Patent Grant
9617620
The present invention relates to a method for reducing alumina (aluminum oxide) or magnesia (magnesium oxide) by utilizing supersonic gas flow for isolating aluminum or magnesium.
Aluminum is a widely used metal for industrial products such as construction materials because of its light weight, easy processing characteristics, and high corrosion resistance owing to protection made by oxide film surrounding its surface. From processing view point, a variety of processing, such as stamping, extruding, or casting may be applied, and from alloying view point, duralumin is well known as an example. Further, it is also used in other technological fields by making use of its excellent heat conductivity or electricity conductivity. Aluminum is also a metal having potential to be used as energy source in the future, since it generates high energy when combusted, and its energy density per volume is comparable with even coal or petroleum (41.9 kJ/cm3).
From historical view point, its origin is discovery of alumina in early 19th Century, and it had been considered as precious metal until technique for isolating aluminum from alumina was established, but its availability is improved after the Hall-Heroult process was found at the end of 19th century. Detailed explanation of the Hall-Heroult process is omitted here since it is widely used today as a method for refining aluminum, but in brief, an ore called bauxite containing high percentage of alumina is melt with sodium hydroxide and extracting alumina out of it (Bayer process), the alumina is then melt in electrolytic bath (1300K) using cryolite (Ga3AlF6), and thereafter aluminum is refined by electrolysis using carbon electrodes. Carbon electrode used as anode acts as reducing agent, which combines with oxygen contained in alumina and generates carbon dioxide and carbon monoxide (1100K or more).
Al2O3+3C→2Al+3CO
Al2O3+3/2C→2Al+3/2CO2
Although the Hall-Heroult process is used as a major method even today for dissociating alumina, the method has problems that it consumes a large amount of electric power for dissociating alumina (electric power consumed for 1 ton of aluminum: 13,000-14,000 kWh), and further it emits a large volume of greenhouse effect gas such as CO or CO2 as shown in the above formulas. Especially, the latter problem has direct influence on warming up of the earth, hence it is a big issue on global scale to develop alternative methods for reducing alumina.
Some technological developments of the Hall-Heroult process are underway for improving its energy efficiency (for example, refer to “patent document 1”), or some alternative reducing methods that may replace the Hall-Heroult process (for example, refer to “patent document 2” and “patent document 3”) are proposed, but these counter measures would not fundamentally resolve the above mentioned problems, therefore there still remains need for drastic improvement in the method for reducing alumina.
On the other hand, magnesium is even lighter in weight compared to aluminum, and easy for processing, therefore it is a widely used metal as industrial material in the field of such as automobile, aerospace, or machinery equipment, and it is also used as an additive for improving mechanical characteristics of a variety of materials. From processing view point, extruding, stamping, forging etc. may be applied, therefore it may cover a wide range of industrial application. Although it tends to be corroded due to its relatively high chemical activity, it is possible to make it in stable condition by applying surface treatment. It is also known that it generates a large amount of energy when it is combusted (601.7 kJ/mol).
Historically, commercial production of magnesium was started in late 19th century, almost the same timing as aluminum, but timing of wide use of it became somewhat belated due to difficulty of its refining process. Thermal reduction method and electrolytic method are known today as methods for refining magnesium. In the former method, which is a major method today, magnesia obtained by burning dolomite ore is reduced by adding reducing agent and heating it at high temperature under low pressure (known as the Pidgeon process).
2MgO+Si→SiO2+2Mg
In the latter process, magnesium is obtained by electrolyzing mercuric magnesium gained mainly from sea water (known as electrolysis refining process).
MgCl2→Mg+Cl2
However, since both of these processes are the same in a sense that a large amount of electric power needs to be consumed, a novel method for refining magnesium with low energy consumption is also required.
Based on the above description, the purpose of the present invention is to provide a method for reducing alumina or magnesia that would not emit greenhouse effect gas and improve energy efficiency, by resolving the above mentioned problems in connection with the Hall-Heroult process for aluminum, and by resolving the above mentioned problems in connection with the Pidgeon process which is a major refining method for magnesium
The present invention resolves the above-described problems by thermally dissociating aluminum or magnesium from oxygen by heating alumina or magnesia by using heating means such as laser beam and putting them into plasma state, and preventing them from re-combining to each other by making the gas in plasma state into supersonic gas flow. More specifically, the present invention includes the following.
That is, one aspect of the present invention is directed to a method for reducing alumina or magnesia, wherein the method includes a step of heating alumina powders or magnesia powders by heating means thereby putting it in a plasma state and thermally dissociating aluminum or magnesium from oxygen, and a step of ejecting the gas in the plasma state in a form of supersonic jet steam from a nozzle so as to make it in frozen flow, thereby isolating aluminum or magnesium.
