kaolin clay mining and processing

beneficiation process of kaolinite clay: kaolin processing

beneficiation process of kaolinite clay: kaolin processing

Kaolin is an important industrial mineral having numerous uses and requiring various market specifications. High brightness kaolin clays represent a continuing challenge to the producer. An advancement in this field of Kaolinite Clay Beneficiation has been a patented process developed by Minerals and Chemicals Philipp Corporation and termed Ultra Flotation. Contaminants that are 1 micron and finer are separated from a feed which is virtually 100% finer than 3 microns and 48% finer than 0.5 microns. Removal of the contaminations by conventional froth flotation has never been commercially successful previously.

Ultra Flotation is a new concept of mineral separation that extends the flotation principle to the submicron range well beyond its present limits. The keyto Ultraflotation is the increased surface available for floating fine particles by the addition of a suitable carrier mineral usually in the 325 mesh range. In conventional flotation air bubbles alone do the job. In Ultra Flotation the reagentloadedslime particles to be floated attach themselves to the carrier mineral and are readily floated as a froth product.

The first step in processing kaolin clay is to slurry it in a blunger with water and a dispersing agent. Degritting using screens, cyclones and hydro-classifiers is the next step. The minus 325 mesh degritted clay is fractionated using centrifugal sizers to produce the fine fractions demanded by the various markets. Bleaching, filtering, and drying complete the general processing steps.

The flowsheet in this study follows the general steps outlined above but Ultraflotation is included to produce a high brightness product from the fine fraction. Bleaching alone will not produce the desired brightness.

The Ultraflotation feed (90-94% finer than 2 microns) is stored in a holding agitator and then pumped through a density and flow control apparatus to three Conditioners arranged in series. The mineral carrier (ground limestone, 200-400 lbs. per ton) and ammonium sulphate (4-8 lbs. per ton) are added to the first conditioner. The discharge from the final conditioner containing 20% solids is fed directly to a six cell High Energy Conditioner. An emulsion of tall oil (3-5 lbs. per ton), neutral calcium petronate (3-5 lbs. per ton), aqua ammonia (2-4 lbs. per ton), and water are added to the first cell of the high energy conditioner. The conditioned pulp has a pH of 9.0. Fuel oil (6-10 lbs. per ton) is added to the fourth conditioning cell.

A total of 24 Sub-A Flotation Machines (cell-to-cell design) are used for the flotation separation. The conditioned pulp is first floated in a six-cell machine and then this froth, which contains the mineral carrier and color contaminants, is successively refloated in stages using a six-cell machine for the first stage and four-cell machines for the second and third cleaning stages. Dilution water is added to each stage of flotation to maintain dilute pulp conditions. The rougher tailings and reflotation tailings are combinedand scavenged of any additional contaminant in a 4-cell Sub-A Flotation Machine. The tailings from this final flotation step represents the beneficiated kaolin and is pumped to a thickener. Sulphurous acid is added to the pump to produce a pH of 2.8 to 3.0 for flocculation.

The froth products from the reflotation and scavenging steps are combined and impounded. The principal contaminant removed in the Ultraflotation process is a titaniferous mineral which does not bleach and imparts a yellowish-brown cast to the finished kaolin if present. Typical results of the Ultra-flotation separation are shown in the table.

The Fe2O3 content, which affects the brightness of the clays is controlled by careful mining and by the reducing bleach using zinc hydrosulphite. The ferric iron is reduced to the ferrous state and the slip washed to remove soluble salts.

In general, Ultraflotation enhances the brightness of the kaolin by more than 5%. By incorporating bleaching for additional color improvement, the beneficiated product (Ultra White 90) has a brightness of 90-92. Brightness is a measurement of light reflectance by a standard method of the Technical Association of the Pulp and Paper Industry.

