CA1115062A - Purification of rutile - Google Patents
Purification of rutileInfo
- Publication number
- CA1115062A CA1115062A CA326,300A CA326300A CA1115062A CA 1115062 A CA1115062 A CA 1115062A CA 326300 A CA326300 A CA 326300A CA 1115062 A CA1115062 A CA 1115062A
- Authority
- CA
- Canada
- Prior art keywords
- rutile
- ilmenite
- ore
- slurry
- suspended
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C22—METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
- C22B—PRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
- C22B34/00—Obtaining refractory metals
- C22B34/10—Obtaining titanium, zirconium or hafnium
- C22B34/12—Obtaining titanium or titanium compounds from ores or scrap by metallurgical processing; preparation of titanium compounds from other titanium compounds see C01G23/00 - C01G23/08
- C22B34/1236—Obtaining titanium or titanium compounds from ores or scrap by metallurgical processing; preparation of titanium compounds from other titanium compounds see C01G23/00 - C01G23/08 obtaining titanium or titanium compounds from ores or scrap by wet processes, e.g. by leaching
- C22B34/1259—Obtaining titanium or titanium compounds from ores or scrap by metallurgical processing; preparation of titanium compounds from other titanium compounds see C01G23/00 - C01G23/08 obtaining titanium or titanium compounds from ores or scrap by wet processes, e.g. by leaching treatment or purification of titanium containing solutions or liquors or slurries
Abstract
PURIFICATION OF RUTILE
ABSTRACT
Rutile which has been separated from ilmenite during a process for obtaining titanium metal values may be recovered in a more simple manner by effecting the water wash of the solid rutile at a pH above about 7.
ABSTRACT
Rutile which has been separated from ilmenite during a process for obtaining titanium metal values may be recovered in a more simple manner by effecting the water wash of the solid rutile at a pH above about 7.
Description
PURIFICATION OF RUTILE
SPECIE' ICAT ION
.
This invention relates to a method for treating the rutile product which is obtained during -the treatrnent of ilmenite. More particularly, the invention is concerned with an improvement in a method for treating rutile which has been separated from ilmenite whereby said rutile may be obtained in a form which is more readily handled during the subsequent steps for obtaining titanium dioxide.
Titanium in metallic form or as a compound is an important element in the chemical series. For example, titanium dioxide lS utilized in paint pigments, in white rubbers and plastics, floor coverings, glassware and cer-amics, printing inks and as an opacifying agent in papers.
Other titanium compounds are used in electronics, as flre retardants and waterproofing agents. The metal;~may be`used as such, or in alloy form as structural material in air-craft, in jet engines, marine equipment, textile machinery, surgical instruments, orthopedic appliances, sporting equip-ment and food handling eyuipment. When aktempting to sepa-rate titanium dioxide from impurities such as ilmenite and ~20 iron oxides, which are also contained in the titanium bear-ing sour such as ores, the separation is relatively d1f-ficult to effect whereby relatively low yields of titanium dioxide in a pure form are obtained. However, it has now been found that the separation of rutile, which is titanium dioxide, from ilmenite or ilmenite ores which is a compound ;~ of 'errous oxide and titanium dioxide, may be acco~plished
SPECIE' ICAT ION
.
This invention relates to a method for treating the rutile product which is obtained during -the treatrnent of ilmenite. More particularly, the invention is concerned with an improvement in a method for treating rutile which has been separated from ilmenite whereby said rutile may be obtained in a form which is more readily handled during the subsequent steps for obtaining titanium dioxide.
Titanium in metallic form or as a compound is an important element in the chemical series. For example, titanium dioxide lS utilized in paint pigments, in white rubbers and plastics, floor coverings, glassware and cer-amics, printing inks and as an opacifying agent in papers.
Other titanium compounds are used in electronics, as flre retardants and waterproofing agents. The metal;~may be`used as such, or in alloy form as structural material in air-craft, in jet engines, marine equipment, textile machinery, surgical instruments, orthopedic appliances, sporting equip-ment and food handling eyuipment. When aktempting to sepa-rate titanium dioxide from impurities such as ilmenite and ~20 iron oxides, which are also contained in the titanium bear-ing sour such as ores, the separation is relatively d1f-ficult to effect whereby relatively low yields of titanium dioxide in a pure form are obtained. However, it has now been found that the separation of rutile, which is titanium dioxide, from ilmenite or ilmenite ores which is a compound ;~ of 'errous oxide and titanium dioxide, may be acco~plished
-2-~5~
in a relatively simple manner by utilizing the process of the present invention. The advantage of utiliæing the process of the present invention is found in the fact that it is possible to obtain a high degree of rutile recovery using relatively low grade ilmenite ore as the starting material.
