CN215799202U - Device for producing fused magnesia by magnesite through microwave/electric arc heating - Google Patents
Device for producing fused magnesia by magnesite through microwave/electric arc heating Download PDFInfo
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- CN215799202U CN215799202U CN202122128636.2U CN202122128636U CN215799202U CN 215799202 U CN215799202 U CN 215799202U CN 202122128636 U CN202122128636 U CN 202122128636U CN 215799202 U CN215799202 U CN 215799202U
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Abstract
The utility model discloses a magnesite microwave/electric arc heating co-production fused magnesia device, which comprises a fused magnesia device body, wherein a feeding hole, a discharging hole, a material pusher, a base, a microwave layer, a first refractory beam, a microwave emitter, a heat insulating layer, a wave-transmitting layer, a wave-absorbing layer, a second refractory beam and a hearth are arranged in the fused magnesia device body; the feed inlet is arranged at the upper end of the fused magnesia device body, and the discharge outlet is arranged at the lower end of the fused magnesia device body; the microwave layer is arranged on the base, the material pushing device is arranged on the microwave layer, and a first fire-resistant beam is arranged on the material pushing device. According to the electric melting magnesia device, the microwave emitters on the two sides in the hearth are used for carrying out microwave calcination on magnesite, so that the porosity of the electric melting magnesia is effectively improved, and the porosity of the finally prepared magnesia crystal is 4% -10%.
Description
Technical Field
The utility model relates to the technical field of non-metallic ore sintering, in particular to a device for producing fused magnesia by magnesite through microwave/electric arc heating.
Background
The fused magnesia is a magnesia crystal with high temperature resistance, high hardness, high purity and high density formed by heating, decarbonizing (adopting magnesite), dehydrating (adopting brucite), melting, crystallizing, growing crystal, cooling and other physical and chemical change processes of a magnesia raw material. The fused magnesia is used as an important industrial raw material and widely applied to high-temperature electrical insulation materials, and is also an important raw material for manufacturing high-grade magnesia bricks, magnesia carbon bricks and unshaped refractory materials. In addition, the single crystal, polycrystal and high-purity fused magnesite is also used for manufacturing high-grade and ultrahigh-grade temperature-resistant, pressure-resistant and high-frequency-resistant insulating materials, thermocouple materials, electronic ceramic materials, rockets, nuclear melting furnaces and the like.
The main production raw material of the fused magnesite is magnesite, and the current production process comprises a one-step melting method and a two-step calcining melting method. The one-step melting method is formed by melting natural magnesite or purified magnesite concentrate powder serving as a raw material at high temperature in an electric arc furnace; the two-step calcining fusion method is that magnesite ore or purified magnesite concentrate powder is lightly burned in a vertical kiln or a rotary kiln to obtain light-burned magnesia powder, and then the light-burned magnesia powder is finely ground, pressed into a compact and finally fused in an electric arc furnace at high temperature to obtain the electrofused magnesia.
However, when the fused magnesite is produced by the current electric arc furnace in industrial scale, the obtained fused magnesite product has high porosity and small single crystal size. The porosity is a main factor determining the fire resistance and electrical performance of the fused magnesia, and the application of the fused magnesia in the fields of refractory materials, electrical materials and the like is limited by the high porosity.
Disclosure of Invention
The utility model provides a device for producing fused magnesia by magnesite through microwave/electric arc heating, which solves the problems of high porosity and small single crystal size of the fused magnesia produced by the traditional fused magnesia device.
In order to achieve the purpose, the technical scheme of the utility model is as follows:
the utility model provides a device of magnesite microwave/electric arc heating coproduction fused magnesia which characterized in that includes: the device comprises an electric melting magnesia device body, wherein a feeding hole, a discharging hole, a material pusher, a base, a microwave layer, a first fire-resistant beam, a microwave emitter, a heat insulation layer, a wave-transmitting layer, a wave-absorbing layer, a second fire-resistant beam and a hearth are arranged in the electric melting magnesia device body;
the feed inlet is arranged at the upper end of the fused magnesia device body, and the discharge outlet is arranged at the lower end of the fused magnesia device body;
the microwave layer is arranged on the base, the material pusher is arranged on the microwave layer, and the first fire-resistant beam is arranged on the material pusher;
the microwave emitter and the heat insulating layer are both arranged between the first fire-resistant beam and the second fire-resistant beam;
the wave-transparent layer and the wave-absorbing layer are arranged on the inner wall of the hearth.