Brightness (G.E. brightness range)..90-92% Particle size percent finer than 2 microns90-94% Maximum screen residue wet, 325 mesh..0.005% Refractive index.1.56% Specific gravity2.58 pH range6.3-7.0

Ultra White 90 is a pre-dispersed premium clay that has applications in the filling of high quality papers to reduce TiO2 requirement for brightness and in coatings for high brightness, easier finishing, gloss improvements and ink holdout. It is available in bulk, slurry, or bags and is produced by the Ultra-flotation process developed by Minerals & Chemicals Philipp Corporation.

-in and on most paper products (from modern newsprint to National Geographic and packaging board) sometimes as much as 25% (by weight) of the product,40% of the tile (ceramic, rubber, and linoleum) you walk on, and15% of the tires you ride on.

The most common origins of kaolin were from the alteration of such source minerals as feldspar, granite, and gneiss during the warm, wet environments between the early Tertiary (50 million years) and Cretaceous (135 million years) Eras. Kaolin is found in primary (or insitu) and secondary (sedimentary) sites on all continents.

The viable air-float producer has a customer list consisting 200-300 locations, each purchasing one or more of its 6-20 products. Product differentiation is by the type of crude as it is found in the ground, blending of these different crudes, and degrees of cleanliness.

The air-floaters primary tools are slicers, dryers, and mills of the either the roller-type or the impact-type, and a lean, aggressive management style. Most office-holders cover two-or three jobs, R&D is a part-time function at best, and routine high-capital activity (such as stripping and hauling) is contracted.

The typical water-washed operation has a capacity of + 1.0 million mTpA and employs +600 persons. It has a heavy commitment to R&D and customer service, especially on applications development. Its customer list would extend to 1000 locations for its +50 basic products.

Anxious to exploit a tightening supply and rising prices, usually all four majors will increase capacity. As a general rule all expansions are completed within the same 6-8 months putting the industry, once again, back in over supply.

In the air-float segment, the chronic oversupply situation results from the relative ease of entry, with new players having added about 400,000 mTpA of new capacity in recent years, putting the air-floaters at almost 100% over-supply. Market and managerial skills have pushed most of the over-supply onto the new entrants, so they operate at less than 30% of their capacity. They in turn create tremendous pricing pressure which has the effect of shutting down the less provident air-floaters. In the last ten years, four producers have left the field, mostly those affiliated with water-washed producers.

By tacking on a calcination step at the end of the ultrafine product line, the price can be increased by ca. $200/mT for a cost of $70/mT plus $50/mT in depreciation. Calcination consists of finely deagglomerating the ultrafine product and roasting it at temperatures of between 1000C and 1100C. This is followed by another deagglomerating step to counter the formation of abrasive mullite or cristobolite generated locally in the process. In calcination of kaolin the water of hydration between the gibbsite and silica sheets is driven off, in effect generating two more air interfaces and thereby enhancing brightness a couple points and opacity.

Another current challenge to the kaolin industry has been the quality movement. Typically kaolin producers strived to attain threshold specifications i.e., specifications which required the brightest product or the lowest viscosity. This tended to produce consistency, mainly around a performance-ceiling. But today quality means reliability in meeting not only these requirements but also additional arbitrary specifications. They are arbitrary in the sense that they occur along the spectrum, not at the edges of the range. And the primary concern of the customer is a narrow consistency.

chapter 4 exploration, mining, and processing - sciencedirect

chapter 4 exploration, mining, and processing - sciencedirect

This chapter discusses the exploration, mining, and processing. Once a clay deposit has been discovered, a drilling program to determine the areal extent, thickness and type of overburden, and thickness and quality of the clay is initiated. Both core and auger drills are used in exploration and mine development. For most clay deposits, a grid pattern of drilling is used to determine the size and quality of the deposit. The distance between the drill holes in the grid pattern is based on several factors including topography, geology, and lateral extent and uniformity, and water table considerations. For example, the drilling and testing program is very different if the clay deposit is sedimentary or residual from a deposit that is hydrothermal or is structurally deformed by faults, folds, and inclined beds. Professional advice from a geologist or mining engineer is very helpful in designing a drilling and testing program.

