AU2005100939A4

AU2005100939A4 - F - treatment of titanium materials

Info

Publication number: AU2005100939A4
Application number: AU2005100939A
Authority: AU
Inventors: Alan Robert Mcgregor; Alexander Rodionov
Original assignee: INNOVATIVE WATER SOLUTIONS
Current assignee: INNOVATIVE WATER SOLUTIONS
Priority date: 2005-10-25
Filing date: 2005-11-09
Publication date: 2006-02-02
Anticipated expiration: 2013-11-09
Also published as: AU2005230943A1; AU2005100939A9

Description

-1o F-Treatment of Titanium Materials (Ni 0 Z Field of Invention The invention relates to a continuous process for the fluorine treatment of titanium bearing materials such as ilmenite, titano-magnetite, etc, to produce a high purity end product such as super fine grade titanium dioxide, silicon dioxide and also as an integral part of the recovery C€3 of precious and/or valuable metals/minerals.

Background of Invention C- 10 The extraction of metallic materials from sand, ore or the like can be an expensive and labour intensive task. However as the value and demand for these metallic materials increases the extraction of these metallic materials becomes more viable.

Of these metallic materials, titanium based materials is widely sought after. More than of TiO 2 produced worldwide is used as a paint pigment. Also it is widely used as an ingredient of the heat-resistant glass, ceramics, in metallurgy and electronics, cosmetics, as well as in manufacturing of toners for photocopying. Ilmenite is the main raw material for the production of titanium dioxide.

The unique properties of Ti and its derivatives are well known. A major limitation that withholds the widespread application of these materials is its high cost.

The bulk amount of TiO 2 is produced via digestion of ilmenite with sulphuric acid. This method, however, has serious drawbacks such as high cost, hazards related to handling concentrated sulphuric acid, environmental aspects associated with chemical waste recovery and disposal, complexity due to multi-stage operation and also limitations related to the quality of raw materials.

Fluorine-based methods are more efficient in processing ilmenite. There are two publications having close relation to this invention, namely Russian patents RU 2058408 and RU 2136771).

F:\share\7000-7099\702600AUC\702600AUC 20051108 Soeci.doc -2- O Both methods utilise the flourination of the titanium-bearing material with ammonia N, bifluoride NH 4

HF

2 producing fluoammonium salts (complex salts) of titanium, silicon and 0 iron. The obtained complex salts are then heat-treated in air, causing sublimation of the volatile fluorides of titanium and silicon, the latter being separated either using the difference S 5 in partial pressure values at the temperature of volatilization, or by means of pyrolytic hydrolysis of ammonium fluotitanate.

SThese disclosed methods have the following drawbacks: S 10 as a result of simultaneous sublimation of titanium and silicon (in the form of their complex salts), the latter contaminates the end product or otherwise introduces additional stages to the process, thus making it less cost efficient; sublimation of the complex salts in the presence of oxygen (air) leads to incomplete volatilization of titanium and also contaminates the sublimate with titanium oxofluorides, the latter causing deterioration of the quality of an end product or necessity of additional treatment; sublimation of the complex salts causes partial losses of iron to the sublimate due to gas-transport reaction within the system, what consequently ends up with contamination of an end product with iron oxides.

Object of the Invention It is an object of the invention to provide a continuous process for the fluorine treatment of metallic bearing materials, including titanium-bearing materials, that ameliorates some of the disadvantages and limitations of the known art or at least provide the public with a useful choice.

Summary of Invention.

In a first aspect the invention resides in a process for the treatment of titanium materials, wherein the process includes: a) reacting the material with ammonium bifluoride at 50-190 0 C to form a fluorinated mass. and b) heating the fluorinated mass in two stages: F:\share\7000-7099\702600AUC\702600AUC 20051108 SDeci.doc 0 i) the first stage involves heating the fluorinated mass to 220-300 0 C to form a reaction mixture and volatilised ammonium fluosilicate and 0 then extracting the volatilised ammonium fluosilicate and chemically separate silicon dioxide from the volatilised ammonium fluosilicate, ii) the second stage involves further heating the reaction mixture to 300- 600 0 C to sublimate the titanium compounds and further hydrolyse ¢C them to produce titanium dioxide.

