Rutile titanium dioxide

Abstract: A process for the preparation of rutile titanium dioxide comprises heating hydrous titanium oxide which readily converts to rutile titanium dioxide until at least 99.5 per cent by weight is in the rutile crystal form. The test for ready conversion to rutile consists of heating the hydrous titanium oxide to 950°C at a rate of 1°C per minute. Suitable material is thereby converted to at least 99.0 per cent rutile by weight. The product has a very narrow particle size and crystal size distribution and is an excellent pigment.

Description: This invention relates to rutile titanium dioxide and a method for its preparation. In particular the method is suitable for producing rutile titanium dioxide having narrow particle size and crystal size distributions. It is well known that a principal factor affecting the opacity available from a rutile titanium dioxide pigment is the average crystal size of the pigment. For maximum optical efficiency it is also important that the distribution of crystal sizes is narrow and that the size distribution of particles (which comprise one or more crystals) is narrow. For titanium dioxide having optimised crystal size and crystal size distribution, the best efficiency is obtained when the pigment has a high single crystal fraction (i.e. the average particle size is close to the average crystal size). It is an object of this invention to make available a process which can generate rutile titanium dioxide having narrow particle size and crystal size distributions and a high single crystal fraction. As a general rule it is acknowledged that calcination of titanium oxide to a very high rutile content leads to sintering of individual crystals and hence a relatively wide particle size distribution and a relatively low single crystal fraction. Surprisingly, the process of the invention is capable of generating a novel product having narrow crystal and particle size distributions and a high single crystal fraction and, accordingly, a second aspect of the invention comprises rutile titanium dioxide having an average crystal size in the range 0.17 to 0.32 micrometre, a particle size distribution with a geometric weight standard deviation less than 1.25 and a ratio of average particle size to average crystal size of less than 1.25:1. The process of the invention differs from conventional processes in utilising a form of hydrous titanium oxide which rutilises relatively easily. It is common practice to adjust calcination conditions (e.g. by the addition of rutilisation inhibitors to the calcination feed) such that the hydrous titanium oxide is relatively slowly converted to rutile titanium dioxide since this is generally beneficial for calciner control. Hydrous titanium oxide suitable for use in the process of this invention can be prepared in a number of ways, for example by adding rutile promoters to the calciner feed, reducing the normal amount of rutile inhibitor added to the calciner feed or using a relatively large amount of rutile-promoting nuclei (either during precipitation of the hydrous titanium oxide or by addition to the calciner). Rutilisation promoters which can be present during calcination include lithium and zinc compounds and rutilisation inhibitors, whose presence should be controlled include aluminium, potassium and phosphorus compounds. The process of the invention comprises hydrolysing an aqueous solution of titanium sulphate in the presence of titanium dioxide nuclei in an amount of from 0.2 per cent to 4.0 per cent by weight calculated with respect to potential TiO 2 in the titanium sulphate solution to form hydrous titanium oxide and said hydrous titanium oxide is calcined by heating to a temperature in the range of 850°C to 930°C in the presence of a compound of sodium or a compound of lithium which is present in an amount between 0.05 per cent and 0.3 per cent by weight calculated as alkali metal oxide with respect to weight of hydrous titanium oxide calculated as TiO 2 and, optionally, in the presence of a compound of phosphorus which is present in an amount up to 0.25 per cent by weight calculated as P 2 O 5 with respect to weight of hydrous titanium oxide calculated as TiO 2 , no other calcination additive being deliberately added, said calcination being continued until titanium dioxide of which at least 99.5 per cent by weight is in the rutile crystal form is produced. A variation on this preferred process comprises the further addition of a compound of aluminium to the hydrous