It is therefore an object of this invention to provide an improved process for the production of titanium dioxide values.
A further object of this invention is to pro~ide a process for obtaining high yields of titanium dioxide values from titanium bearing sources.
In one aspect an embodiment of this invention resides in a method for the separation of rutile which com-prises the steps of agitating a slurry of leach tails con-taining a mixture of ilmenite and ru-tile, allowing said slurry to settle, decanting the suspended rutile from the settled ilmenite, adjusting the pH o~ the decanted, suspended rutile solution to effect the flocculation of said rutile;
and recovering the flocculated rutile.
A specific embodiment of this invention is found in a method for the separation of rutile which comprises agitating a slurry of leach tails containing a mixture of ilmenite and rutile at a pH in the range of from 2 to 4, allowing said slurry to settle, decanting the suspended rutile from the settled ilmenite, adjusting the pH of the decanted suspended rutile solution to a pH in the range of from 7.1 to 10 by adding thereto sodium hydroxide whereby said rutlle is ilocculated, an~ recovering the ilocculated rutile.
.
~, The present invention is concerned with an im-provement in a method for effecting the treatment of rutile.
In one method oF effecting the recovery of titanium values from a titanium bearing source such as ilmenite which is a compound of ferrous oxide and titanium dioxide along with several other impurities, the ilmenite, after having been crushed to a desired mesh value, may be subjected to an oxidation step by being contacted with water at ambient temperature for a period of several days or by being con-tacted with an oxidizing gas such as oxygen or air at an alevated temperature for a period ranging from about 0.5 up to several hours. The oxidized metal bearing source such as the ilmenite is then divided into two portions. One portion is then subjected to a reductive roast in the presence of a reductant which may comprise hydrogen, car-bon monoxide~ or mixtures thereof and, after having unde~-gone the reductive roast for a period of time sufficient to effect a reduction of the metal bearing source at tempera-tures ranging from about 600 to about 1000C., the metal bearing source is then subjected to an aqueous hydrogen chloride leach. The leaching of the metal bearing source is usually effected at elevated temperatures in the range of from about 80 to about 100C. for a period of time which may range from about 0.25 to about 1 hour in duration.
Upon completion of the leaching step, the leached slurry is then subjected to precipitation by treating the slurry with the portion of the oxidized ore which was separated from the total portlon of the ore and whLcb was not sub~ected - -4_ ' to the reductive roast. The addition of the oxidized source to the leached solution is also ef~ected at elevated tem-peratures ranging from about 75 to about 105C. while sub-jecting the mixture to agitation or stirring for a period of time which may range from about 2 minutes up to about 1 hour in duration and causes the dissolved titanium to pre-cipitate as rutile.
The leach tails consisting of a mixture of un-reacted ilmenite and rutile is then separated from the leach liquox. Following this the leach tails are then treated with water in an agitator. Inasmuch as the leach-ing of the reduced ore was efected in an acidic medium, the pH of the aqueous solution will be at a value less than 7 and usually will be in a range of from 2 to 4.
. After agitating the mixture for a period which may range from 2 to 10 minutes, the agitation is dlscontinued and the ilmenite is allowed to settle. The.rutile which is present in the solution will remain in a suspended form and thus the settled ilmenite may be removed from the settler for retreatment.
Inasmuch as the leaching of the reduced ilmenite ore was effected in an acidic medium, the repulping of the . rutile product with wash water in order to remove any acids ~which may still adhere to the solids will be in ~he pH
range of less than 7. Due to the fact that the pH is on the acidic side and at a relatively low value, the wash water step will result in a stable suspension of the ru : : ' I tile in the wash water and it is therefore dif~icult to 1 . .
~ -5- ~
.
,.
recover the rutile from the colloidal suspension. It has now been found that by adjusting the pH of the wash water to a value in excess of 7, and preferably in a range of from 7.1 to 10, it is possible to produce a flocculated rutile. The flocculation of the rutile will permit the product to be subsequently recovered in a more simple manner than has heretofore been possible. In addition, the acid which adhered to the rutile solids during the filtering and drying step will be washed away in said water wash and thus the rutile product will be in purer form.