Preferably, ammonium bifluoride is added to the titanium material at the molar ratio S 10 1.

Preferably, the molar ratio is 1.

Preferably, the reacting the material with ammonium bifluoride at a temperature between 160-180 C.

Preferably, the reacting the material with ammonium bifluoride is complete within 0.5-6 hours.

Preferably, the reacting the material with ammonium bifluoride is complete within 0.5-10 hours.

Preferably, the first stage heating is kept within a temperature range of 225-245 °C in order to achieve sublimation of ammonium fluosilicate from the fluorinated mass.

Preferably, the extracted volatilised ammonium fluosilicate is fed to a condenser to solidify before being chemically separated in a separator.

Preferably, the solid ammonium fluosilicate is treated with an ammonium solution to form silicon dioxide precipitate.

Preferably, the silicon dioxide precipitate obtained has a purity of at least 99.99%.

F:\share\7000-7099\702600AUC\702600AUC 20051108 SDeci.doc -4- Preferably, the reaction mixture is heated to a temperature between 540-580 °C.

Preferably, an inert gas is supplied during the second stage to ensure the oxygen-free condition of the reaction mixture.

Preferably, hydrogen gas is fed during the second stage to ensure reduction of the metallic fluorides to their metallic form.

Preferably, the formed metal is separated and extracted from the titanium compounds.

Preferably, the formed metal is iron.

Preferably, a non fluorinated and non volatile residue formed as a result the sublimation of the reaction mixture to the titanium compounds is separated and extracted from the titanium compounds.

Preferably, non fluorinated and non volatile residue is further refined to extract thereform any precious metals or any other suitable metals.

Preferably, the second stage is complete within 2-5 hours.

Preferably, the titanium compound is volatilised ammonium fluotitanate.

Preferably, the volatilised ammonium fluotitanate is fed to a condenser-hydrolyser where it undergoes pyrolytic hydrolysis to produce titanium dioxide.

Preferably, the titanium dioxide is produced in a crystalline form.

Preferably, the crystalline titanium dioxide obtained has a purity of at least 99.98%.

Preferably, the titanium material is a titanium bearing ore or sand.

Preferably, the titanium bearing ore or sand is ilmenite or tiano-magnetite.

F:\share\7000-7099\702600AUC\702600AUC 20051108 Sneci.doc o Preferably, the hydrolysis of the titanium compounds occurs in two steps, these steps being: i) passing the titanium compounds into a condenser in order to condense the titanium O compounds, and ii) hydrolysing the titanium compound condensate to produce titanium dioxide.

Preferably, the hydrolysing of the titanium compound condensate involves adding an Cc ammonia solution.

SIn a second aspect the invention resides in a method of processing the minerals in any form 0 10 (liquid, gaseous or solid) aimed at simultaneous extraction of other valuable products (Au, Pt, Pd, Agetc), consists of the following stages: i) preparation of the raw material (crushing, grinding, sizing, etc of the ore); ii) adding fluorine source to the raw material (Hydrofluoric Acid, Ammonia Bifluoride, etc.); iii) fluorination at elevated temperature (preferably below 200'C), producing as a result complex salts ammonia fluosilicate) and non-fluorinated materials; iv) sublimation of the volatile complex salt at the temperatures above 200°C followed by condensation and hydrolysis of sublimate to produce high purity oxides of Si and Ti; v) reduction of ferrous fluoride to form iron metal; vi) separation of iron metal from residue using magnetic or any other type separator, the residue containing precious metals, non-volatile metallic fluorides and other non-fluorinated matter; vii) second fluorination with ammonium bifluoride to convert metal fluorides into ammonium fluometallates; viii) hydration followed by separation of soluble ammonium fluometallates from residue using any existing method (precipitation, filtration, etc.); ix) extraction of precious metals from residue by means of acid leaching, electrowinning, flotation, etc; x) smelting precious metals followed by their refinery.