titanium oxide before calcination. However, it is important that the amount of aluminium compound added is strictly controlled and is related to the presence of niobium in the hydrous titanium oxide. Niobium compounds are frequently present in feedstocks used to prepare the titanium oxide and their presence generally causes discolouration of the finished rutile titanium dioxide. This discolouration is minimised by adding sufficient aluminium compound to ensure that at least approximately equimolar amounts of aluminium and niobium are present. Usually an amount slightly in excess of an equimolar quantity is added in order to ensure at least equimolar quantities when the niobium content varies due to production variations. Typically, the amount of aluminium compound added is about 55 per cent by weight calculated as Al 2 O 3 of the weight of niobium present calculated as Nb 2 O 5 . Some variation is possible but the amount of aluminium compound added should normally be between 52 and 62 per cent by weight (as Al 2 O 3 ) with respect to weight of niobium (as Nb 2 O 5 ). A variation on this further preferred process comprises the addition of a compound of aluminium to the hydrous titanium oxide before calcination. As hereinbefore described the aluminium is added with the intention of minimising the effect of niobium impurity in the titanium oxide. The amount of aluminium compound added is therefore between 52 and 62 per cent by weight (as Al 2 O 3) ) with respect to weight of niobium present (as Nb 2 O 5 ) as hereinbefore described. In the above mentioned preferred embodiments the hydrous titanium oxide is precipitated in the presence of titanium dioxide nuclei. Such nuclei and their method of production are well known in the titanium dioxide industry. Normally, nuclei will be rutile-promoting nuclei and such nuclei are typically prepared by rapidly adding an aqueous solution of titanium tetrachloride containing the equivalent of about 200 grams per litre TiO 2 to a solution of sodium hydroxide in water. The nuclei are present in an amount between 0.2 per cent and 4.0 per cent by weight calculated as TiO 2 based on weight of potential TiO 2 in the titanium sulphate solution. Preferably the amount of nuclei is from 1.0 per cent to 2.0 per cent by weight with respect to potential TiO 2 . The precipitated hydrous titanium oxide is separated from the residual titanium sulphate solution, typically by filtration, to produce what is normally described as 'pulp'. The pulp is generally washed to remove soluble iron salts and reduce sulphuric acid contamination, frequently by reslurrying with water and filtering again. In one preferred process one or more compounds of lithium or sodium are present during the calcination of the hydrous titanium oxide. Normally, it will be necessary to add these compounds before calcination commences. Generally, any lithium or sodium compounds such as chlorides, sulphates or hydroxides can be used but the preferred compounds are lithium and sodium carbonate. In the embodiment using lithium or sodium the amount of lithium or sodium compound present is from 0.05 per cent to 0.3 per cent by weight calculated as Li 2 O or Na 2 O with respect to hydrous titanium oxide calculated as TiO 2 . For lithium compounds, the preferred amount is from 0.05 per cent to 0.15 per cent Li 2 O by weight with respect to TiO 2 and, for sodium, the preferred amount is from 0.10 per cent to 0.20 per cent Na 2 O with respect to TiO 2 . In the preferred embodiments, a compound of phosphorus is optionally present during the calcination. Frequently, phosphorus compounds are present in the hydrous titanium oxide due to the presence of phosphorus impurities in the ore used. However, it is commonly necessary to adjust the amount of phosphorus present by the addition of a phosphorus compound. Suitable compounds include phosphoric acid or, preferably, an ammonium phosphate. When sodium or lithium is used as a calciner additive, the amount of phosphorus compound present, if used, is up to 0.25 per cent by weight calculated as P 2 O 5 with respect to hydrous titanium oxide calculated as TiO 2 by weight. Preferably a phosphorus compound is present in an amount equivalent to 0.05 per cent to 0.25 per cent P 2 O 5 with respect to TiO 2 . When used in conjunction with a lithium compound, the preferred amount of phosphorus compound is from 0.10 per cent to 0.20 per cent by weight calculated as P 2 O 5 with respect to TiO 2 and, when used with a sodium compound, the preferred amount