Further, the microwave emitter penetrates through the wave absorbing layer and does not penetrate through the wave transmitting layer.
Further, the microwave emitters and the heat insulation layers are alternately arranged on two sides of the hearth.
Furthermore, the feed inlet is of an inverted trapezoidal structure.
Further, the discharge hole is of a wedge-shaped structure.
The utility model relates to a device for producing fused magnesia by magnesite through microwave/electric arc heating. Under the high-temperature action that is less than the melting point, through the mutual cohesive action and the material transfer between granule, micropore gas pocket reduces the rounding gradually and disappears, and granule system volume shrink, the crystalline grain increase, the density improves, and the porosity reduces to through using microwave sintering to carry out accurate accuse temperature to the light-burned pellet, make the inside and outside even that is heated of light-burned pellet, the shrink is even, is heated not the fracture pulverization. In addition, because micropore pores almost disappear in the process of lightly firing the pellets, when the magnesium oxide intermediate is sintered in an electric arc furnace, the changes of decarburization, dehydration and micropore migration are not involved, and only melting, crystallization and crystal growth are involved, so that the porosity of the fused magnesia can be effectively reduced, and the porosity of the finally prepared magnesium oxide crystal reaches 4-10%.
Drawings
In order to more clearly illustrate the embodiments of the present invention or the technical solutions in the prior art, the drawings needed to be used in the description of the embodiments or the prior art will be briefly introduced below, and it is obvious that the drawings in the following description are some embodiments of the present invention, and for those skilled in the art, other drawings can be obtained according to these drawings without creative efforts.
FIG. 1 is a schematic flow chart of an electrofused magnesite grain process of the present invention;
FIG. 2 is a schematic structural diagram of a microwave calcination apparatus according to the present invention.
In the figure, the device comprises a feed inlet 1, a feed inlet 2, a discharge outlet 3, a material pusher 4, a base 5, a microwave layer 6, a first fire-resistant beam 7, a microwave emitter 8, a heat insulation layer 9, a wave-transparent layer 10, a wave-absorbing layer 11, a second fire-resistant beam 12 and a hearth.
Detailed Description
In order to make the objects, technical solutions and advantages of the embodiments of the present invention clearer, the technical solutions in the embodiments of the present invention will be clearly and completely described below with reference to the drawings in the embodiments of the present invention, and it is obvious that the described embodiments are some, but not all, embodiments of the present invention. All other embodiments, which can be derived by a person skilled in the art from the embodiments given herein without making any creative effort, shall fall within the protection scope of the present invention.
Example 1:
as shown in fig. 1, a method for producing fused magnesia by magnesite through microwave/electric arc heating comprises the following specific operation steps:
s1, lightly burning the magnesite ore or purified magnesite concentrate powder in an electric arc furnace to obtain light-burned magnesia powder, controlling the temperature during light burning to be 1000 ℃, grinding the light-burned magnesia powder into powder through dry grinding, and compacting the powder to obtain light-burned pellets. Wherein, water is not needed to be added during dry grinding, and the water can react with the magnesium oxide to cause the magnesium oxide powder after light burning to go bad;
s2, calcining the light-burned pellets in a hearth 12 of a microwave calcining device shown in figure 2 to obtain a magnesium oxide intermediate, wherein the temperature during microwave calcining is 1600 ℃, the frequency is 915MHz, and the calcining time is 40 min;
s3, smelting the obtained magnesium oxide intermediate by using an electric magnesium melting furnace, wherein the temperature of the electric magnesium melting furnace is 2800 ℃, and thus obtaining an electric magnesium lump;
and S4, crushing, sorting, metering and crushing the smelted fused magnesia lump to obtain a fused magnesia finished product. The fused magnesia lump is crushed into fused magnesia finished products with different sizes according to actual requirements, the fused magnesia can be crushed to 0-400 meshes by a common Raymond mill, and the fused magnesia can be crushed to smaller particles by an airflow mill.