For isolating aluminum and magnesium in the above mentioned aspect, the method can be structured in such a manner that alumina powders or magnesia powders are fed into a reducing device together with carrier gas at upstream of a throat portion provided to the reducing device, operating gas is introduced similarly at upstream of the throat portion, gas pressure of which forcedly transport the fed powders toward the throat portion, and heating means heats the throat portion, thereby dissociating alumina or magnesia, which is then ejected in a form of supersonic jet gas stream from the nozzle located at downstream of the throat portion.
In the above mentioned aspect, hydrogen can be further added to the operating gas. Such addition would promote reducing of alumina or magnesia by action of the added hydrogen.
In the above mentioned aspect, the method may further includes a step of controlling volume of alumina powders or magnesia powders to be fed at upstream of the throat portion. Also, the method can further includes a step of guiding isolated aluminum or magnesium into a cooling tube so as to deposit aluminum or magnesium inside of the cooling tube and collect the same.
Implementation of the present invention makes it possible to perform reduction of alumina or magnesia without emitting greenhouse effect gas or other harmful gas, and reducing electric power consumption in comparison with the prior art Hall-Heroult process or Pidgeon process.
The first embodiment of the method for reducing alumina or magnesia by using laser according to the present invention is now be described by referring to appended drawings. Although illustration in drawings and the following explanation are directed to a method for reducing alumina as a representing example, the devices and processes used hereinafter are basically applicable to reducing magnesia in a similar manner, except difference of base materials to be used between alumina powders and magnesia powders.
First, at the step of thermally dissociating alumina shown in area A on left hand side of the drawing, a throat portion 111 is provided in inside of a reducing device 100 used in the present embodiment for throttling the flow flowing through it, and an alumina feeding gate 112 is provided at upstream thereof (left hand side of the drawing), and an operating gas introducing gate 113 is also provided on even far upstream side. Alumina powders are fed into inside of the device from the alumina feeding gate 112 together with carrier gas such as argon, and pressurized operating gas comprising oxygen and inert gas such as argon is introduced from the operating gas introducing gate 113. Mixing ratio between alumina and carrier gas to be fed from the alumina feeding gate 112 is properly controlled in such a manner that alumina content is in a range of, for example, about 0.1-0.6 g/l (l: little). Further, pressure of the operating gas to be introduced from the operating gas introducing gate 113 is desirably about 10 atm. Mixture of alumina and carrier gas is forcedly transported by operating gas pressure from left hand side to right hand side of the drawing toward the throat portion 111.
In the throat portion 111, a laser beam 114 is irradiated from right hand side of the drawing focusing on the throat portion 111. In the present embodiment, carbon dioxide gas laser having 34 mm beam diameter, maximum output of 2 kW, and wave length of 10.6 μm is used, but such specification of laser beam 114 may be changed as far as it has enough energy sufficient to put alumina into plasma state. Temperature at the vicinity of focal point of the laser beam becomes as high as 12,000K locally, and alumina is melt due to such high temperature heat (melting point of alumina is 2,300K, and that of magnesia is 3,070K), and is put in plasma state thereby it is thermally dissociated into aluminum and oxygen. At this stage, a phenomena so called inverse bremsstrahlung radiation is generated in which atom is accelerated through absorbing beamed laser power, and plasma is heated by repeated coulomb collision among atoms and ions.
Al2O3=2Al+3/2O2−838 kJ
Operation is then moved to area B located in the center of the drawing, in which gas in plasma state, expanded by heating and throttled at throat portion 111, is ejected in a form of jet stream from the nozzle 116 which is an exit of the throat portion 111 toward right hand side of the drawing. Gas flow at this stage becomes supersonic flow such as 1,000-3,000 m/s in speed, and the gas flow is instantly cooled due to rapid expansion. In case of the prior art Hall-Heroult process, among electrolyzed alumina elements, oxygen is separated by being drawn by anode and combines with carbon, thereby being isolated in a form of carbon monoxide or carbon dioxide, and only remaining element, aluminum, is deposited in the electrolytic bath and collected. However, in case of no reducing agent such as carbon electrode is provided, even if alumina is once thermally dissociated into aluminum and oxygen, aluminum and oxygen having strong combining force tend to re-combine to each other and return to alumina during cooling process. On the other hand, according to the present embodiment, since separated aluminum and oxygen in plasma state are rapidly cooled in frozen supersonic gas flow down to normal temperature, re-combination of aluminum and oxygen is prevented and their separated condition can be maintained. Such fact can be confirmed by emission light spectrum measurement in which peaks of emission light spectrum unique to aluminum are observed.