is up to 0.15 per cent by weight calculated as P 2 O 5 with respect to TiO 2 . When a potassium compound is used as a calciner additive, the amount of phosphorus compound present, if used, is up to 0.15 per cent by weight calculated as P 2 O 5 with respect to hydrous titanium oxide calculated as TiO 2 . Preferably the amount of phosphorus present is in the range 0.05 to 0.15 per cent by weight calculated as P 2 O 5 with respect to titanium oxide calculated as TiO 2 . As mentioned hereinbefore a portion of an aluminium compound is added in carrying out a variation of either of the preferred processes of the invention. It is important that the amount of aluminium compound added is closely related to the amount of niobium present in the 'pulp' as hereinbefore described and the actual amount used will be determined by analysing the 'pulp' or the feedstock ore for niobium. Usually not more than 0.15 per cent by weight aluminium compound calculated as Al 2 O 3 with respect to titanium oxide calculated as TiO 2 will be present. The aluminium compound used may be one of several aluminium compounds including aluminium chloride, hydroxide or nitrate but preferably aluminium sulphate is used. In the process of the invention the hydrous titanium oxide is calcined by any conventional techniques known in the art. The essential feature of the calcination is that conditions are established which ensure that the titanium dioxide produced contains at least 99.5 per cent in the rutile crystal form. Preferably, conditions are established so that at least 99.8 per cent of the titanium dioxide produced is in the rutile crystal form. A useful product is obtained by calcining the titanium oxide to the point where it contains 99.9 per cent by weight rutile titanium dioxide and subsequently raising the temperature of the titanium oxide by a further 30 to 70 degrees centigrade. This product has a narrow particle size distribution as hereinbefore discussed and also has the useful property of having crystals which are more spherical and less angular than titanium dioxide prepared by conventional processes. In the preferred embodiments of the invention described hereinbefore, the required conversion to rutile can be typically achieved by heating the hydrous titanium oxide to a temperature in the range 860°C to 930°C. The product of the invention has been found to possess narrow crystal size and particle size distributions. Normally, however, the material discharged from the calciner will require milling in order to optimise the particle size distribution and to reduce particle size and increase the single crystal fraction of the titanium dioxide powder. Any suitable milling process can be used and several are known to persons skilled in this art. Preferably, however, a sand mill is used in which a dispersion of the titanium dioxide in water is prepared and said dispersion is mixed with sand particles in a milling zone where it is agitated by, for example, a series of discs mounted upon a rotating shaft. The sand particles act as a grinding medium and reduce the average particle size of the titanium dioxide. In order to produce the novel product which is one aspect of this invention milling conditions are established which generate a product in which the ratio of average particle size to average crystal size is less than 1.25:1. Preferably, the conditions which are established ensure that this ratio is less than 1.1:1. Typically, the average particle size is measured by X-ray sedimentation (e.g. by a Brookhaven BIXDC Particle Size Analyser) and the average crystal size is determined by transmission electron microscopy on a rubbed out sample with image analysis of the resulting photograph (e.g. using a Quantimet 570 Image Analyser). Normally, the milled titanium dioxide has an average particle size, as determined by X-ray sedimentation, of less than 0.40 micrometre. Preferably the average size is less than 0.35 micrometre and, more preferably, less than 0.30 micrometre. Usually, the average crystal size of the product of the process of the invention is in the range 0.17 micrometre to 0.32 micrometre and, preferably, products have an average crystal size in the range 0.22 micrometre to 0.30 micrometre. Frequently, the average crystal size is adjusted to suit the intended use of the titanium dioxide. For example, when the titanium dioxide is used in inks, it preferably has an average crystal size in the range 0.23 micrometre to 0.30 micrometre and, when used in paints, the preferred product