And (3) observing and analyzing the internal pore condition of the crushed fused magnesia finished product by adopting a CT detection technology, wherein the porosity of the fused magnesia finished product is calculated to be 10% by adopting the CT detection technology and matched software because the imaging gray levels of substances with different densities are different during CT scanning.
Example 2:
a method for producing fused magnesia by magnesite through microwave/electric arc heating comprises the following specific operation steps:
s1, lightly burning the magnesite ore or purified magnesite concentrate powder in an electric arc furnace to obtain light-burned magnesia powder, controlling the temperature during light burning to be 1000 ℃, grinding the light-burned magnesia powder into powder through dry grinding, and compacting the powder to obtain light-burned pellets. Wherein, water is not needed to be added during dry grinding, and the water can react with the magnesium oxide to cause the magnesium oxide powder after light burning to go bad;
s2, calcining the light-burned pellets in a hearth 12 of a microwave calcining device shown in figure 2 to obtain a magnesium oxide intermediate, wherein the temperature during microwave calcining is 1600 ℃, the frequency is 2500MHz, and the calcining time is 40 min;
s3, smelting the obtained magnesium oxide intermediate by using an electric magnesium melting furnace, wherein the temperature of the electric magnesium melting furnace is 2800 ℃, and thus obtaining an electric magnesium lump;
and S4, crushing, sorting, metering and crushing the smelted fused magnesia lump to obtain a fused magnesia finished product. The fused magnesia lump is crushed into fused magnesia finished products with different sizes according to actual requirements, the fused magnesia can be crushed to 0-400 meshes by a common Raymond mill, and the fused magnesia can be crushed to smaller particles by an airflow mill.
And (3) observing and analyzing the internal pore condition of the crushed fused magnesia finished product by adopting a CT detection technology, wherein the porosity of the fused magnesia finished product is calculated to be 8% by adopting the CT detection technology and matched software because the imaging gray levels of substances with different densities are different during CT scanning.
Example 3:
a method for producing fused magnesia by magnesite through microwave/electric arc heating comprises the following specific operation steps:
s1, lightly burning the magnesite ore or purified magnesite concentrate powder in an electric arc furnace to obtain light-burned magnesia powder, controlling the temperature during light burning to be 1000 ℃, grinding the light-burned magnesia powder into powder through dry grinding, and compacting the powder to obtain light-burned pellets. Wherein, water is not needed to be added during dry grinding, and the water can react with the magnesium oxide to cause the magnesium oxide powder after light burning to go bad;
s2, calcining the light-burned pellets in a hearth 12 of a microwave calcining device shown in figure 2 to obtain a magnesium oxide intermediate, wherein the temperature during microwave calcining is 1400 ℃, the frequency is 915MHz, and the calcining time is 40 min;
s3, smelting the obtained magnesium oxide intermediate by using an electric magnesium melting furnace, wherein the temperature of the electric magnesium melting furnace is 2800 ℃, and thus obtaining an electric magnesium lump;
and S4, crushing, sorting, metering and crushing the smelted fused magnesia lump to obtain a fused magnesia finished product. The fused magnesia lump is crushed into fused magnesia finished products with different sizes according to actual requirements, the fused magnesia can be crushed to 0-400 meshes by a common Raymond mill, and the fused magnesia can be crushed to smaller particles by an airflow mill.
And (3) observing and analyzing the internal pore condition of the crushed fused magnesia finished product by adopting a CT detection technology, wherein the porosity of the fused magnesia finished product is calculated to be 4% by adopting the CT detection technology and matched software because the imaging gray levels of substances with different densities are different during CT scanning.
As shown in fig. 2, the apparatus for producing fused magnesite by magnesite microwave/electric arc heating comprises: the device comprises an electric melting magnesia device body, wherein a feed inlet 1, a discharge outlet 2, a material pusher 3, a base 4, a microwave layer 5, a first refractory beam 6, a microwave emitter 7, a heat insulation layer 8, a wave-transmitting layer 9, a wave-absorbing layer 10, a second refractory beam 11 and a hearth 12 are arranged in the electric melting magnesia device body; preferably, the feed port 1 is made of a wave-resistant material, a microwave layer 5 and a base 4 are arranged below the discharge port 2, and the microwave layer 5 is made of a wave-resistant material and used for blocking microwaves of fused magnesia when the discharge port 2 discharges materials; the base 4 is made of refractory materials.