henan mining machinery and equipment manufacturer - kaolin feeding equipment supplies

henan mining machinery and equipment manufacturer - kaolin feeding equipment supplies

Price Kaolinite Crushing Equipment And Kaolin Grinding Mill 27 Views. The Zenith is the professional mining equipments manufacturer in the world, located in China ...Primarie delle idee Proposte di Dibattito Clay Leading Mining Process Equipment. ... grinding mill machine, feeding ... Mining Equipment Supplies in Clay, ...

Ore beneficiation equipment, sand making equipment, crushing equipment and powder grinding equipment, which are widely used in various industries such as metallurgy, mine, chemistry, building material, coal, refractory and ceramics.

kaolin mining and processing

kaolin mining and processing

Kaolin is an important industrial mineral because it exhibits desirable properties in many applications and because of its relatively low cost. Approximately 2,000,000 tons of kaolin from Georgia and South Carolina are processed and used commercially in the United States each year. Strictly defined, the name kaolin is applied to a group of hydrous aluminum silicates of which the mineral kaolinite is the most common. Kaolinite has such desirable properties as natural whiteness, chemical stability, non-abrasiveness, and very fine particle size. Kaolinite particles are characteristically thin, flat, and hexagonal in outline. The particles range in size from submicron to as much as 40 microns (equivalent spherical diameter).

The kaolin is mined with diesel or electric shovels or draglines and loaded in trucks for transport to the processing plant or dropped directly from the dragline into a blunger. The blunger chews the kaolin into small lumps and mixes it with water and dispersing chemical to form a clay-water slip or slurry. This slurry is pumped from the blunger to settling boxes and screens to remove the coarse material which is called grit in the industry, but is usually designated as material coarser than about 44 microns. After the kaolin slurry is degritted it is collected in large storage tanks and pumped several miles to the processing plant.

The kaolin slurry is pumped from the mines to the plant into large terminal tanks in a dispersed state. The common dispersants used are the sodium polyphosphates and sodium silicate. The first step in the wet process is to fractionate the kaolin slurry into a coarse and fine fraction through continuous centrifuges or by settling in large hydroseparators or vats. The coarse fraction can be used as filler in paper, plastics, paint, and adhesives and for many of the same applications as the dry processed kaolin. The fine fractions are used in paper coatings, high gloss paints, inks, special ceramics, and rubber. The fine particle kaolins undergo the most rigorous and advanced treatment in the processing. After fractionation the kaolin is bleached, if necessary, to remove ferruginous coloring components. In the bleaching operation the kaolin slip is acidified with sulfuric acid to a pH of approximately 3.0 to solubilize the iron. Zinc or sodium hydrosulfite is added and the iron forms a soluble sulfate and is removed from the kaolin during the dewatering process.

kaolinite processing | equipment, process flow, cases - jxsc machine

kaolinite processing | equipment, process flow, cases - jxsc machine

Kaolinite is a non-metallic mineral, mainly composed of kaolinite, halloysite, hydromica, illite, montmorillonite and quartz, feldspar and other minerals, often mixed with pyrite, limonite, anatase, quartz, chalcedony, alum, etc. Kaolin is widely used in ceramics, paper, rubber, plastics and refractory industries due to its excellent processabilities such as plasticity, cohesiveness, sinterability and fire resistance. There are three main types of the genesis of kaolin deposits: weathering, sedimentary and hydrothermal alterations.

The processing of kaolin ore depends on the nature of the ore and the end-use of the product. There are two processes used in industrial production: the dry process and wet process. Usually, hard kaolin is produced by the dry process, and soft kaolin is produced by a wet process.

