Patent Application
20180202024
The present invention belongs to the technical field of metallurgy and particularly relates to a method for producing titanium and titanium aluminum alloys through two-stage aluminothermic reduction and obtaining titanium-free cryolite as byproducts.
Titanium is a light rare metal material and is widely applied in the technical fields of aviation, aerospace and chemical engineering. At present, titanium is produced by a method for reducing titanium tetrachloride (TiCl4) with magnesium at high temperature, and the titanium produced by the method is spongy. The titanium can also be produced by a method for reducing titanium tetrachloride(TiCl4) with sodium at high temperature. The method for producing titanium by reducing the titanium tetrachloride(TiCl4) with the magnesium or the sodium is high in cost. In addition, Cl2 is a raw material during production of the TiCl4, and the byproduct in reduction process is chloride. Since Cl2 and the chloride are strong corrosive to equipment, the operation conditions are complicated and extreme. Therefore, people also continuously explore other smelting methods for producing titanium, such as fused salt electrolysis of TiCl4, and electro-deoxidization fused salt electrolysis of TiO2 which is used as a negative pole, but the methods are still in a laboratory research stage and do not succeed in the industry. Additionally, methods for producing the titanium by using sodium fluotitanate or potassium fluotitanate or titanium trifluoride as a raw material and using Al—Zn, Al—Mg, and Al—Zn—Mg alloys as well as pure Al, pure Mg and pure Na as reducing agents, also exist (see US2010/0173170A1, CN102534263A, CN102560153A and CN102534260A). According to the methods of producing titanium, the purity of titanium can be 70.7% or above, and the maximum purity can be 99.5%.
The reduction reactions are all performed at the temperature of 900-1000° C., but the methods still cannot be applied in the industry. The methods have the disadvantages and problems as follows:
1. The reduction process is comparatively complicated; in the methods disclosed by the patents, the reducing agents are mixed and fused firstly, and then the mixed and fused compound reducing agents are added or dropped into the raw material needed to reduce; and the reaction material needs to be stirred in the reaction process, and finally products should be separated out;
2. when the reduction agent is Al—Zn alloys, Zn does not participate in the reduction reaction, so that Zn needs to be separated out the purification technology is complicated, and the production cost is greatly increased; and
3. in the technical methods disclosed by the patents, the byproducts mainly Na3AlF6 and AlF3 separated out from products are black or grey-black and contain a lot of titanium compounds, so that the loss of titanium is caused.
With the development of aviation and aerospace techniques and requirements for some high-temperature corrosion-resistant materials in the chemical engineering field, the development of Ti—Al alloys or Ti—Al-based high-performance alloys doped with some other metal elements is extensively concerned in various countries of the world. However, raw metals of the alloys are all produced by the method of smelting pure metal aluminum and sponge titanium which are produced by magnesiothermic reduction for TiCl4, and the production technology is comparatively complicated.