F:\share\7000-7099\702600AUC\702600AUC 20051108 Soeci.doc 0 In a third aspect the invention resides in an apparatus for the treatment of titanium materials c wherein the apparatus includes: 0 a) a fluorination reactor in which the material is mixed with and reacts with ammonium bifluoride, wherein the flourination reactor is adapted to be heated to a temperature between 50-190 0 C to initially form a fluorinated mass and then adapted to cause the fluorinated mass to be heated to a temperature Cc between 220-300 0 C to form a reaction mixture and volatilised ammonium Sfluosilicate; b) a condenser connected to the fluorination reactor, wherein the condenser is 0 10 adapted to extract the volatilised ammonium fluosilicate from the fluorination C1 reactor and condense the volatilised ammonium fluosilicate to a solid form; c) a first separator connected to the condenser, wherein the separator is adapted to extract the solid form of ammonium fluosilicate and separate thereform silicon dioxide; d) a reactor sublimator connected to the fluorination reactor, wherein the reactor sublimator is adapted to extract the reaction mixture from the fluorination reactor and heat the reaction mixture to a temperature between 300-600 0 C to reduce iron to form iron metal and sublimate reaction mixture to form titanium compounds and residue; and e) a condenser-hydrolser adapted to receive the titanium compounds from the reactor sublimator and adapted to hydrolyse the titanium compounds to produce titanium oxide.

Preferably, the apparatus has a second separator connected to the reactor sublimator, wherein the second separator is adapted to extract from the reactor sublimator the residue and separate therefrom pure metal.

In a fourth aspect of the invention resides in a process for the treatment of titanium materials, wherein the process includes: a) reacting the material with ammonium bifluoride at 50-190 C to form a fluorinated mass. and b) heating the fluorinated mass to 220-300 0 C to form a reaction mixture and volatilised ammonium fluosilicate and then extracting the volatilised F:\share\7000-7099\702600AUC\702600AUC 20051108 Soeci.doc -7ammonium fluosilicate and chemically separate silicon dioxide from the volatilised ammonium fluosilicate in order to obtain a silica precipitate.

O

In other aspects herein described Brief Description r The invention will now be described, by way of example only, by reference to the accompanying drawings: Figure 1 is a process flow diagram in accordance with a preferred embodiment of the invention.

Figure 2 is a process flow diagram in accordance with a further preferred embodiment of the invention Description of Drawings The following description will describe the invention in relation to preferred embodiments of the invention. The invention is in no way limited to these preferred embodiments as they are purely to exemplify the invention only and that possible variations and modifications would be readily apparent without departing from the scope of the invention.

Ground titanium-bearing ore or sand (ilmenite, titano-magnetite, etc.) is mixed with crystalline, molten or dissolved ammonim bifluoride at the molar ratio 1: respectively. The generalized equation of fluorination for ilmenite can be presented as follows: FeTiO 3 6.5 NH4HF 2 0.25 02 (NH 4 3 FeF 6

(NH

4 3 TiF 7 3.5 H 2 0 0.5 NH 3 The chosen molar ratio of components, however, ensures lesser saturation of the complex fluoammonium salts with ammonium fluoride, as compared with shown stoichiometry. This facilitates the completion of the reaction within 0.5 10 hours. Any ratios below 2.5 moles of ammonium bifluoride per 1 mole of the titanium-bearing material would result in incomplete volatilisation of ammonium fluotitanates at the sublimation stage.

