whereby a filter cake is produced. This cake can be washed with either water or steam to reduce alkalinity before being transported and stored as a semi-dried material. Residue produced in this form is ideal for reuse as it has lower alkalinity, is cheaper to transport, and is easier to handle and process.
In 2013 Vedanta Aluminium, Ltd. commissioned a red mud powder-producing unit at its Lanjigarh refinery in Odisha, India, describing it as the first of its kind in the alumina industry, tackling major environmental hazards.
Use
Since the Bayer process was first adopted industrially in 1894, the value of the remaining oxides has been recognized. Attempts have been made to recover the principal components – especially the iron. Since mining began, an enormous amount of research effort has been devoted to seeking uses for the residue.Many studies have been conducted to develop uses of red mud. An estimated 2 to 3 million tonnes are used annually in the production of cement, road construction and as a source for iron. Potential applications include the production of low cost concrete, application to sandy soils to improve phosphorus cycling, amelioration of soil acidity, landfill capping and carbon sequestration.
Reviews describing the current use of bauxite residue in Portland cement clinker, Supplementary Cementious materials/blended cements and special calcium sulfo-aluminate cements have been extensively research and well documented.
- Cement manufacture, use in concrete as a supplementary cementitious material. From 500,000 to 1,500,000 tonnes.
- Raw material recovery of specific components present in the tailings/residue: iron, titanium, steel and REEs production. From 400,000 to 1,500,000 tonnes;
- Landfill capping/roads/soil amelioration – 200,000 to 500,000 tonnes;
- Use of the bauxite residue as a component in building or construction materials – 100,000 to 300,000 tonnes;
- Other – 100,000 tonnes.
- Use in building panels, bricks, foamed insulating bricks, tiles, gravel/railway ballast, calcium and silicon fertilizer, refuse tip capping/site restoration, lanthanides recovery, scandium recovery, gallium recovery, yttrium recovery, treatment of acid mine drainage, adsorbent of heavy metals, dyes, phosphates, fluoride, water treatment chemical, glass ceramics, ceramics, foamed glass, pigments, oil drilling or gas extraction, filler for PVC, wood substitute, geopolymers, catalysts, plasma spray coating of aluminium and copper, manufacture of aluminium titanate-Mullite composites for high temperature resistant coatings, desulfurisation of flue gas, arsenic removal, chromium removal.
Additional references
- M. B. Cooper, “Naturally Occurring Radioactive Material in Australian Industries”, EnviroRad report ERS-006 prepared for the Australian Radiation Health and Safety Advisory Council.
- Agrawal, K. K. Sahu, B. D. Pandey, "Solid waste management in non-ferrous industries in India", Resources, Conservation and Recycling 42, 99–120.
- Jongyeong Hyuna, Shigehisa Endoha, Kaoru Masudaa, Heeyoung Shinb, Hitoshi Ohyaa, "Reduction of chlorine in bauxite residue by fine particle separation", Int. J. Miner. Process., 76, 1-2,, 13–20.
- Claudia Brunori, Carlo Cremisini, Paolo Massanisso, Valentina Pinto, Leonardo Torricelli, "Reuse of a treated red mud bauxite waste: studies on environmental compatibility", Journal of Hazardous Materials, 117,, 55–63.
- H. Genc¸-Fuhrman, J. C. Tjell, D. McConchie, "Increasing the arsenate adsorption capacity of neutralized red mud ", J. Colloid Interface Sci. 271 313–320.
- H. Genc¸-Fuhrman, J. C. Tjell, D. McConchie, O. Schuiling, "Adsorption of arsenate from water using neutralized red mud", J. Colloid Interface Sci. 264 327–334.