has an average crystal size in the range 0.22 micrometre to 0.26 micrometre. The titanium dioxide pigment particles are normally subsequently treated with the surface treatments common in this industry. For example, the particles are normally coated with an inorganic hydrous oxide or a phosphate. Typical oxides are oxides of silicon, titanium, zirconium and aluminium. Frequently, the surface of the particles is also treated with an organic compound such as a polyol or an alkanolamine. Typical organic compounds used are trimethylolpropane, pentaerythritol, triethanolamine and trimethylolethane. Conveniently, the dispersion which is a product from a sand mill is used for treatment with one or more inorganic compounds after which the pigment is separated, dried and, if necessary, micronised. As already stated hereinbefore, the invention is capable of generating a novel titanium dioxide in which the geometric weight standard deviation of the particle size as determined using a Brookhaven BIXDC Particle Size Analyser is less than 1.25. In preferred products of the invention the geometric weight standard deviation of particle size is less than 1.22. Normally, the geometric weight standard deviation of crystal size of the novel titanium dioxide is less than 1.28. The ratio of average particle size to average crystal size in this product of the invention is less than 1.25:1 and, preferably, is less than 1.1:1 Despite the fact that in the process of the invention the titanium dioxide is calcined to a higher rutile content than is conventionally thought to be desirable, no adverse optical effects are observed. In addition products made using the process of the preferred embodiments have been shown to have an exceptionally low abrasivity. The invention is illustrated by the following examples. EXAMPLE 1 A titanium sulphate solution was prepared by digesting a slag feedstock with sulphuric acid, dissolving the resultant digestion cake with dilute sulphuric acid and clarifying the solution produced. The titanium sulphate solution had an acid/titanium ratio of 1.81, an iron/titanium ratio of 0.12 and a concentration equivalent to 240 grams TiO 2 per litre. The solution was heated to 85°C and titanium dioxide nuclei equivalent to 1.9% by weight TiO 2 with respect to weight of potential TiO 2 in the solution were added over 5 minutes. The temperature of the solution was held at 85°C for 2 hours after which it was raised to boiling point and held for 1 hour. Then the solution was diluted to 170 grams TiO 2 per litre and held at the boil for a further 15 minutes to form a slurry of hydrous titania. This slurry was washed and leached and then mixed with monoammonium phosphate to produce the equivalent of 0.10% P 2 O 5 with respect to TiO 2 in the slurry and with sodium carbonate equivalent to 0.19% Na 2 O with respect to TiO 2 . The resultant slurry was dried overnight at 110°C and passed through a 2 mm sieve. The powder produced was heated in a rotary calciner at a rate of 1°C per minute until the product was found to contain 99.9% rutile. This conversion was achieved at a temperature of 915°C. The product was found to have an average crystal size of 0.26 micrometre and the geometric weight standard deviation of crystal size was 1.27 (by Quantimet 570 Image Analyser). The product was milled in a sand mill until the average particle size was 0.274 micrometre as determined by optical density. It was then coated with 2.6% alumina by conventional techniques involving precipitation from aluminium sulphate and sodium aluminate. After drying and grinding, the coated pigment was passed through a microniser twice during which it was treated with 0.60% trimethylolpropane prior to the first pass. The final product had an average particle size (Brookhaven BIXDC) of 0.263 micrometre and an exceptionally narrow geometric weight particle size standard deviation of 1.20. When incorporated in conventional manner into nitrocellulose inks the gloss of the inks was outstanding and the opacity was not compromised. EXAMPLE 2 A titanium sulphate solution was prepared in a similar manner to that used in Example 1 except that the feedstock was ilmenite. The solution had an acid/titanium ratio of 1.80, an iron/titanium ratio of 0.50 and a concentration equivalent to 202 grams TiO 2 per litre. A slurry of hydrous titania was produced by hydrolysis in a manner similar to that used in Example 1 except that the amount of titanium dioxide nuclei used was equivalent to 1.6% by weight TiO 2 with respect to weight