The adjustment of the pH to a range greater than 7 and preferably in a range of from 7.1 to 10 i9 efected by the addition of a basic compound. The basic compound will comprise a salt of an alkali metal or alkaline earth metal and for the purposes of the present specification and appended claims will include oxides, hydroxides, and - salts of weak acids. Some specific examples o these basic compounds which may be utilized will include sodium hydroxide, potassium hydroxide, lithium hydroxide, rubidium hydroxide, cesium hydroxide, magnesium hydroxide, calcium hydroxide, strontium hydroxide, barium hydroxide, magnesium oxide, calcium oxide, strontium oxide, barium oxide, sodium :~
carbonate, potassium carbonate, lithium carbonate, rubidium carbonate, cesium carbonate, magnesium carbonate, calcium .
carbonate, strontium carbonate, barium carbonate, sodium acetate, potassium acetate, lithium acetate, rubidium acetate, .cesium acetate, magnesium acetate, calcium acetate, strontium ~ t~ ~
acetate and barium acetate. It is to be understood that the aforementioned basic compounds are only representative of the class of compounds which may be employed and that the present invention is not necessarily limited thereto.
The amount of basic compound which is added will be de-pendent upon the desired pH and will usually be in a range of from 0.01 to 1.0~ by weight of the rutile.
The process of this invention may be effected in any suitable manner and may comprise a batch or con-tinuous type operation. For example, when a batch type operation is to be employed, a quantity of the ilmenite ore is crushed to the desired mesh value and thereafter subjected to an oxidizing step for a period of time suf-ficient to oxidize the ore. Thereafter the ore is divided into two portions, one portion of which is subjected to a reductive roast in an appropriate apparatus s~ch as an oven at an elevated temperature within the range herein-before set forth and in the presence of a reductant such as hydrogen, carbon monoxide, or mixtures thereof. After being reduced for a sufficient period of time, the reduced ilmenite ore is then removed from the oven and placed in an appropriate apparatus wherein it is subjected to a leaching step utilizing an aqueous hydrogen chloride ~olu-tion. Upon completion of the leaching step the slurry is then treated with the portion of the oxidized ore whioh did not undergo reduction in order to precipitate the rutile.
As previously discussed the leaching and the precipitation are effected at elevated temperatures.
..
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5~
After precipitation of the rutile is completed, the solids are separated from the spen leach liquor and placed in a separation vessel wherein the solids are treated as an aqueous slurry at a pH less than 7 in order to sus-S pend both the rutile and the ilmenite. After agitating the solution containing the ilmenite and rutile particles for a predetermined period of time in the aforesaid aqueous suspension, the agitation is discontinued, allowing the ilmenite to settle from suspension while ruti~e remains suspended. After settling of the ilmenite, the concen-trated rutile as a slurry is placed in a vessel wherein the pH is maintained in a range of from 7.1 to 10 by the addition of a basic compound of the type hereinbefore set forth. The rutile will flocculate and thus may be sepa-rated from the wash watex in a more simple manner of oper-ation. Thereafter the flocculated rutile may be collected and treated in any suitable manner known in the art to re-cover th desired titanium dioxide in purified form.
It is also contemplated within the scope of this invention that the process may be effected in a continuous manner of operation. When such a type of operation is used the ilmente ore which has been crushed to the desired mesh size lS continuously charged to an oxidation zone wherein it is contacted with an oxidizing agent such as air at an elevated temperature for a predetermined period of time.
After passage through the oxidative zone the ore is con-tinuously withdrawn and divided into two portions, one por- -tion of which is continuously charged to a reducing zone I
fl`9l~ ~
wherein a reduction of the ilmenite ore is effected at a temperature in the range of from about 600 to about 1100C.
The second portion of the ore is withdrawn and continuously charged to a precipitation zone hereinafter described.
After passage through the reducing zone such as an oven wherein the ilmenite i5 sub j ected to action of a reductant such as hydrogen, carbon monoxide, or a mixture of the two, the reduced ore is continuously withdrawn and passed to a leaching zone wherein the ore is contacted with an aqueous hydrogen chloride leach. After passage through the leach-ing zone which is maintained at an elevated temperature in the range of from about 80~ to ab~ut 100C., the pregnant leach liquor containing the soluble rutile in the form of titanium chloride, is continuously charged to a precipitation zone which is also maintained at an elevated temperature, usually in a range of from about 75 to about 105C. In the precipitation zone the leach liquor is admixed with the oxidized ore which is also continuously charged thereto and which had been separated from a portion of the total ore charge after oxidation thereof. After a predetermined period of time in the precipitation zone khe leach liquor containing the precipitated rutile and ilmenite is con-tinuously wlthdrawn and passed to a separation zone wherein the solids are separated from the leach liquor. After sepa-ration from the spent leach liquor the solids are then con-tinuously charged to a second separation zone wherein said solids are suspended in an aqueous slurry. After agitation in the second separation zone, the ilmenlte ore partlclos : _g _ 1- .