For the problems existing in the production technique of titanium, the present invention provides a method for producing titanium and titanium aluminum alloys through two-stage aluminothermic reduction and producing titanium-free cryolite as byproducts; the titanium-free cryolite containing the extremely low content of titanium can be used for electrolytic aluminum industry. The two-stage aluminothermic reduction method consists of a first-stage aluminothermic reduction process and a second-stage aluminothermic reduction process. In the first-stage aluminothermic reduction process, the titanium or the titanium aluminum alloys are the to-be-produced products, and sodium fluoride and sodium fluotitanate are used as raw materials, or sodium fluotitanate is used as raw material, and powder made of the Al—Ti alloys produced by the second-stage aluminothermic reduction process is used as reducing agent. The titanium or the titanium aluminum alloys are produced by the first-stage aluminothermic reduction. In the first-stage aluminothermic reduction process, the materials and the reducing agent participating in the reduction reaction are mixed and pressed into lumps, and the lumps are heated to 900-1300° C. under the vacuum or argon protection condition for aluminothermic reduction. Then, the reduction product is separated through vacuum distillation at the temperature of 900-1300° C., so as to obtain titanium-containing cryolite and the titanium or the titanium aluminum alloys. In the second-stage aluminothermic reduction process, the titanium-containing cryolite produced by the first-stage aluminothermic reduction is used as a raw material, and aluminum powder is used as reducing agent. The titanium-containing cryolite and the reducing agent are mixed and pressed into lumps, and the lumps are reduced under the argon protection condition at the temperature of 900-1300° C., so as to obtain the titanium-free cryolite and the aluminum titanium alloys. In the second-stage aluminothermic reduction process, the feeding quantity of the reducing agent follows a rule that the melting point of the aluminum titanium alloys produced after the second-stage reduction process is lower than the temperature of the reduction reaction. In the second-stage aluminothermic reduction process, the aluminum titanium alloys and the titanium-free cryolite are mutually insoluble, so that the aluminum titanium alloy melt and the titanium-free cryolite melt can be well separated out in the molten state. the titanium in the aluminum titanium alloys produced by the second-stage aluminothermic reduction mainly exist in the form of TiAl3 metallic compound, and most of TiAl3 metallic compound settle at the bottom of the alloy melt in a slow cooling process, therefore, low-titanium aluminum titanium alloys with lower content of titanium are formed at the upper part, and high-titanium aluminum titanium alloys with higher content of titanium are formed at the lower part. When the second-stage reduction reaction completed and the reduction product cooled, the solid titanium-free cryolite can be separated from the aluminum titanium alloys. The aluminum titanium alloys separated out in the second-stage aluminothermic reduction process are remolten and made into powder to be used as the reducing agent of the first-stage aluminothermic reduction. The aluminum titanium alloys produced in the second-stage aluminothermic reduction can also be separated out by adopting one of the following two methods: 1, separating the low-titanium aluminum titanium alloys from the high-titanium Al—Ti alloys by a mechanical method. 2, putting the aluminum titanium alloys obtained by the second-stage aluminothermic reduction into a tiltable induction furnace for remelting, after standing for a period of time, firstly pouring out the low-titanium aluminum titanium alloys at the upper part, and then digging out the high-titanium aluminum titanium alloys at the bottom, so that the purpose of separating the high-titanium aluminum titanium alloys from the low-titanium aluminum titanium alloys is realized. The low-titanium aluminum titanium alloys which are divided out or separated are made into powder, and the powder is used as the reducing agent of the first-stage aluminothermic reduction, and the high-titanium aluminum titanium alloys with higher content of titanium are sold as commodities.
The method provided by the present invention comprises the following steps:
1. using sodium fluotitanate as the raw material, or using sodium fluoride and sodium fluotitanate as the raw materials. when the titanium and the titanium aluminum alloys are produced and manufactured, using the aluminum titanium alloy powder produced in the second-stage aluminothermic reduction as the reducing agent. In addition, designing the proportion of all the materials according to the to-be-produced product, wherein the reaction formulas of the production proportion are shown as follows:
3Na2TiF6+2NaF+(3x+4)Al=3TiAlx+Na3AlF6+Na5Al3F14, 10≥x≥0 (1)
Ti+xAl=TiAlx, x=0-10 (2);
or,
12Na2TiF6+(12x+16)Al=12TiAlx+3Na3AlF6+3Na5Al3F14+4AlF3, 10≥x≥0 (3);
and, Ti+xAl=TiAlx, x=0-10 (4);
2. uniformly mixing the raw materials with the reducing agent to obtain a mixture, pressing the mixture into lumps, placing the lumps into a vacuum reduction furnace, heating the placed lumps to 900-1300° C. under the vacuum condition or in the argon atmosphere, performing the first-stage aluminothermic reduction, and separating the reduction product by vacuum distillation at the temperature of 900-1300° C.; coagulating the titanium-containing cryolite distilled out on a crystallizer at the low-temperature end of the vacuum reduction furnace, wherein the product mainly comprises Na3AlF6, Na5Al3F14, AlF3 and titanium-containing sub-fluoride, the residual product which is not distilled out in the reduction furnace is the metal Ti or the titanium aluminum alloys.