of potential TiO 2 in the titanium sulphate solution. The slurry was washed and leached and mixed with monoammonium phosphate to produce the equivalent of 0,10% P 2 O 5 with respect to TiO 2 in the slurry and sodium carbonate equivalent to 0.22% Na 2 O with respect to TiO 2 . This treated slurry was heated in a rotary calciner at a ramp rate of 1°C per minute to a temperature of 950°C at which point the product was found to contain 99.9% rutile. The product was found to have an average crystal size of 0.26 micrometre and the geometric weight standard deviation of crystal size was 1.26 (by Quantimet 570 Image Analyser). The product was coarsely dry milled and subsequently sand milled to an average particle size of 0.28 micrometre with a geometric particle size standard deviation of 1.45 (as measured by Optical Density Particle Size Analyser). It was then coated with 2.5 per cent by weight alumina by conventional techniques, dried and passed twice through a microniser. The final product had an average particle size of 0.27 micrometre (Brookhaven BX1 particle size analyser). The particle size geometric standard deviation was 1.24. When incorporated in conventional manner into nitrocellulose inks the inks had a high gloss with excellent opacity. EXAMPLE 3 A titanium sulphate solution was prepared in a similar manner to that used in Example 1. The solution had an acid/titanium ratio of 1.81, an iron/titanium ratio of 0.12 and a concentration equivalent to 240 grams TiO 2 per litre. A slurry of hydrous titania was produced by hydrolysis in a manner similar to that used in Example 1 except that the amount of titanium dioxide nuclei used was equivalent to 1.8% by weight TiO 2 with respect to weight of potential TiO 2 in the titanium sulphate solution. The slurry was washed and leached and mixed with monoammonium phosphate to produce the equivalent of 0.12% P 2 O 5 with respect to TiO 2 in the slurry and sodium carbonate equivalent to 0.20% Na 2 O with respect to TiO 2 A sample of this treated slurry was heated in a rotary calciner at a ramp rate of 1°C per minute to a temperature of 950°C at which point the product was found to contain 99.9% rutile. The bulk of the slurry was heated in a rotary calciner at a ramp rate of 3°C per minute until the titanium dioxide was converted to 99.9% rutile. The product was found to have an average crystal size of 0.24 micrometre and the geometric weight standard deviation of crystal size was 1.27 (by Quantimet 570 Image Analyser). The product was coarsely dry milled and subsequently sand milled to an average particle size of 0.30 micrometre with a geometric particle size standard deviation of 1.43 (as measured by Optical Density Particle Size Analyser). It was then coated with 2.5 per cent by weight alumina by conventional techniques, dried and passed twice through a microniser. The final product had an average particle size of 0.30 micrometre (Brookhaven BX1 particle size analyser). The particle size geometric standard deviation was 1.24. When incorporated in conventional manner into nitrocellulose inks the inks had a high gloss with excellent opacity. EXAMPLE 4 (lying outside the claimed invention) A titanium sulphate solution was prepared in a similar manner to that used in Example 2. The solution had an acid/titanium ratio of 1.88 an iron/titanium ratio of 0.80 and a concentration equivalent to 170 grams TiO 2 per litre. A slurry of hydrous titania was produced by hydrolysis in a manner similar to that used in Example 1 except that the amount of titanium dioxide nuclei used was equivalent to 1.0% by weight TiO 2 with respect to weight of potential TiO 2 in the titanium sulphate solution. The slurry was washed and leached and mixed with monoammonium phosphate to produce the equivalent of 0.10% P 2 O 5 with respect to TiO 2 in the slurry, potassium carbonate equivalent to 0.22% K 2 O with respect to TiO 2 and aluminium sulphate equivalent to 0.15% Al 2 O 3 by weight with respect to TiO 2 . (The niobium content of the slurry was 0.27% Nb 2 O 5 by weight with respect to TiO 2 ). A sample of this treated slurry was heated in a rotary calciner at a ramp rate of 1°C per minute to a temperature of 950°C at which point the product was found to contain 99.4% rutile. The bulk of the slurry was heated in a rotary calciner at a ramp rate of 3°C until the product contain 99. 