F:\share\7000-7099\702600AUC\702600AUC 20051108 SDeci.doc c Fluorination of silicon dioxide, which is typically present in ilmenite, leads to formation of 0 its fluoammonium salt according to the following reaction: SiO 2 3 NH 4

HF

2

(NH

4 2 SiF 6 2 H 2 0 NH 3 C Ammonia and steam evolved from the reaction zone are used for the hydrolysis of Sammonium fluosilicate and also to absorb the acidic fluoride vapours for ammonium bifluoride recovery and reuse in the process. Additional heat produced in the course of this S 10 reaction, might lower the temperature of the beginning of fluorination.

Obviously, a major and current problem in separation of titanium, silicon, iron and other metals derived from a natural source, is cross-contamination which can effect the obtaining of high-purity end products. This problem could be resolved possibly at the very beginning of the process, which would greatly simplify the process and make the technology costefficient. Therefore, the present invention deploys separation of the said elements before sublimation, using differences in their physico-chemical properties.

Ammonium fluosilicate can be easily volatilised within a temperature range between 220 and 300 0 C. Under these conditions ammonium fluotitanate has negligibly low partial pressure, thus ensuring easy separation of silicon from the other two elements present in the titanium bearing ore. The volatilised ammonium fluosilicate is then condensed at lower temperatures, followed by hydrolysis and subsequent precipitation of silicon dioxide as follows:

(NH

4 2 SiF 6 2 H 2 0 NH 3 SiO 2 2 NH 3 6 HF A high quality of hydrated silica (99.99% purity) is obtained.

The remaining fluorinated mass consisting of the complex fluoammonium salts of titanium, iron and other trace metals, undergo pyrolytic decomposition while temperature rises from 300 to 600 according the following scheme:

(NH

4 3 TiF 7

(NH

4 2 TiF 6

NH

4 TiF 5 TiF 4 F:\share\7000-7099\702600AUC\702600AUC 20051108 SDeci.doc This causes the release of fluoride and ammonia that are then further reused in the process.

O

Presence of any significant amount of oxygen (air) in the reactor results in the formation of S 5 ammonium oxofluotitanate:

S(NH

4 2 TiF 6

H

2 0 (NH 4 )0.5TiOF 2 .5 1.5 NH 3 3.5 HF The pyrolytic decomposition of this compound yields in formation of oxofluotitanates S 10 TiOnFm (yellow colour) that may affect the quality of the target titanium dioxide and/or considerably complicate the scheme due to necessity of inclusion additional treatment/purification stages. Therefore, it is critical to carry out the high-temperature sublimation in airtight conditions and/or in the atmosphere of an inert gas.

Although the volatility of ferrous fluoride is negligible at below 600 0 C, there is a potential of contamination of sublimate with iron and/or other trace metals due to its loss to gaseous phase during the high rate gas-transport reaction of sublimation. However this can be overcome by the addition of hydrogen gas or other reductant to reduce for example the ferrous fluoride producing iron metal in a powdered form, as follows: FeF 2 3 H 2 Fe 6 HF The reduced iron completely eliminates the probability of its losses with sublimate.

Additionally this gives an advantage of producing another valuable pure iron metal. Iron can be mechanically separated from other impurities or otherwise used as a commercial product for metallurgy (other ingredients are fluorides of calcium and magnesium these are used as anti-friction components). Another invaluable advantage is that the surplus amounts of fluoride liberated in the course of this reaction creates an atmosphere favourable for more complete extraction of titanium from ilmenite, thus allowing considerable shortening of the initial fluorination and saving on equipment and ammonium bifluoride.

A non-fluorinated and non-volatile residue is formed as a result the sublimation of the reaction mixture to the titanium compounds and this residue is separated and extracted from F:\share\7000-7099\702600AUC\702600AUC 20051108 SDeci.doc O the titanium compounds. The non-fluorinated and non-volatile residue is further refined to c N extract thereform any precious metals or any other suitable metals such as Au, Pt, Pd, Ag,etc.