Because of containing some unreacted sodium fluotitanate and titanium-containing sub-fluoride produced by a side reaction, the product distilled out after the first-stage aluminothermic reduction is black-grey, so that the product distilled out is called as the titanium-containing cryolite;
3. taking out the titanium-containing cryolite, grinding it until the particle size is less than 1.0 mm, using the aluminum powder as the reducing agent, uniformly mixing the grinded titanium-containing cryolite with the aluminum powder to obtain a mixture, and pressing the mixture into lumps, wherein the feeding amount of the aluminum powder follows the rule that the melting point of the aluminum titanium alloys produced by the second-stage aluminothermic reduction is less than or equal to the temperature of the second-stage reduction reaction; placing the lumps in the reduction furnace, heating the placed lumps to 900-1300° C. in the argon atmosphere and preserving the temperature for 0.5-2 h for the second-stage aluminothermic reduction, wherein when the reduction reaction completed and the temperature in the furnace reduced to normal temperature, white easily-broken titanium-free cryolite is formed at the upper parts of the product and the aluminum titanium alloys are formed at the bottom of the product, wherein the low-titanium aluminum titanium alloys with low content of titanium are formed at the upper parts of the aluminum titanium alloys, which are called as the low-titanium aluminum titanium alloys, and the aluminum titanium alloys with comparatively high content of titanium are formed at the lower parts of the aluminum titanium alloys, which are called as the high-titanium aluminum titanium alloys; and
4. remelting the aluminum titanium alloys produced by the second-stage aluminothermic reduction, making the aluminum titanium alloys into powder and returning the powder back to the first-stage aluminothermic reduction by using as the reducing agent, which are shown as in the flow diagram of
In the method, when the first-stage aluminothermic reduction is performed for the first time, the metal aluminum powder is used as the reducing agent if no available aluminum titanium alloys are used as the reducing agent, and the dosage of the reducing agent in step 1 is designed according to the to-be-produced product, and the reaction formulas of the production proportion are respectively shown in (1), (2) or (3), (4).
In the method, the titanium-containing cryolite in step 2 mainly comprises Na3AlF6, Na5Al3F14, AlF3 and titanium-containing sub-fluoride, wherein the titanium mainly exists in the form of Na3TiF6, TiF3 and a small amount of Ti. Since the content of AlF3, TiF3 and titanium powder are small in the mixture, they are possibly not obvious in an XRD (x-ray diffraction) analysis result of the product.
In the method, the argon condition in step 2 and step 3 refers to that the reduction furnace is vacuumized to 10 Pa or below, and then argon is inflated to realize normal pressure.
In the method, the vacuum distillation refers to that distillation is performed for 1 h or above under the condition that the vacuum of the reduction furnace is 10 Pa or below, and the temperature is 900-1300° C.
The method provided by the present invention is simple to operate, lower corrosion to the equipment, and high in purity of obtained cryolite, titanium and titanium aluminum alloys. The method also does not need complicated equipment. The reaction process of the method and the contents of Ti and Al in the alloys are easy to control, and the production cost is low, and the reduction rate of titanium and the utilization rate of aluminum are 100%. The byproduct namely the cryolite obtained by the method is high in purity and can be used in the aluminum electrolysis industry.
XRD phase analysis equipment adopted in an embodiment of the present invention is an X'Pert Pro type X-ray diffractometer.
SEM morphology analysis equipment adopted in an embodiment of the present invention is an S-4800 type cold field emission scanning electron microscope.
EDS detection equipment adopted in an embodiment of the present invention is an accessory X-ray energy spectrometer of the S-4800 type scanning electron microscope.
Metal aluminum powder adopted in an embodiment of the present invention is a product purchased on the market, and the purity of the metal aluminum powder is greater than or equal to 99%.