The kaolinite dry mining process is a simple and economical process. The ore is crushed to 25.4mm by a hammer crusher and fed into the cage mill to reduce the particle size to 6.35mm. The hot air in the cage mill reduces the moisture of the kaolin from about 20% to 10%. The crushed ore is further ground by a blown-type Raymond mill equipped with a centrifugal separator and a cyclone. This process removes most of the sand and the product is commonly used in low-cost fillers in the rubber, plastics and paper industries. When used in the paper industry, the product can be used as a filler in the filler layer with an ash content of less than 10% or 12%. At this time, the brightness of the product is not high.

When the dry beneficiation method requires high whiteness of the product, the product produced by Raymond mill must be dry iron removed. The dry process has the advantages of eliminating the dehydration and drying process, reducing the loss of ash powder, short process flow, low production cost, and is suitable for drought and water shortage areas. However, it is necessary to rely on the wet beneficiation process to obtain high-purity kaolin.

The wet process includes three stages of ore preparation, ore beneficiation processing and product processing. The beneficiation stage may include hydraulic grading, flotation, selective flocculation, magnetic separation, chemical treatment (bleaching), etc. to remove different impurities.

The prepared slurry pulp is first desanded by the rake type washing box, floating tank classifier or cyclone, and then divided into two grades of coarse and fine by the continuous centrifuge, hydraulic cyclone, hydraulic separator or vibrating fine sieve (325 mesh).

The fine-grained grade of the classifier is fed into HGMS (high-gradient magnetic separator) to remove iron-titanium impurities. The product is detached by stirring and scouring and then leached by iron oxide. The clay which is high enough in brightness and has good coating properties can be magnetically removed. Stripped and sent directly to the leaching operation. After leaching, alum is added to the slurry to coagulate the clay minerals to facilitate dehydration.

The bleached clay is dewatered using a high-speed centrifuge, a rotary vacuum filter or a filter press. Dewatering by filter or filter press. The filter cake is redispersed into a slurry of 55% to 65% solids and then spray dried to make a loose dry product. Part of the dry product was mixed into the dispersed slurry to make 70% solids and shipped to the paper mill.

The final product, which is not selected, has low brightness and can only be obtained by magnetic separation, froth flotation or selective flocculation in the process. However, these independent operations have their own advantages and disadvantages, so the industry usually uses a combined process of two or three of these processes for the comprehensive utilization of clay resources.

Related post: Whats High Gradient Magnetic Separator? The dyed impurities in kaolin (such as hematite, etc.) have weak magnetic properties and can be removed by a high gradient magnetic separator. In the United States, the PEM-84 wet high gradient magnetic separator can reduce Fe2O3 in kaolin ore from 0.9% to 0.6%, and Ti2O3 from 1.8% to 2.0% to 0.8%. This high-gradient magnetic separator uses stainless steel wool as a medium. When the field strength is 1.5 to 2.0T, it consumes 270-500kw.

China has carried out wet research on Hunan acid, Lingyang, Boluo and Hengling soils, and all of them have obtained good test results, especially the removal of iron and titanium in kaolin by vibration high gradient magnetic separation. Very good test indicators. From the comparative test results of Chinas CLY500 vibrating high gradient magnetic separator and the US PEM-84 high gradient magnetic separator, the high gradient magnetic of China is seen from the iron and titanium impurities and whiteness. The machine performance is better than the United States.

Since some iron impurities in some kaolin mines exist in the form of silicates, the magnetic properties are very weak, and titanium exists in the form of rutile, the magnetic separation method is difficult to work, so the process is usually accompanied by flotation, selective flocculation and other operations. To improve the quality of the product. In recent years, superconducting magnetic separators have been successfully applied to kaolin sorting, which not only reduces energy consumption, but also greatly increases the field strength, and the quality of kaolin concentrate is also higher. The Eriez superconducting magnetic separator features a rapid magnetic lift, achieving the highest design field strength (5T) in 60 seconds, while the degaussing time is short, which greatly reduces the time required to flush magnetic impurities from the magnet during the load cycle. Its energy consumption is low, about 80% less than conventional magnetic separator, and the processing capacity is large, up to 100t/h.