. . ~ . . . ~: . .
are continuously removed from the bottom of the separation cell while the concentrated rutile solids are continuously withdrawn and continuously charged to a recovery zone, the p~ of which is maintained above 7. The flocculated il-menite is then withdrawn from the recovery zone and treated to recover purified titanium dioxide.
The following examples are given for purposes of illustrating the process of this invention. However, it is to be understood that said examples are merely for purposes of illustration and that the present process is not necessarily limited thereto.
EXAMPLE I
In this example a natural ilmenite ore was ground to about -65 mesh. The ore was oxidized by treatment with air at a temperature of 750C. for a period of 1 hour.
Following this the ore was divided lnto two separate por-tions, one portion being subjected to a reductive roast in a reducing atmosphere comprising a mixture of hydrogen and carbon monoxide at a temperature of 750C. The il-menite was then subjected to an aqueous hydrogen chloride leach at a temperature of 100C. for a period o 0.25 hours. The pregnant leach liquor was then admixed with the second portion of the oxidized ore which had not been subjected to the reductive roast and agitated for a period of 0.25 hours at~100C.
The rutile product was separated from the spent leach li~uor, slurried in wash water and allowed to stand for a period of several days. However, the rutile formed --10-- . .
,.i~
~.$~
and remained in a stable colloidal suspension. The p~I
of the slurried rutile was determined to be less than 7.
EXAMPLE II
.
In this example an ore sample similar in nature to that described in Example I was treated in an identical manner down through the precipitation of the rutile by treatment of the leach liquor with a portion of the oxi-dized ore. The rutile which was recovered as the product was again slurried with 200 cc of water and the pH of the solution was adjusted to 8 by means of the addition of a suEficient amount of sodium hydroxide. The rutile floccu-lated rapidly and within 2 hours the solution clarified, the flocculated rutile being easily recovered from the solution.
EXAMPLE III
A 50 gram sample of leach tails which had been obtained by utilizing a process set forth in the above examples was slurried in about 200 cc of water at a pH of 2.5 and after agitation for a period of about 5 minutes was allowed to settle. After allowing the solution to stand for a period of 3 minutes, the slimes which comprise suspended solids were separated from the settled solids and recovered by raising the pH of the slurry to 8, caus-ing the suspended slimes to flocculate. The flocculated slimes were then easily separated from the water. X-ray analysis of the flocculated slimes detected a strong ru-tile constituency, while chemical analysis showed the .
presence of a minor amount of iron, vanadium, cobalt, 1 . .
~,if~
chromium and aluminum. x-ray analysis of the tails which had been used as the starting materi~l showed a strong il-menite pattern with a moderately weak pattern for sericite which is a silica mineral. The sink which comprised the settled solids consisted of ilmenite and silica minerals and showed, upon X-ray analysis, a strong ilmenite patte~n with large crystals. Therefore, it is apparent that a separation of a major portion of the ilmenite from the rutile may be accomplished while a further purification of the rutile is efected by treating the slimes in a manner similar to that hereinbefore set forth.
.
, , :
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in a relatively simple manner by utilizing the process of the present invention. The advantage of utiliæing the process of the present invention is found in the fact that it is possible to obtain a high degree of rutile recovery using relatively low grade ilmenite ore as the starting material.
It is therefore an object of this invention to provide an improved process for the production of titanium dioxide values.
A further object of this invention is to pro~ide a process for obtaining high yields of titanium dioxide values from titanium bearing sources.
In one aspect an embodiment of this invention resides in a method for the separation of rutile which com-prises the steps of agitating a slurry of leach tails con-taining a mixture of ilmenite and ru-tile, allowing said slurry to settle, decanting the suspended rutile from the settled ilmenite, adjusting the pH o~ the decanted, suspended rutile solution to effect the flocculation of said rutile;
and recovering the flocculated rutile.
A specific embodiment of this invention is found in a method for the separation of rutile which comprises agitating a slurry of leach tails containing a mixture of ilmenite and rutile at a pH in the range of from 2 to 4, allowing said slurry to settle, decanting the suspended rutile from the settled ilmenite, adjusting the pH of the decanted suspended rutile solution to a pH in the range of from 7.1 to 10 by adding thereto sodium hydroxide whereby said rutlle is ilocculated, an~ recovering the ilocculated rutile.
.
~, The present invention is concerned with an im-provement in a method for effecting the treatment of rutile.