The feed inlet 1 is arranged at the upper end of the fused magnesia device body, and the discharge outlet 2 is arranged at the lower end of the fused magnesia device body;
the microwave layer 5 is arranged on the base 4, the pusher 3 is arranged on the microwave layer 5, and the first fire-resistant beam 6 is arranged on the pusher 3;
the microwave launcher 7 and the heat insulating layer 8 are both arranged between the first fire-resistant beam 6 and the second fire-resistant beam 11;
the wave-transparent layer 9 and the wave-absorbing layer 10 are arranged on the inner wall of the hearth 12.
Further, the microwave emitter 7 penetrates through the wave-absorbing layer 10 and does not penetrate through the wave-transparent layer 9. Preferably, the wave-transmitting layer 9 is made of a wear-resistant wave-transmitting material, and when the irregularities on the surfaces of the light-burned pellets are calcined in the microwave hearth 12, the wear-resistant wave-transmitting material is adopted, so that the service time of the light-burned pellets is prolonged on one hand, and the microwave of the microwave emitter 7 can penetrate through the light-burned pellets in the hearth 12 to be calcined in the microwave on the other hand. In addition, the wave-absorbing layer 10 can absorb redundant microwaves, so that the microwaves can uniformly radiate the light-burned pellets, and the porosity in the pellets is reduced.
Further, the microwave emitters 7 and the heat insulating layers 8 are alternately arranged on two sides of the hearth 12.
Further, the feed inlet 1 is of an inverted trapezoidal structure. Preferably, the feeding hole 1 is in an inverted trapezoid shape, so that the light-burned pellets are conveniently added.
Further, the discharge port 2 is in a wedge-shaped structure. Preferably, the discharge port 2 is arranged to be in a wedge-shaped structure, so that the magnesium oxide intermediate can gradually fall under the action of gravity instead of directly sliding out during discharging, and if the magnesium oxide intermediate directly slides out, the magnesium oxide intermediate is easy to collide with each other under the action of gravity to rub and damage, so that the calcined surface of the magnesium oxide intermediate is damaged.
The method for producing the fused magnesia by using the magnesite through microwave/electric arc heating comprises the following steps of firstly, according to the process flow for producing the fused magnesia, lightly burning the fused magnesia in an electric arc furnace at the temperature of 1000 ℃ to obtain lightly burned magnesia, and then, grinding the lightly burned magnesia, carrying out dry grinding without adding water, and compacting the ground lightly burned magnesia to obtain lightly burned pellets; the lightly calcined pellet is calcined in a microwave calcining device as shown in figure 2 by microwave, and the lightly calcined pellet is calcined in the temperature range of 1400 ℃ to 1600 ℃. Due to the temperature lower than the melting point, the micro particles are bonded with each other to generate mass transfer. Along with the reduction of the center distance among the particles during sintering, the generation of sintering necks through contact and continuous growth, the particle system shrinks, the micropore pores gradually shrink and round until disappear, and the obtained magnesium oxide is a magnesium oxide intermediate completely converted from amorphous to magnesium oxide crystals. And then smelting a magnesium oxide intermediate by using an electric smelting magnesia furnace, wherein the temperature of the electric smelting magnesia furnace is more than or equal to 2800 ℃ to obtain an electric smelting magnesia lump, cooling the smelted electric smelting magnesia lump, crushing, sorting, metering and crushing to obtain an electric smelting magnesia finished product with low porosity, observing and analyzing the internal pore condition of the electric smelting magnesia finished product obtained after crushing by adopting a CT detection technology, and calculating by adopting the CT detection technology and matched software to obtain the finished product with the porosity of 4-10% compared with the porosity of the electric smelting magnesia finished product prepared by the traditional technology because substances with different densities have different imaging gray levels during CT scanning, wherein the porosity of the electric smelting magnesia finished product is reduced by 50-60%.