Sodium fluoride adopted in an embodiment of the present invention is a powder product purchased on the market, and the purity of the sodium fluoride is greater than or equal to 98%.
Sodium fluotitanate adopted in an embodiment of the present invention is a powder product purchased on the market, and the purity of the sodium fluotitanate is greater than or equal to 98%.
A reduction furnace adopted in an embodiment of the present invention is a vacuum reduction furnace with a crystallizer.
1. Sodium fluoride and sodium fluotitanate are used as raw materials, and 100 g of aluminum titanium alloy powder containing 4.21 wt % of titanium is used as reducing agent; when Ti3Al alloys (x=1/3 in the formula (1)) are produced, the reaction formulas of the production proportion of all the materials are shown as follows:
3Na2TiF6+2NaF+5Al=Ti3Al+Na3AlF6+Na5Al3F14 (5)
and, 3Ti+Al=Ti3Al (6);
according to the chemical reaction formulas (5) and (6), it can be obtained that 100 g of the reducing agent (aluminum titanium alloy powder) contains 4.21 g of Ti, namely the content of Ti3Al is 5 g, Al powder participating into the reduction reaction is 95 g, the content of Na2TiF6 required by the reaction is 439.11 g, and the content of NaF required by the reaction is 59.11 g; therefore, the actual production materials of the embodiment comprise 439.11 g of Na2TiF6, 59.11 g of NaF and 100 g of the aluminum titanium alloy powder containing 4.21 wt % of titanium;
2. the production materials are uniformly mixed and then are pressed into lumps, the lumps are placed into a vacuum reduction furnace, the reduction furnace is vacuumized to 10 Pa or below, argon is inflated into the reduction furnace to realize normal pressure, and the reduction furnace is heated to 1100° C. under the argon atmosphere condition, so that a first-stage aluminothermic reduction reaction is completed; and
3. after the reduction reaction is ended, the reduction furnace is vacuumized to 10 Pa or below, a product of the reduction reaction is distilled for 2 h under the vacuum condition at the temperature of 1100° C., a distillation product on a crystallizer at the low-temperature end in the vacuum reduction furnace is titanium-containing cryolite, and an alloy product is reserved in a reactor in a loose spongy form; an XRD phase analysis result of the alloy product is shown in
1. Sodium fluotitanate is used as raw materials, and 100 g of titanium aluminum alloy powder containing 4.21 wt % of titanium is used as reducing agent; when the produced product is Ti3Al alloys (x=1/3 in the formula (3)), the reaction formulas of the production proportion of all the materials are shown as follows:
12Na2TiF6+20Al=4Ti3Al+3Na3AlF6+3Na5Al3F14+4AlF3 (7)
and, 3Ti+Al=Ti3Al (8);
according to the chemical reaction formulas (7) and (8), it can be obtained that 100 g of the reducing agent (titanium aluminum alloy powder) contains 4.21 g of Ti, namely the content of Ti3Al is 5 g, Al powder participating into the reduction reaction is 95 g, and the content of Na2TiF6 required by the reaction is 439.11 g; therefore, the actual production materials of the embodiment comprise 439.11 g of Na2TiF6 and 100 g of the titanium aluminum alloy powder containing 4.21 wt % of titanium;
2. the production materials are uniformly mixed and then are pressed into lumps, the lumps are placed into a vacuum reduction furnace, the reduction furnace is vacuumized to 10 Pa or below, and the reduction furnace is heated to 1100° C. under the argon atmosphere condition, so that a first-stage aluminothermic reduction reaction is completed; and
3. after the reduction reaction is ended, the reduction furnace is vacuumized to 10 Pa or below, a product of the reduction reaction is distilled for 2 h under the vacuum condition at the temperature of 1100° C., the distillation product on the crystallizer at the low-temperature end in the vacuum reduction furnace is a mixture of the titanium-containing cryolite and aluminium fluoride, and an alloy product is reserved in a reactor in a loose spongy form; an XRD phase analysis result of the alloys is shown in embodiment 1; and an XRD phase analysis result of the distillation product is shown in