In one method oF effecting the recovery of titanium values from a titanium bearing source such as ilmenite which is a compound of ferrous oxide and titanium dioxide along with several other impurities, the ilmenite, after having been crushed to a desired mesh value, may be subjected to an oxidation step by being contacted with water at ambient temperature for a period of several days or by being con-tacted with an oxidizing gas such as oxygen or air at an alevated temperature for a period ranging from about 0.5 up to several hours. The oxidized metal bearing source such as the ilmenite is then divided into two portions. One portion is then subjected to a reductive roast in the presence of a reductant which may comprise hydrogen, car-bon monoxide~ or mixtures thereof and, after having unde~-gone the reductive roast for a period of time sufficient to effect a reduction of the metal bearing source at tempera-tures ranging from about 600 to about 1000C., the metal bearing source is then subjected to an aqueous hydrogen chloride leach. The leaching of the metal bearing source is usually effected at elevated temperatures in the range of from about 80 to about 100C. for a period of time which may range from about 0.25 to about 1 hour in duration.
Upon completion of the leaching step, the leached slurry is then subjected to precipitation by treating the slurry with the portion of the oxidized ore which was separated from the total portlon of the ore and whLcb was not sub~ected - -4_ ' to the reductive roast. The addition of the oxidized source to the leached solution is also ef~ected at elevated tem-peratures ranging from about 75 to about 105C. while sub-jecting the mixture to agitation or stirring for a period of time which may range from about 2 minutes up to about 1 hour in duration and causes the dissolved titanium to pre-cipitate as rutile.
The leach tails consisting of a mixture of un-reacted ilmenite and rutile is then separated from the leach liquox. Following this the leach tails are then treated with water in an agitator. Inasmuch as the leach-ing of the reduced ore was efected in an acidic medium, the pH of the aqueous solution will be at a value less than 7 and usually will be in a range of from 2 to 4.
. After agitating the mixture for a period which may range from 2 to 10 minutes, the agitation is dlscontinued and the ilmenite is allowed to settle. The.rutile which is present in the solution will remain in a suspended form and thus the settled ilmenite may be removed from the settler for retreatment.
Inasmuch as the leaching of the reduced ilmenite ore was effected in an acidic medium, the repulping of the . rutile product with wash water in order to remove any acids ~which may still adhere to the solids will be in ~he pH
range of less than 7. Due to the fact that the pH is on the acidic side and at a relatively low value, the wash water step will result in a stable suspension of the ru : : ' I tile in the wash water and it is therefore dif~icult to 1 . .
~ -5- ~
.
,.
recover the rutile from the colloidal suspension. It has now been found that by adjusting the pH of the wash water to a value in excess of 7, and preferably in a range of from 7.1 to 10, it is possible to produce a flocculated rutile. The flocculation of the rutile will permit the product to be subsequently recovered in a more simple manner than has heretofore been possible. In addition, the acid which adhered to the rutile solids during the filtering and drying step will be washed away in said water wash and thus the rutile product will be in purer form.
The adjustment of the pH to a range greater than 7 and preferably in a range of from 7.1 to 10 i9 efected by the addition of a basic compound. The basic compound will comprise a salt of an alkali metal or alkaline earth metal and for the purposes of the present specification and appended claims will include oxides, hydroxides, and - salts of weak acids. Some specific examples o these basic compounds which may be utilized will include sodium hydroxide, potassium hydroxide, lithium hydroxide, rubidium hydroxide, cesium hydroxide, magnesium hydroxide, calcium hydroxide, strontium hydroxide, barium hydroxide, magnesium oxide, calcium oxide, strontium oxide, barium oxide, sodium :~
carbonate, potassium carbonate, lithium carbonate, rubidium carbonate, cesium carbonate, magnesium carbonate, calcium .
carbonate, strontium carbonate, barium carbonate, sodium acetate, potassium acetate, lithium acetate, rubidium acetate, .cesium acetate, magnesium acetate, calcium acetate, strontium ~ t~ ~
acetate and barium acetate. It is to be understood that the aforementioned basic compounds are only representative of the class of compounds which may be employed and that the present invention is not necessarily limited thereto.
The amount of basic compound which is added will be de-pendent upon the desired pH and will usually be in a range of from 0.01 to 1.0~ by weight of the rutile.