O

Eventually, the sublimated fluorides enter the last compartment where titanium undergoes 0 5 hydrolysis according to its reaction with water: TiF 4 2 H 2 0 TiO2 4 HF SThe resultant titanium dioxide precipitates on the reactor walls in the form of snow-white 0 10 fine crystals.

The hydrolysis of titanium compounds can be carried out either pyrolytically at elevated temperatures, according its reaction with steam or, alternatively, in two steps, these steps being: i) passing the titanium compounds in a condenser in order to condense the titanium compounds, and ii) hydrolysing the titanium compound condensate to produce titanium dioxide.

Ammonium fluoride evolved from different stages of the process, is mixed with ammonia solution, which is then evaporated and after crystallization reused at the fluorination stage.

A preferred method of the invention will now be described in association with figure 1 which is a process flow diagram illustrating the preferred process of the fluorine treatment of titanium materials into titanium oxide..

Ammonium bifluoride is gradually added to ilmenite or titano-magnetite at the molar ratio of 1. This minimises the viscosity of the composite mass, thus improving mixing and mass-transfer conditions in the fluorination reactor (F-reactor) 10. The reaction is complete within 0.5 6 hours, at the temperature between 120 and 1900, preferably 160-180 0 C. On heating above 190 0 C ammonia bifluoride vaporizes. Factors affecting the duration of fluorination are the temperature, mass ratio and fraction size of components. The reaction is complete when no more ammonia and steam are evolved from the reaction zone.

F:\share\7000-7099\702600AUC\702600AUC 20051108 Sneci.doc 11 O The sublimation of ammonium fluosilicate in the F-reactor 10 starts after the temperature is C increased and kept within a range from 220 to 300 0 C, preferably 225-245 0 C. Any values O above 300 0 C may lead to contamination of the sublimate with titanium. The volatilised ammonium fluosilicate is fed to a condenser 11 where it solidifies at 20 to 220 0 C. The O 5 condensed product is then transferred to a separator 12 to be treated with ammonia solution, followed by precipitation and further separation of silicon dioxide 13 by either filtration, c drying, etc.

All the off-products including ammonia, ammonium fluoride and steam, are withdrawn and 0 10 diverted to the ammonium bifluoride recovery system for further reuse in the process. The C1 ammonia can also be reused to produce pure silica.

The solid discharge from the F-reactor 10 consists of the complex fluoammonium salts of titanium, iron together with quantities of other metal flourides (Ca, Mg, Na, etc.) and oxides, plus a quantity of unreacted ilmenite. This solid discharge is transferred to a reactorsublimator 14 where the fluorinated mass is indirectly heated to 300-600 preferably to 540-580 0 C, with simultaneous feed of hydrogen or its mixture with inert gas (nitrogen, argon, etc.) into the reaction zone. The amount of hydrogen fed to reactor should be between and 100 percent from stoichiometric requirement. This ensures reduction of ferrous fluoride to iron metal, release of additional hydrogen fluoride and, thus, digestion of unreacted ilmenite. The reaction is complete within 2-5 hours.

The solid discharge from the reactor-sublimator 14 containing iron metal, other metals, other oxides and unvolatilized fluorides of calcium and magnesium undergo magnetic separation in a separator 15 to produce powdered iron 16 and residue 19. A non-fluorinated and nonvolatile residue 19 is formed as a result of the sublimation of the reaction mixture to the titanium compounds and this residue 19 is extracted from the titanium compounds and separated in separator 15 from iron. The non-fluorinated and non-volatile residue 19 is able to be further refined to extract therefrom any precious metals or any other suitable metals such as Au, Pt, Ag, Pd, etc.

The volatilised ammonium fluotitanate together with other gases is then fed to a condenserhydrolyzer 17 where steam is also added; the temperature of this reaction is kept within 300- F:\share\7000-7099\702600AUC\702600AUC 20051108 Soeci.doc 11 -12o 600 oC. As a result, titanium undergoes pyrolytic hydrolysis to form crystalline titanium c dioxide 18 precipitating on the walls of this reactor.