Thereafter, the flow moves to area C on right hand side of the drawing, and only isolated aluminum is recovered. In the example shown in the drawing, a cooled copper tube 117 is provided into which the flow is guided and separated oxygen in gaseous state is discharged while aluminum is accumulated on inner wall of the copper tube 117 and collected. Such method for recovering is just an example, and some other methods may be adopted, such as using a filter device capable of selectively permeating oxygen and capturing aluminum powders.
As explained above, it is desirable to properly control content of alumina powders in the mixture of introduced alumina powders and carrier gas.
Turntable 11 is rotated by a motor 17, and its rotational speed may be controlled by a controller not shown in the drawing. Proper volume of alumina powders 5 are released in a timely manner from the releasing tube 13 into the alumina container 12. By providing a sensor (not shown in the drawing) to tip of the releasing tube 13 for detecting level of alumina powders in the alumina container 12, it is possible to release proper volume of alumina powders 5 so as to maintain height level of the powders constant. Alumina powders may be replenished once in a while to the releasing tube 13. In the present embodiment, alumina powders having diameter of about 0.03 to 3 μm may be used, but it is desirable to select and use alumina powders having almost the same diameter for one batch treatment so as to stably control feeding volume rate of alumina powders. The alumina feeding tube 14 and the carrier gas supplying tube 16 are formed in a double-tube structure, and carrier gas such as argon or helium may be supplied downwardly from upper side through the carrier gas supplying tube 16 located at outer side of the double-tube structure. Since height of the double tube structure is adjusted at a level just establishing contact with alumina powders 5 in the alumina container 12, the aluminum powders 5 are mixed with the carrier gas due to pressure of the carrier gas, and the mixed carrier gas containing the alumina powders 5 is then forcedly pushed into inside of the alumina feeding tube 14 in upward direction from lower end, and further it is supplied to the alumina feeding gate 112 shown in
Actions of the alumina feeding device 10 as structure above are: first, alumina powders 5 are released into the alumina container 12 from the alumina releasing tube 13, and then the turntable 11 is rotated by the motor 17. Next, carrier gas is supplied from upper side of the carrier gas supplying tube 16, alumina powders 5 are dragged in by the carrier gas at lower end of the double-tube and forcedly pushed into the alumina feeding tube 14, and the mixed gas is then supplied to alumina feeding gate 112 of the alumina reducing device 100 shown in
Next, the second embodiment of the method for reducing alumina (or could be magnesia) according to the present invention is now be described. The method for reducing alumina according to the present embodiment is basically similar to the former embodiment explained by referring to
Al2O3+3H=2Al+3H2O−112 kJ
By making use of hydrogen as a reducing agent as described above, alumina reduction may be achieved by using even fewer energy. In
In the examples of the above mentioned embodiments, laser beam is used as heating means for reducing alumina in thermal dissociation process instead of electrolysis in prior art, but the present invention is not limited thereto, but some other heating means may be utilized. Some examples are: arc discharge or inductively-coupled plasma. However, in case of using arc discharge, electrodes (tungsten or cupper) are consumed, and operation in oxygen environment is prohibited. In case of using conductively-coupled plasma, operating pressure is limited to less than 1 atm, and also it has a problem of interference with generated aluminum. By the laser plasma means according to the present embodiment, operation in oxygen atmosphere is possible since no consuming material such as electrode exists, and operating pressure can be kept at high level (about up to 10 atm), therefore the method according to the present invention is more suitable for realizing frozen supersonic flow.
The method for reducing alumina according to embodiment 1 is conducted under the following assumption:
The result is shown in
The method for reducing alumina or magnesia according to the present invention may be used in industrial fields such as field of reducing alumina for producing aluminum, or field of reducing magnesia for producing magnesium.
| Number | Date | Country | Kind |
|---|---|---|---|
| 2012-183356 | Aug 2012 | JP | national |
| Filing Document | Filing Date | Country | Kind |
|---|---|---|---|
| PCT/JP2013/056417 | 3/8/2013 | WO | 00 |
| Publishing Document | Publishing Date | Country | Kind |
|---|---|---|---|
| WO2014/030369 | 2/27/2014 | WO | A |
| Number | Date | Country |
|---|---|---|
| 2011032131 | Feb 2011 | JP |
| Entry |
|---|
| Arakawa,Yoshihiro et al. “Research and Development of an Energy Cycle System Using Aluminum.” Journal of IAPS 20(1) 2012. pp. 3-7. Human translation. |
| Nakamura et al. JP 2011032131 A published Feb. 2011. Machine translation. |
| Number | Date | Country | |
|---|---|---|---|
| 20150203937 A1 | Jul 2015 | US |