The process of this invention may be effected in any suitable manner and may comprise a batch or con-tinuous type operation. For example, when a batch type operation is to be employed, a quantity of the ilmenite ore is crushed to the desired mesh value and thereafter subjected to an oxidizing step for a period of time suf-ficient to oxidize the ore. Thereafter the ore is divided into two portions, one portion of which is subjected to a reductive roast in an appropriate apparatus s~ch as an oven at an elevated temperature within the range herein-before set forth and in the presence of a reductant such as hydrogen, carbon monoxide, or mixtures thereof. After being reduced for a sufficient period of time, the reduced ilmenite ore is then removed from the oven and placed in an appropriate apparatus wherein it is subjected to a leaching step utilizing an aqueous hydrogen chloride ~olu-tion. Upon completion of the leaching step the slurry is then treated with the portion of the oxidized ore whioh did not undergo reduction in order to precipitate the rutile.
As previously discussed the leaching and the precipitation are effected at elevated temperatures.
..
:
,' , . :.. ,.... . ~ ., ~
5~
After precipitation of the rutile is completed, the solids are separated from the spen leach liquor and placed in a separation vessel wherein the solids are treated as an aqueous slurry at a pH less than 7 in order to sus-S pend both the rutile and the ilmenite. After agitating the solution containing the ilmenite and rutile particles for a predetermined period of time in the aforesaid aqueous suspension, the agitation is discontinued, allowing the ilmenite to settle from suspension while ruti~e remains suspended. After settling of the ilmenite, the concen-trated rutile as a slurry is placed in a vessel wherein the pH is maintained in a range of from 7.1 to 10 by the addition of a basic compound of the type hereinbefore set forth. The rutile will flocculate and thus may be sepa-rated from the wash watex in a more simple manner of oper-ation. Thereafter the flocculated rutile may be collected and treated in any suitable manner known in the art to re-cover th desired titanium dioxide in purified form.
It is also contemplated within the scope of this invention that the process may be effected in a continuous manner of operation. When such a type of operation is used the ilmente ore which has been crushed to the desired mesh size lS continuously charged to an oxidation zone wherein it is contacted with an oxidizing agent such as air at an elevated temperature for a predetermined period of time.
After passage through the oxidative zone the ore is con-tinuously withdrawn and divided into two portions, one por- -tion of which is continuously charged to a reducing zone I
fl`9l~ ~
wherein a reduction of the ilmenite ore is effected at a temperature in the range of from about 600 to about 1100C.
The second portion of the ore is withdrawn and continuously charged to a precipitation zone hereinafter described.
After passage through the reducing zone such as an oven wherein the ilmenite i5 sub j ected to action of a reductant such as hydrogen, carbon monoxide, or a mixture of the two, the reduced ore is continuously withdrawn and passed to a leaching zone wherein the ore is contacted with an aqueous hydrogen chloride leach. After passage through the leach-ing zone which is maintained at an elevated temperature in the range of from about 80~ to ab~ut 100C., the pregnant leach liquor containing the soluble rutile in the form of titanium chloride, is continuously charged to a precipitation zone which is also maintained at an elevated temperature, usually in a range of from about 75 to about 105C. In the precipitation zone the leach liquor is admixed with the oxidized ore which is also continuously charged thereto and which had been separated from a portion of the total ore charge after oxidation thereof. After a predetermined period of time in the precipitation zone khe leach liquor containing the precipitated rutile and ilmenite is con-tinuously wlthdrawn and passed to a separation zone wherein the solids are separated from the leach liquor. After sepa-ration from the spent leach liquor the solids are then con-tinuously charged to a second separation zone wherein said solids are suspended in an aqueous slurry. After agitation in the second separation zone, the ilmenlte ore partlclos : _g _ 1- .
. . ~ . . . ~: . .
are continuously removed from the bottom of the separation cell while the concentrated rutile solids are continuously withdrawn and continuously charged to a recovery zone, the p~ of which is maintained above 7. The flocculated il-menite is then withdrawn from the recovery zone and treated to recover purified titanium dioxide.
The following examples are given for purposes of illustrating the process of this invention. However, it is to be understood that said examples are merely for purposes of illustration and that the present process is not necessarily limited thereto.
EXAMPLE I
In this example a natural ilmenite ore was ground to about -65 mesh. The ore was oxidized by treatment with air at a temperature of 750C. for a period of 1 hour.
Following this the ore was divided lnto two separate por-tions, one portion being subjected to a reductive roast in a reducing atmosphere comprising a mixture of hydrogen and carbon monoxide at a temperature of 750C. The il-menite was then subjected to an aqueous hydrogen chloride leach at a temperature of 100C. for a period o 0.25 hours. The pregnant leach liquor was then admixed with the second portion of the oxidized ore which had not been subjected to the reductive roast and agitated for a period of 0.25 hours at~100C.
The rutile product was separated from the spent leach li~uor, slurried in wash water and allowed to stand for a period of several days. However, the rutile formed --10-- . .