O

Or alternatively hydrolysis of the titanium compounds can also occur in two steps, these 0 5 steps being: i) passing the titanium compounds in a condenser 17A in order to condense the titanium compounds, and ii) hydrolysing the titanium compound condensate in a separator 17B to produce and extract titanium dioxide 18A.

C C1 The above process even though described in relation to the obtaining of titanium oxide can be readily applicable to the extraction of other valuable and/or precious metals and minerals such as Au, Pt, Pd, Ag, from sand, ore, or the like.

The process consists of the following stages: i) preparation of the raw material (crushing, grinding, sizing, etc of the ore); ii) adding fluorine source to the raw material (Hydrofluoric Acid, Ammonia Bifluoride, etc.); iii) fluorination at elevated temperature (preferably below 200 0 producing as a result complex salts ammonia fluosilicate) and non-fluorinated materials; iv) sublimation of the volatile complex salt at the temperatures above 200°C followed by condensation and hydrolysis of sublimate to produce high purity oxides of Si and Ti; v) reduction of ferrous fluoride to form iron metal; vi) separation of iron metal from residue using magnetic or any other type separator, the residue containing precious metals, non-volatile metallic fluorides and other non-fluorinated matter; vii) second fluorination with ammonium bifluoride to convert metal fluorides into ammonium fluometallates; viii) hydration followed by separation of soluble ammonium fluometallates from residue using any existing method (precipitation, filtration, etc.); F:\share\7000-7099\702600AUC\702600AUC 20051108 Soeci.doc -13ix) extraction of precious metals from residue by means of acid leaching, N, electrowinning, flotation, etc; 0 Sx) smelting precious metals followed by their refinery.

S 5 Turning to figure 2 which shows a process flow chart incorporating the the process described in figure 1, but which further includes a preferred process for the recovery of precious metals Cc and/or minerals such as Au, Pt, Pd, Ag, etc.. Ground ore or sand is passed through a separation unit 30 to separate a target fraction from tailings. The target fraction is then passed to a fluorination treatment unit 31 where precious metals and metal fluorides are S 10 separated from volatile silicon compounds. The silicon compounds are then passed through C1 a condensation-separation unit 32 so as to obtain silicon dioxide. The precious metals and metal fluorides are then passed through a reduction-sublimation unit 33 from which titanium compounds are extracted and passed through a separator reduction-sublimation unit 33A.

The iron, precious metals and metal fluorides is then passed through a separator 34 in order to separate iron from the precious metals and metal fluorides. The precious metals and metal fluorides are then passed through another fluorination treatment step 35 so as to form ammonia fluometallates and precious metals mixture. The ammonia fluometallates and precious metals are passed through a separator 36 to form and separate ammonia fluotitanates 39 from the precious metals mixture. The precious metals mixture is then passed through an extraction unit 37 to extract therefrom non-fluorinated residue 40. The precious metals are then refined in a refining unit 38 in order to refine and obtain the precious metals.

Advantages The proposed method allows manufacture high purity 99.98%) fine grade titanium dioxide with exceptional whiteness; Along with the main product titanium dioxide, other valuable products can be obtained, such as high purity silicon dioxide and metals such as iron; Method ensures substantial saving (up to 30-35%) on active ingredients, such as ammonium bifluoride, as a result of additional fluorination of the source material with fluoride released from iron reduction; therefore, the duration of fluorination is considerably shortened (1,5-2 times); F:\share\7000-7099\702600AUC\702600AUC 20051108 SDecidoc -14- S* Capital (equipment and space) saving achieved due to elimination of stages related to c calcination of an end product and also separation of the target elements after O sublimation; Proposed method has no waste or undesirable by-products, what makes it 5 environmentally attractive and cost-efficient.

r c Variations Throughout the description of this specification, the word "comprise" and variations of that I word such as "comprising" and "comprises", are not intended to exclude other additives, 0 10 components, integers or steps.