The United Kingdom has tested a reciprocating helical superconducting magnetic system that is similar in design to a conventional can magnetic filter, except that it retains the superconducting magnet in an excited state during the duty cycle without switching control. Continuous operation. The 3048mm superconducting high gradient magnetic separator designed by Humboldt of Germany has simple structure, low operation and maintenance cost and good stability.

The purpose of the flotation operation is to float titanium impurities from the kaolin. Since the impurity particles are extremely fine, a carrier flotation process is usually employed. The carrier mineral may be calcite or silica sand (-325 mesh), and the amount of the carrier mineral is generally 10% to 20% by weight of the kaolin, and a part of the carrier may be reused after being recycled.

The agents used in the flotation process include dispersant sodium silicate, pH adjuster amine hydroxide and caustic soda collector Tal oil, fatty acid and calcium petroleum sulfonate. However, flotation has many disadvantages. The hydrophobization of the carrier requires a large number of chemicals. The flotation process can only be effective at a lower concentration of the slurry, thereby increasing the cost of dewatering. The loaded body must be removed from the clay product as much as possible. Recycling in the product for recycling.

Chemicals and carrier minerals remaining in the clay are detrimental to the final product. Cundy and Yong et al. studied a flotation process that does not require a carrier and floats anatase directly from kaolin, which is characterized by the presence of dispersants (such as sodium silicate) and pH adjusters (usually amine hydroxide). Under high conditions, high pulp concentration (40% to 60% solids) is scrubbed to remove surface contaminants. At the same time, scrubbing also disintegrates anatase and hematite from kaolin minerals, and then traps a small number of activators and fatty acids. The slurry is added together with the slurry, and the anatase covered by the collector forms selective agglomeration under high shear stirring conditions, so that the particle size is significantly increased, and the slurry after high shear stirring and slurry is diluted to 15%~ Flotation is carried out with 20% solids, and alum in kaolin can also be removed by flotation.a You may interest in buying flotation machine, 7 Factors Affecting Froth Flotation

At pH 8~11, selective agglomeration of iron-titanium impurities was observed by adding alkaline earth metal ions such as Ca2+ and Mg2+ to the kaolin slurry, and then selective flocculation was carried out with a weak anionic polyelectrolyte. The process requires a slurry concentration of less than 20%, so a large amount of moisture must be removed in subsequent operations, and the residual flocculant also affects the quality of the final product.

Selective flocculation of kaolin with high-molecular flocculant, the kaolin particles flocculate to the bottom, and the iron-titanium impurities are reddish-brown in the suspension in the upper part due to the fine particles, and the upper suspension can be removed. Most of the iron-titanium impurities are removed and processed by other operations (such as magnetic separation) to obtain high-quality kaolin. Suzhou Kaolin Company has achieved good indicators using a new process of selective flocculation. The use of selective flocculation and high gradient magnetic separation to treat kaolin also obtained satisfactory indicators.

Leaching is carried out in the presence of a weakly acidic solution (pH 3 to 4) in the presence of a reducing agent (NaS2O4) to keep the dissolved iron in the Fe2+ state, avoiding the formation of Fe(OH)3, and washing it with water to separate it from the kaolin. In order to remove the dark organic matter, it can be bleached with a strong oxidizing agent (hydrogen peroxide, sodium hypochlorite, etc.), and the Suzhou Kaolin Company has obtained high-quality kaolin products by oxidative bleaching. It has been reported that the treatment of kaolin with microorganisms can significantly improve the quality of the product.

The selected clay is stored in a slurry tank for 6-8 hours, and the pH is adjusted to 3-4, which is close to the zero points of the clay, so that the clay particles are easily agglomerated. The addition of alum to the pulp helps the agglomeration of the clay particles and promotes dehydration. The cylinder filter is a commonly used dewatering device which increases the slurry concentration to 55% to 60%. One of the important functions of the filtration operation is to remove chemicals from the clay.