,.i~
~.$~
and remained in a stable colloidal suspension. The p~I
of the slurried rutile was determined to be less than 7.
EXAMPLE II
.
In this example an ore sample similar in nature to that described in Example I was treated in an identical manner down through the precipitation of the rutile by treatment of the leach liquor with a portion of the oxi-dized ore. The rutile which was recovered as the product was again slurried with 200 cc of water and the pH of the solution was adjusted to 8 by means of the addition of a suEficient amount of sodium hydroxide. The rutile floccu-lated rapidly and within 2 hours the solution clarified, the flocculated rutile being easily recovered from the solution.
EXAMPLE III
A 50 gram sample of leach tails which had been obtained by utilizing a process set forth in the above examples was slurried in about 200 cc of water at a pH of 2.5 and after agitation for a period of about 5 minutes was allowed to settle. After allowing the solution to stand for a period of 3 minutes, the slimes which comprise suspended solids were separated from the settled solids and recovered by raising the pH of the slurry to 8, caus-ing the suspended slimes to flocculate. The flocculated slimes were then easily separated from the water. X-ray analysis of the flocculated slimes detected a strong ru-tile constituency, while chemical analysis showed the .
presence of a minor amount of iron, vanadium, cobalt, 1 . .
~,if~
chromium and aluminum. x-ray analysis of the tails which had been used as the starting materi~l showed a strong il-menite pattern with a moderately weak pattern for sericite which is a silica mineral. The sink which comprised the settled solids consisted of ilmenite and silica minerals and showed, upon X-ray analysis, a strong ilmenite patte~n with large crystals. Therefore, it is apparent that a separation of a major portion of the ilmenite from the rutile may be accomplished while a further purification of the rutile is efected by treating the slimes in a manner similar to that hereinbefore set forth.
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Claims (10)
PROPERTY OR PRIVILEGE IS CLAIMED ARE DEFINED AS FOLLOWS:
1. A method for the separation of rutile which comprises the steps of:
(a) agitating a slurry of leach tails containing a mixture of ilmenite and rutile;
(b) allowing said slurry to settle;
(c) decanting the suspended rutile from the settled ilmenite;
(d) adjusting the pH of the decanted, suspended rutile solution to effect the flocculation of said rutile; and, (e) recovering the flocculated rutile.
(a) agitating a slurry of leach tails containing a mixture of ilmenite and rutile;
(b) allowing said slurry to settle;
(c) decanting the suspended rutile from the settled ilmenite;
(d) adjusting the pH of the decanted, suspended rutile solution to effect the flocculation of said rutile; and, (e) recovering the flocculated rutile.