It will of course be realised that while the foregoing has been given by way of illustrative example of this invention, all such and other modifications and variations thereto as would be apparent to persons skilled in the art are deemed to fall within the broad scope and ambit of this invention as is hereinbefore described.

F:\share\7000-7099\702600AUC\702600AUC 20051108 Soeci.doc

Claims

2. The process as claimed in claim 1 wherein ammonium bifluoride is added to the titanium material at the molar ratio 1.
3. The process as claimed in claim 2 wherein the molar ratio is 1.
4. The process as claimed in claim 3 wherein the reacting the material with ammonium bifluoride at a temperature between 160-180 oC. The process as claimed in claim 3 wherein the reacting the material with ammonium bifluoride is complete within 0.5-6 hours.
6. The process as claimed in claim 3 wherein the reacting the material with ammonium bifluoride is complete within 0.5-10 hours.
7. The process as claimed in any one of the preceding claims wherein the first stage heating is kept within a temperature range of 225-245 °C in order to achieve sublimation of ammonium fluosilicate from the fluorinated mass. F:\share\7000-7099\702600AUC\702600AUC 20051108 Soeci.doc -16- O 8. The process as claimed in claim 7 wherein the extracted volatilised ammonium cN fluosilicate fed to a condenser to solidify before being chemically separated in a separator. O
9. The process as claimed in claim 8 wherein the solid ammonium fluosilicate is treated 0 5 with an ammonium solution to form silicon dioxide precipitate. ¢C 10. The process as claimed in claim 9 wherein the silicon dioxide precipitate obtained Shas a purity of at least 99.99%. 0 10 11. The process as claimed in anyone of the preceding claims wherein the reaction ,1 mixture is heated to a temperature between 540-580 oC.
12. The process as claimed in claim 11 wherein an inert gas is supplied during the second stage to ensure the oxygen-free condition of the reaction mixture.
13. The process as claimed any one of claims 11 to 12 wherein hydrogen gas is fed during the second stage to ensure reduction of the metallic fluorides to their metal form.
14. The process as claimed in claim 13 wherein the formed metal is separated from the titanium compounds. The process as claimed in claim 13 wherein the formed metal is iron.
16. The process as claimed in any one of the preceding claims wherein the second stage is complete within 2-5 hours.
17. The process as claimed in any one of the preceding claims wherein the titanium compound is volatilised ammonium fluotitanate.
18. The process as claimed in claim 17 wherein the volatilised ammonium fluotitanate is fed to a condenser-hydrolyser where it undergoes pyrolytic hydrolysis to produce titanium dioxide. F:\share\7000-7099\702600AUC\702600AUC 20051108 Sneci.doc -17- S19. The process as claimed in claim 18 wherein the titanium dioxide is produced in a crystalline form. 0 Z 20. The process as claimed in claim 19 wherein the crystalline titanium dioxide obtained S 5 has a purity of at least 99.98%. c 21. The process as claimed in any one of the preceding claims wherein the titanium material is a titanium bearing ore or sand.
22. The process according to claim 21, wherein the titanium bearing ore or sand is ilmenite or tiano-magnetite.
23. The process as claimed in any one of the claims 1 to 17 wherein the hydrolysis of the titanium compounds occurs in two steps, these steps being: i) passing the titanium compounds in a condenser in order to condense the titanium compounds, and ii) hydrolysing the titanium compound condensate to produce titanium dioxide.
24. The process as claimed in claim 23 wherein the hydrolysing of the titanium compound condensate involves adding an ammonia solution. The process as claimed in claim 13 wherein a non-fluorinated and non-volatile residue formed as a result of the sublimation of the reaction mixture to the titanium compounds is separated and extracted from the titanium compounds.
26. The process as claimed in claim 25 wherein the non-fluorinated and non-volatile residue is further refined to extract therefrom any precious metals or any other suitable valuables.