A method in an embodiment 3 is the same as the method in the embodiment 1, but differs from it in that 100 g of aluminum titanium alloy powder containing 1.86 wt % of titanium is used as reducing agent for production of TiAl3 alloys:
1. according to the produced product TiAl3 (x=3 in the formula (1)), the reaction formulas of the production proportion of all the materials are shown as follows:
3Na2TiF6+2NaF+13Al=3TiAl3+Na3AlF6+Na5Al3F14 (9)
and, Ti+3Al=TiAl3 (10);
according to the chemical reaction formulas (9) and (10), it can be obtained that 100 g of the reducing agent (titanium aluminum alloy powder) contains 1.86 g of Ti, namely the content of TiAl3 is 5 g, Al powder participating in the reduction reaction is 95 g, the content of Na2TiF6 required by the reaction is 168.89 g, and the mass of NaF required by the reaction is 22.74 g; therefore, the actual production materials of the embodiment 3 comprise 168.89 g of Na2TiF6, 22.74 g of NaF and 100 g of titanium aluminum alloy powder containing 1.86 wt % of titanium;
2. all the materials are heated to 1100° C. under the argon atmosphere condition, and the temperature is preserved for 2 h for first-stage aluminothermic reduction; and
3. distillation is performed for 2 h at the temperature of 1100° C.; after cooling, the residual metal in a reduction furnace is the TiAl3 alloys, and an XRD phase analysis result of the TiAl3 alloys is shown in
A method in an embodiment 4 is the same as the method in the embodiment 2 and differs from it in that 100 g of aluminum titanium alloy powder containing 1.86 wt % of titanium is used as reducing agent for production of TiAl3 alloys:
1. according to the produced product TiAl3 (x=3 in the formula (3)), the reaction formulas of the production proportion of all the materials are shown as follows:
12Na2TiF6+52Al=12TiAl3+3Na3AlF6+3Na5Al3F14+4AlF3 (11)
and, Ti+3Al=TiAl3 (12);
and therefore, it can be obtained that from the reaction equations (11) and (12) the actual production materials of the embodiment comprise 168.89 g of Na2TiF6 and 100 g of aluminum titanium alloy powder containing 1.86 wt % of titanium;
2. all the materials are heated to 1100° C. under the argon atmosphere condition, and the temperature is preserved for 2 h for the first-stage aluminothermic reduction; and
3. distillation is performed at the temperature of 1100° C. for 2 h; after cooling, the residual metal in a reduction furnace is the TiAl3 alloys, and an XRD phase analysis result of the TiAl3 alloys is the same as that in embodiment 3.
A method in an embodiment 5 is the same as the method in the embodiment 1 and differs from it in that 100 g of titanium aluminum alloy powder containing 3.2 wt % of titanium is used as reducing agent for production of TiAl alloys.
1. according to the produced product TiAl (x=1 in the formula (1)), the reaction formulas of the production proportion of all the materials are shown as follows:
3Na2TiF6+2NaF+7Al=3TiAl+Na3AlF6+Na5Al3F14 (13)
and, Ti+Al=TiAl (14);
according to the chemical reaction formulas (13) and (14), it can be obtained that 100 g of the reducing agent (aluminum titanium alloy powder) contains 3.2 g of Ti, namely the content of TiAl is 5 g, Al powder participating in the reduction reaction is 95 g, the content of Na2TiF6 required by the reaction is 313.65 g, and the content of NaF required is 42.22 g; therefore, the actual production materials of the embodiment 5 comprise 313.65 g of Na2TiF6, 42.22 g of NaF and 100 g of aluminum titanium alloy powder containing 3.2 wt % of titanium;
2. all the materials are heated to 1100° C. under the argon atmosphere condition, and the temperature is preserved for 2 h for first-stage aluminothermic reduction; and
3. distillation is performed at the temperature of 1100° C. for 2 h; after cooling, the residual metal in the reduction furnace is the TiAl alloys, and an XRD phase analysis result of the TiAl alloys is shown in
A method in an embodiment 6 is the same as the method in the embodiment 2 and differs from the embodiment 2 in that 100 g of aluminum titanium alloy powder containing 3.2 wt % of titanium is used as reducing agent for production of TiAl alloys.