2. The method of Claim 1 wherein the agitation of said slurry of leach tails is effected at a pH less than 7.
3. The method of Claim 2 wherein said pH is in a range of from 2 to 4.
4. The method of Claim 1 wherein the flocculation of said suspended rutile is effected at a pH in excess of 7.
5. The method of Claim 4 wherein the pH of the solution is maintained in the range of from 7.1 to 10.
6. The method of Claim 4 wherein said pH is provided for by the presence of a basic compound.
7. The method of Claim 6 wherein said basic compound is a salt of an alkali metal or alkaline earth metal.
8. The method of Claim 7 wherein said basic compound is sodium hydroxide.
9. The method of Claim 7 wherein said basic com-pound is potassium hydroxide.
10. The method of Claim 7 wherein said basic com-pound is calcium oxide.
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US05/902,630 US4152252A (en) | 1978-05-04 | 1978-05-04 | Purification of rutile |
| US902,630 | 1978-05-04 |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CA1115062A true CA1115062A (en) | 1981-12-29 |
Family
ID=25416139
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CA326,300A Expired CA1115062A (en) | 1978-05-04 | 1979-04-25 | Purification of rutile |
Country Status (10)
| Country | Link |
|---|---|
| US (1) | US4152252A (en) |
| JP (1) | JPS5515988A (en) |
| AU (1) | AU524491B2 (en) |
| CA (1) | CA1115062A (en) |
| DE (1) | DE2917905A1 (en) |
| ES (1) | ES8107034A1 (en) |
| FR (1) | FR2424879A1 (en) |
| GB (1) | GB2022563A (en) |
| IT (1) | IT1115187B (en) |
| NO (1) | NO791478L (en) |
Families Citing this family (13)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US5316664A (en) * | 1986-11-24 | 1994-05-31 | Canadian Occidental Petroleum, Ltd. | Process for recovery of hydrocarbons and rejection of sand |
| US5340467A (en) * | 1986-11-24 | 1994-08-23 | Canadian Occidental Petroleum Ltd. | Process for recovery of hydrocarbons and rejection of sand |
| ZA898010B (en) * | 1988-10-24 | 1990-08-29 | Wimmera Ind Minerals Proprieta | Separation of chromite from metalliferous ores |
| US5559035A (en) * | 1992-08-24 | 1996-09-24 | Umpqua Research Company | Solid phase calibration standards |
| US6375923B1 (en) | 1999-06-24 | 2002-04-23 | Altair Nanomaterials Inc. | Processing titaniferous ore to titanium dioxide pigment |
| US6548039B1 (en) | 1999-06-24 | 2003-04-15 | Altair Nanomaterials Inc. | Processing aqueous titanium solutions to titanium dioxide pigment |
| US6440383B1 (en) | 1999-06-24 | 2002-08-27 | Altair Nanomaterials Inc. | Processing aqueous titanium chloride solutions to ultrafine titanium dioxide |
| WO2006017336A2 (en) * | 2004-07-13 | 2006-02-16 | Altairnano, Inc. | Ceramic structures for prevention of drug diversion |
| AU2006283170A1 (en) * | 2005-08-23 | 2007-03-01 | Altairnano, Inc. | Highly photocatalytic phosphorus-doped anatase-TiO2 composition and related manufacturing methods |
| US20080020175A1 (en) * | 2006-03-02 | 2008-01-24 | Fred Ratel | Nanostructured Indium-Doped Iron Oxide |
| US20080038482A1 (en) * | 2006-03-02 | 2008-02-14 | Fred Ratel | Method for Low Temperature Production of Nano-Structured Iron Oxide Coatings |
| WO2007103829A1 (en) * | 2006-03-02 | 2007-09-13 | Altairnano, Inc. | Method for production of metal oxide coatings |
| US20080254258A1 (en) * | 2007-04-12 | 2008-10-16 | Altairnano, Inc. | Teflon® replacements and related production methods |
Family Cites Families (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US1937037A (en) * | 1931-08-07 | 1933-11-28 | Krebs Pigment & Color Corp | Process of making titanium oxide of fine texture |
| US2121992A (en) * | 1936-02-28 | 1938-06-28 | Sherwin Williams Co | Purification of titanium fluoride solutions |
| US2437164A (en) * | 1944-12-08 | 1948-03-02 | Du Pont | Processing of titanium ores |
| FR1064964A (en) * | 1951-10-24 | 1954-05-19 | Titan Co | Method of accelerating the formation of rutile in hydrated titanium compounds |
| NL136820C (en) * | 1963-01-07 | 1900-01-01 | ||
| US3446348A (en) * | 1965-10-15 | 1969-05-27 | Freeport Sulphur Co | Process for treating clay |
| AU496809B2 (en) * | 1975-04-02 | 1978-11-02 | Inco Limited | Process forthe recovery of metals from solution |
-
1978
- 1978-05-04 US US05/902,630 patent/US4152252A/en not_active Expired - Lifetime
-
1979
- 1979-04-25 CA CA326,300A patent/CA1115062A/en not_active Expired
- 1979-05-02 AU AU46656/79A patent/AU524491B2/en not_active Ceased
- 1979-05-03 NO NO791478A patent/NO791478L/en unknown
- 1979-05-03 GB GB7915456A patent/GB2022563A/en not_active Withdrawn
- 1979-05-03 ES ES480188A patent/ES8107034A1/en not_active Expired
- 1979-05-03 IT IT22337/79A patent/IT1115187B/en active
- 1979-05-03 DE DE19792917905 patent/DE2917905A1/en not_active Withdrawn
- 1979-05-04 FR FR7911303A patent/FR2424879A1/en active Granted
- 1979-05-04 JP JP5516879A patent/JPS5515988A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| GB2022563A (en) | 1979-12-19 |
| NO791478L (en) | 1979-11-06 |
| AU4665679A (en) | 1979-11-08 |
| FR2424879B1 (en) | 1982-10-15 |
| US4152252A (en) | 1979-05-01 |
| ES480188A0 (en) | 1981-10-01 |
| IT7922337A0 (en) | 1979-05-03 |
| DE2917905A1 (en) | 1979-11-08 |
| AU524491B2 (en) | 1982-09-16 |
| IT1115187B (en) | 1986-02-03 |
| ES8107034A1 (en) | 1981-10-01 |
| JPS5515988A (en) | 1980-02-04 |
| JPS56374B2 (en) | 1981-01-07 |
| FR2424879A1 (en) | 1979-11-30 |
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