27. A process for the treatment of titanium materials, wherein the process includes: a) reacting the material with ammonium bifluoride at 50-190 0 C to form a fluorinated mass. and F:\share\7000-7099\702600AUC\702600AUC 20051108 Soeci.doc -18- o b) heating the fluorinated mass to 220-300 0 C to form a reaction mixture and volatilised ammonium fluosilicate and then extracting the volatilised 0 ammonium fluosilicate and chemically separate silicon dioxide from the volatilised ammonium fluosilicate in order to obtain a silica precipitate.
28. A method of processing the minerals in any form (liquid, gaseous or solid) aimed at ¢C extraction of the valuable products (Au, Pt, Pd, Ag, etc), consists of the following stages: i) preparation of the raw material (crushing, grinding, sizing, etc of the ore); O 10 ii) adding fluorine source to the raw material (Hydrofluoric Acid, Ammonia Bifluoride, etc.); iii) fluorination at elevated temperature (preferably below 200'C), producing as a result complex salts ammonia fluosilicate) and non-fluorinated materials; iv) sublimation of the volatile complex salt at the temperatures above 200 0 C followed by condensation and hydrolysis of sublimate to produce high purity oxides of Si and Ti; v) reduction of ferrous fluoride to form iron metal; vi) separation of iron metal from residue using magnetic or any other type separator, the residue containing precious metals, non-volatile metallic fluorides and other non-fluorinated matter; vii) second fluorination with ammonium bifluoride to convert metal fluorides into ammonium fluometallates; viii) hydration followed by separation of soluble ammonium fluometallates from residue using any existing method (precipitation, filtration, etc.); ix) extraction of precious metals from residue by means of acid leaching, electrowinning, flotation, etc; x) smelting precious metals followed by their refinery.
29. An apparatus for the treatment of titanium materials wherein the apparatus includes: a) a fluorination reactor in which the material is mixed with and reacts with ammonium bifluoride, wherein the fluorintion reactor is adapted to be heated to a temperature between 50-190 0 C to initially form a fluorinated mass and F:\share\7000-7099\702600AUC\702600AUC 20051108 Soeci.doc -19- O then adapted to cause the fluorinated mass to be heated to a temperature between 220-300 0 C to form a reaction mixture and volatilised ammonium 0 fluosilicate; b) a condenser connected to the fluorination reactor, wherein the condenser is 0 5 adapted to extract the volatilised ammonium fluosilicate from the fluorination reactor and condense the volatilised ammonium fluosilicate to a solid form; c€ c) a first separator connected to the condenser, wherein the separator is adapted 0to extract the solid form of ammonium fluosilicate and separate therefrom silicon dioxide; 0 10 d) a reactor sublimator connected to the fluorination reactor, wherein the reactor C1 sublimator is adapted to extract the reaction mixture from the fluorination reactor and heat the reaction mixture to a temperature between 300-600 0 C to sublimate reaction mixture to form titanium compounds and residue; and e) a condenser-hydrolser adapted to receive the titanium compounds from the reactor sublimator and adapted to hydrolyse the titanium compounds to produce titanium oxide. The apparatus as claimed in claim 25, wherein the apparatus has a second separator connected to the reactor sublimator, wherein the second separator is adapted to extract from the reactor sublimator the residue and separate therefrom pure metal.
31. A process for the treatment of metallic bearing materials as hereinbefore described with reference to figure 1.
32. A process for the treatment of titanium materials as hereinbefore described with reference to figure 1.
33. A method of processing the minerals as hereinbefore described with reference to figure 1.
34. An apparatus for the treatment of metallic bearing materials as hereinbefore described with reference to figure 1. F:\share\7000-7099\702600AUC\702600AUC 20051108 SDeci.doc 20 32. An apparatus for the treatment of metallic bearing materials as hereinbefore described with reference to figure 1. F:\share\7000-7099\702600AUC\702600AUC 20051108 Snecdoc