To enhance this work, the water spray is often used. Spray drying has become a very effective process in the clay industry, but it is expensive. In recent years, a new filtration process utilizing the electrophoretic properties of charged particles in an electric field has emerged. The kaolin particles are negatively charged at pH > 3 and are surrounded by an oppositely charged ion mist to form an electric double layer.

In the electric field, the clay particles move toward the anode, and the counterions in the ion mist move toward the cathode. When the particles reach the anode, they are used to protect the filter cake formed on the anode film of the electrode. The anode filter cake is further dehydrated by electroosmosis, and the excess water is pumped out through the negatively charged filter cake capillary by the electroosmotic principle.

The dehydrating agent is used to agglomerate the kaolin particles into large particles, which can accelerate the precipitation rate of the particles, facilitate the dehydration, and reduce the kaolin loss of the fine particles. Therefore, the development of new high-efficiency dehydrating agent for kaolin is also one of its research directions.

1 The raw ore mined from the mine is coarsely selected on-site, and a large number of tailings are discarded in the mine. This not only solves the filling of the goaf but also reduces the stockpiling and transportation of the ore in the ore dressing plant. Concentrates of each roughing plant;

3 high-concentration pulping, dispersing agent is added to the pulp during the sorting process, the flocculating agent is added during the dehydration process, and the filter press or vacuum filter product can be sold as a product without drying;

4 In addition to the hydrocyclone classification, the beneficiation operation also uses a centrifugal classifier, a sand mill, a high gradient magnetic separator, and a flotation machine to improve product fineness and reduce impurities such as iron, titanium and sulfur;

5 The chemical bleaching process is commonly used in major kaolin producing countries such as the United States, the United Kingdom, and the former Soviet Union to produce high-whiteness kaolin products, but the cost is high;

6 Kaolin products are sold in bulk, coarse powder, fine powder and paste form. The manufacturer supplies different products according to the requirements of the users. There are many types of drying equipment for the products, but most applications are spray drying, because the cost is relatively low;

7 Concentrators not only have large production capacity, but also many varieties, and are standardized products. It can meet the needs of different users. China Kaolin Company has four categories and 34 varieties. These products are widely used in paper fillers and coatings, ceramics industry raw materials, rubber and plastic fillers and reinforcing agents, white cement oil felts, roofing coatings and waterproofing agent ingredients, fiberglass ingredients, ink pigments, cosmetics and soaps. Fillers, carriers of pesticides and fertilizers, binders for abrasive materials, synthetic molecular sieves, petroleum catalysts, atomic energy reactors, etc.

1 The carrier flotation process makes it possible to select fine-grained kaolin. The advantage is that the kinetic energy of the particles is increased, but the consumption of the agent is high, and the use and processing cost of the carrier mineral is further increased.

2 The activation of polyvalent cations without a carrier can also cause anatase to float, but the consumption of fatty acid-matched collectors is higher than that of other industrial minerals, which may be due to the large surface area of the particles.

3 High-shear agitation plays a two-fold role in the flotation. One is to dissociate the anatase from the kaolinite, and the other is to induce shear flocculation between the anatase particles covered by the collector.

4 High-gradient magnetic separation technology has greatly changed the appearance of the kaolin industry. Especially the vibration high-gradient magnetic separation can effectively remove the iron-titanium impurities in kaolin, but has little effect on the particle size composition and physical and chemical properties of the product. Produce high-quality kaolin products. Dry high gradient magnetic separation treatment of hard kaolin can eliminate product dehydration and reduce product loss, which is suitable for dry and low water areas. The superconducting high gradient magnetic separator has low energy consumption and large processing capacity. The product purity is high and will be widely used in the kaolin industry.

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