5% rutile. The product was found to have an average crystal size of 0.26 micrometre and the geometric weight standard deviation of crystal size was 1.25 (by Quantimet 570 Image Analyser). The product was coarsely dry milled and subsequently sand milled to an average particle size of 0.34 micrometre with a geometric particle size standard deviation of 1.43 (as measured by Optical Density Particle Size Analyser). It was then coated with 0.1% by weight phosphate (as P 2 O 5 ), 0.4% by weight titania, 0.5% by weight zirconia, 0.6% by weight silica and 3.3% by weight alumina by conventional technique, dried and passed twice through a microniser. The final product had an average particle size of 0.31 micrometre (Brookhaven BX1 particle size analyser). The particle size geometric standard deviation was 1.22. When incorporated in conventional manner into nitrocellulose alkyd paints the inks had a good gloss with high opacity. EXAMPLE 5 A titanium sulphate solution was prepared in a similar manner to that used in Example 1. The solution had an acid/titanium ratio of 1.81, an iron/titanium ratio of 0.12 and a concentration equivalent to 240 grams TiO 2 per litre. A slurry of hydrous titania was produced by hydrolysis in a manner similar to that used in Example 1 except that the amount of titanium dioxide nuclei used was equivalent to 3.5% by weight TiO 2 with respect to weight of potential TiO 2 in the titanium sulphate solution. The slurry was washed and leached and mixed with monoammonium phosphate to produce the equivalent of 0.10% P 2 O 5 with respect to TiO 2 in the slurry and sodium carbonate equivalent to 0.20% Na 2 O with respect to TiO 2 . This treated slurry was heated in a rotary calciner at a ramp rate of 1°C per minute to a temperature of 860°C at which point the product was found to contain 99.9% rutile. Heating was then continued until the temperature reached 900°C at which point calcination was stopped. The product was found to have an average crystal size of 0.19 micrometre and the geometric weight standard deviation of crystal size was 1.25 (by Quantimet 570 Image Analyser). The mean aspect ratio of the product was 1.49. The product was coarsely dry milled and subsequently sand milled to an average particle size of 0.22 micrometre with a geometric particle size standard deviation of 1.39 (as measured by Optical Density Particle Size Analyser). It was then coated with 0.5 per cent by weight alumina by conventional technique, dried and passed through a microniser. The product was found to have a high bulk density relative to conventional products, a property believed to be associated with the sphericity of the particles. EXAMPLE A (comparative) This Example demonstrates that calcination to at least 99. 5% rutile is important to achieve the desired pigmentary properties. A titanium sulphate solution was prepared in a similar manner to that used in Example 1. The solution had an acid/titanium ratio of 1.81, an iron/titanium ratio of 0.12 and a concentration equivalent to 240 grams TiO 2 per litre. A slurry of hydrous titania was produced by hydrolysis in a manner similar to that used in Example 1 except that the amount of titanium dioxide nuclei used was equivalent to 1.8% by weight TiO 2 with respect to weight of potential TiO 2 in the titanium sulphate solution. The slurry was washed and leached and mixed with monoammonium phosphate to produce the equivalent of 0.11% P 2 O 5 with respect to TiO 2 in the slurry and sodium carbonate equivalent to 0.18% Na 2 O with respect to TiO 2 . This treated slurry was heated in a rotary calciner at a ramp rate of 1°C per minute to a temperature of 950°C at which point the product was found to contain 99.9% rutile. The bulk of the slurry was calcined in a rotary calciner at a ramp rate of 3°C and heating was discontinued when the product contained 98.5% rutile. The product was found to have an average crystal size of 0.21 micrometre and the geometric weight standard deviation of crystal size was 1.32 (by Quantimet 570 Image Analyser). The product was coarsely dry milled and subsequently sand milled to an average particle size of 0.29 micrometre with a geometric particle size standard deviation of 1.47 (as measured by Optical Density Particle Size Analyser). It was then coated with 2.5 per cent by weight alumina by conventional technique, dried and passed twice through a microniser. The final product had an average particle size of 0.29 micrometre (Brookhaven BX1 particle size analyser). The particle size geometric standard deviation was 1.29. When incorporated in conventional manner into nitrocellulose inks the inks had a normal gloss and opacity compared to conventional pigments.