1. according to the produced product TiAl(x=1 in the formula (3)), the reaction formulas of the production proportion of all the materials are shown as follows:
12Na2TiF6+28Al=12TiAl+3Na3AlF6+3Na5Al3F14+4AlF3 (15)
and, Ti+Al=TiAl (16);
and therefore, it can be obtained that from the reaction equations (15) and (16) the actual production materials of the embodiment comprise 313.65 g of Na2TiF6 and 100 g of the aluminum titanium alloy powder containing 3.2 wt % of titanium;
2. all the materials are heated to 1100° C. under the argon atmosphere condition, and the temperature is preserved for 2 h for first-stage aluminothermic reduction; and
3. distillation is performed at the temperature of 1100° C. for 2 h; after cooling, the residual metal in a reduction furnace is the TiAl alloys, and an XRD phase analysis result of the TiAl alloys is shown in embodiment 5.
A method in an embodiment 7 is the same as the method in the embodiment 1 and differs from the embodiment 1 in that 100 g of titanium aluminum alloy powder containing 3 wt % of titanium is used as reducing agent for production of pure titanium:
1. according to the produced product Ti (x=0 in the formula (1)), the reaction formulas of the production proportion of all the materials are shown as follows:
3Na2TiF6+2NaF+4Al=3Ti+Na3AlF6+Na5Al3F14 (17);
according to the chemical reaction formula (17), it can be obtained that 100 g of the reducing agent(aluminum titanium alloy powder contains 3 g of Ti), Al powder participating in the reduction reaction is 97 g, the content of Na2TiF6 required by the reaction is 560.44 g, and the content of NaF added is 75.44 g; therefore, the actual production materials of the embodiment 7 comprise 560.44 g of Na2TiF6, 75.44 g of NaF and 100 g of aluminum titanium alloy powder containing 3 wt % of titanium;
2. all the materials are heated to 1100° C. under the argon atmosphere condition, and the temperature is preserved for 2 h for first-stage aluminothermic reduction; and
3. distillation is performed at the temperature of 1100° C. for 2 h; after cooling, the residual metal in the reduction furnace is the Ti, and an XRD phase analysis result of the Ti is shown in
A method in an embodiment 8 is the same as the method in the embodiment 2 and differs from the embodiment 2 in that 100 g of aluminum titanium alloy powder containing 3 wt % of titanium is used as reducing agent for production of pure titanium:
1. according to the produced product Ti (x=0 in the formula (3)), the reaction formulas of the production proportion of all the materials are shown as follows:
12Na2TiF6+16Al=12Ti+3Na3AlF6+3Na5Al3F14+4AlF3 (18);
It can be obtained through the chemical reaction formula (18), the actual production materials of the embodiment comprise 560.44 g of Na2TiF6 and 100 g of the aluminum titanium alloy powder containing 3 wt % of titanium;
2. all the materials are heated to 1100° C. under the argon atmosphere condition, and the temperature is preserved for 2 h for first-stage aluminothermic reduction; and
3. distillation is performed at the temperature of 1100° C. for 2 h; after cooling, the residual metal in the reduction furnace is the metal Ti, and an XRD phase analysis result of the Ti is shown in embodiment 7.
A method in an embodiment 9 is the same as the method in the embodiment 1 and differs from the embodiment 1 in that 100 g of aluminum titanium alloy powder containing 2.13 wt % of titanium is used as reducing agent for production of titanium aluminum alloys containing 42.55% of titanium.