Claims: A process for the preparation of rutile titanium dioxide comprising hydrolysing an aqueous solution of titanium sulphate in the presence of titanium dioxide nuclei to form hydrous titanium oxide and subjecting said hydrous titanium oxide to calcination characterised in that an amount of from 0.2 per cent to 4.0 per cent by weight titanium dioxide nuclei calculated with respect to potential TiO 2 in the titanium sulphate solution is present during hydrolysis and said hydrous titanium oxide is calcined by heating to a temperature in the range 850°C to 930°C in the presence of a compound of sodium or a compound of lithium which is present in an amount between 0.05 per cent and 0.3 per cent by weight calculated as alkali metal oxide with respect to weight of hydrous titanium oxide calculated as TiO 2 and, optionally, in the presence of a compound of phosphorus which is present in an amount up to 0.25 per cent by weight calculated as P 2 O 5 with respect to weight of hydrous titanium oxide calculated as TiO 2 , no other calcination additive being deliberately added, said calcination being continued until titanium dioxide of which at least 99.5 per cent by weight is in the rutile crystal form is produced. A process according to claim 1 characterised in that a compound of lithium is present during calcination in an amount in the range 0.05 per cent to 0.15 per cent by weight calculated as Li 2 O with respect to weight of hydrous titanium oxide calculated as TiO 2 . A process according to claim 3 characterised in that a compound of sodium is present during calcination in an amount in the range 0.10 per cent to 0.20 per cent by weight calculated as Na 2 O with respect to weight of hydrous titanium oxide calculated as TiO 2 . A process according to claim 1 or 2 characterised in that a compound of lithium and a compound of phosphorus are present during calcination, the phosphorus compound being present in an amount in the range 0.10 per cent to 0.20 per cent by weight calculated as P 2 O 5 with respect to hydrous titanium oxide calculated as TiO 2 . A process according to claim 1 or 3 characterised in that a compound of sodium is present during calcination, and, optionally, a compound of phosphorus is present in an amount up to 0.15 per cent by weight calculated as P 2 O 5 with respect to weight of hydrous titanium oxide calculated as TiO 2 . A process according to any one of claims 1 to 5 characterised in that a compound of aluminium is also present during calcination, in an amount which is at least approximately equimolar to the amount of any niobium present in the hydrous titanium oxide. A process according to claim 6 characterised in that the compound of aluminium is present in an amount between 52 and 62 per cent by weight calculated as Al 2 O 3 with respect to weight of niobium present calculated as Nb 2 O 5 . A process according to claim 6 or 7 characterised in that the compound of aluminium is present in an amount up to 0.15 per cent by weight calculated as Al 2 O 3 with respect to hydrous titanium oxide calculated as TiO 2 . A process according to any one of the preceding claims characterised in that the calcination is continued until a titanium dioxide is produced in which at least 99.9 per cent by weight is in the rutile crystal form and the temperature of the titanium dioxide is subsequently raised by a further 30 to 70 degrees Centigrade. A process according to any one of the preceding claims characterised in that the material discharged from the calciner is subjected to a milling process until the ratio of average particle size to average crystal size is less than 1.25:1. A process according to any one of the preceding claims characterised in that the material discharged from the calciner is subjected to a milling process in which the average particle size as measured by X-ray sedimentation is reduced to less than 0.40 micrometre. A process according to any one of the preceding claims characterised in that the titanium dioxide is coated after calcination with an inorganic hydrous oxide, a phosphate or an organic compound. Rutile titanium dioxide having an average crystal size in the range 0.17 to 0.32 micrometre characterised in that said rutile titanium dioxide has a particle size distribution with a geometric weight standard deviation less than 1.25 and a ratio of average particle size to average crystal size less than 1.25:1. Rutile titanium dioxide according to claim 13 characterised in that the rutile titanium dioxide has a geometric weight standard deviation of crystal size less than 1.28. Rutile titanium dioxide according to claim 13 or 14 characterised in that the rutile titanium dioxide has a ratio of average particle size to average crystal size less than 1.1:1.

Inventors: ROBB JOHN, WATSON GARY WILLIAM, ROBB, JOHN, WATSON, GARY WILLIAM
Applicants: TIOXIDE GROUP SERVICES LTD, TIOXIDE GROUP SERVICES LIMITED
Application year: 1996
Main classification: C01G23
IPC codes: C01G23, C09C1