1. The titanium aluminum alloys containing 42.55 wt % of titanium are the same as the product TiAl2.4 alloys (x=2.4 in the formula (1)), and therefore, the reaction formulas of the production proportion of all the materials in the embodiment 9 are shown as follows:
3Na2TiF6+2NaF+11.2Al=3TiAl2.4+Na3AlF6+Na5Al3F14 (19)
And Ti+2.4Al=TiAl2.4 (20)
according to the chemical reaction formulas (19) and (20), it can be obtained that 100 g of the reducing agent (aluminum titanium alloy powder) contains 2.13 g of Ti, namely the content of TiAl2.4 is 5 g, Al powder participating in the reduction reaction is 95 g, the content of Na2TiF6 required by the reaction is 196.03 g, and the mass of NaF added is 26.39 g; therefore, the actual production materials of the embodiment 9 comprise 196.03 g of Na2TiF6, 26.39 g of NaF and 100 g of aluminum titanium alloy powder containing 2.13 wt % of titanium;
2. all the materials are heated to 1100° C. under the argon atmosphere condition, and the temperature is preserved for 2 h for first-stage aluminothermic reduction; and
3. distillation is performed for 2 h at the temperature of 1100° C.; after cooling, the residual metal in a reduction furnace is the TiAl2.4 alloys, and an chemical component analysis result of the TiAl2.4 alloys is shown in Table 1.
Titanium-free cryolite and aluminum titanium alloys are produced through vacuum reduction by using the titanium-containing cryolite distilled out through the first-stage aluminothermic reduction in the embodiment 7 as a raw material and aluminum powder as reducing agent.
1. after the first-stage aluminothermic reduction process, 427.78 g of the titanium-containing cryolite is grinded until the particle size is lower than 1.0 mm, wherein the content of titanium is 12.84 g; 100 g of aluminum powder is used as reducing agent; the grinded titanium-containing cryolite and the aluminum powder are uniformly mixed and then are pressed into lumps; the lumps are placed into the vacuum reduction furnace, the vacuum reduction furnace is vacuumized to 10 Pa or below, argon is inflated into the vacuum reduction furnace to normal pressure, the lumps are heated to 1200° C. under the argon atmosphere condition, and the temperature is preserved for 2 h for the second-stage aluminothermic reduction; and
2. after the materials in the reduction furnace are cooled to normal temperature, a product is taken out and separated out, so as to obtain the white titanium-free cryolite and the aluminum titanium alloys with the forming amounts of 414.94 g and 112.84 g respectively in theory; the aluminum titanium alloys can be used as reducing agent for the next first-stage aluminothermic reduction process to produce metal titanium, and the cycle continues; an XRD phase analysis result of the white titanium-free cryolite is shown in
It can be seen from Table 2 that the cryolite produced in the embodiment 10 completely conforms with the national standard GB/T 4291-1999 ‘cryolite’ and can be directly applied in the aluminum electrolysis industry. Low-titanium aluminum titanium alloys are formed at the upper layer of the aluminum titanium alloy product, and high-titanium aluminum titanium alloys are formed at the lower layer of the aluminum titanium alloy product. An SEM image and an energy spectrum analysis result of the aluminum titanium alloy product are respectively shown in
The titanium-containing cryolite obtained in the first-stage aluminothermic reduction of the embodiments 1-9 can be further treated by the method shown in the embodiment 10, the aluminum powder is adopted for performing the second-stage vacuum aluminothermic reduction, the obtained white titanium-free cryolite can be applied in the aluminum electrolysis industry, and the aluminum titanium alloys can fully returns to the next first-stage aluminothermic reduction process as the reducing agent.
| Number | Date | Country | Kind |
|---|---|---|---|
| 201510420032.1 | Jul 2015 | CN | national |
| Filing Document | Filing Date | Country | Kind |
|---|---|---|---|
| PCT/CN2015/089228 | 9/9/2015 | WO | 00 |