The traditional electric furnace smelting technology for producing the fused magnesia by an electric arc furnace on an industrial scale adopts the raw material as a furnace lining, the magnesium raw material is converted into a magnesium oxide amorphous body at 640-800 ℃, and the magnesium oxide amorphous body is a CO amorphous body2The large amount of the magnesium oxide escapes to form a developed porous product which is MgCO3Hard agglomerates of crystalline structure; converting the magnesium oxide amorphous body into a magnesium oxide crystal at 800-1700 ℃, wherein the magnesium oxide crystal gradually tends to be perfect and is polymerized to form a dense fine crystal, sintering and crystallization phenomena occur, and the crystal structure becomes dense; converting the magnesium oxide crystal into magnesium oxide liquid at the temperature of 2800 ℃; cooling and recrystallizing to obtain compact electric melting magnesia crystal, namely electric melting magnesia. After the melting is started, the impurities with lower melting points reach the melting point temperature firstly along with the rise of the temperature, the impurities are converted into liquid, and the impurities containing Si, Al, Fe, Ca and the like begin to gather on a solid-liquid interface and gradually migrate outwards. The temperature continues to rise, and when the melting point temperature of the magnesium oxide is reached, the magnesium oxide begins to melt, and the density of the magnesium oxide is relatively high, and the density of other impurities is relatively low, so that the impurities gradually migrate upwards. Wherein the impurities with low melting point can be directly sublimated into gas to escape from the molten pool, so that the content of magnesium oxide in the molten pool is higher and higher. As the temperature is slightly reduced, the magnesium oxide crystals begin to crystallize out, and at the moment, the system temperature is still higher than the melting point temperature of the impurities, and the impurities are still in a liquid state. Due to the influence of capillary action, temperature and concentration gradient, impurities gradually migrate or precipitate outwards and upwards and finally fall on the crystal boundary of the fused magnesia, and the magnesium oxide crystal is obtained after the impurities are discharged.
In the process of producing fused magnesia by magnesite through microwave/electric arc heatingThe magnesium ore and the magnesite concentrate powder are subjected to light burning at 1000 ℃, and CO is added2The large amount of the catalyst is escaped to form a developed porous structure of the product, and MgCO is maintained3The light-burned magnesia powder with the crystal structure and the hard aggregate characteristic has small grain size and large porosity. The light-burned magnesia powder is ground into powder and pressed into compact to obtain light-burned pellets, the light-burned pellets are transferred to microwave calcining equipment, and the light-burned pellets are calcined within the temperature range of 1400 ℃ and 1600 ℃. Due to the temperature lower than the melting point, the micro particles are bonded with each other to generate mass transfer. Along with the reduction of the center distance among the particles during sintering, the generation of sintering necks through contact and continuous growth, the particle system shrinks, the micropore pores gradually shrink and round until disappear, and the obtained magnesium oxide is a magnesium oxide intermediate completely converted from amorphous to magnesium oxide crystals. And smelting the magnesium oxide intermediate by using an electric smelting magnesia furnace, wherein the temperature of the electric smelting magnesia furnace is more than or equal to 2800 ℃ to obtain an electric smelting magnesia lump, and cooling the smelted electric smelting magnesia lump, crushing, sorting, metering and crushing to obtain an electric smelting magnesia finished product with low porosity, wherein the porosity of the obtained electric smelting magnesia finished product is 4-10%, and is reduced by 50-60% compared with the porosity of the electric smelting magnesia finished product prepared by the traditional technology.
Finally, it should be noted that: the above embodiments are only used to illustrate the technical solution of the present invention, and not to limit the same; while the utility model has been described in detail and with reference to the foregoing embodiments, it will be understood by those skilled in the art that: the technical solutions described in the foregoing embodiments may still be modified, or some or all of the technical features may be equivalently replaced; and the modifications or the substitutions do not make the essence of the corresponding technical solutions depart from the scope of the technical solutions of the embodiments of the present invention.
Claims (5)
1. The utility model provides a device of magnesite microwave/electric arc heating coproduction fused magnesia which characterized in that includes: the device comprises an electric melting magnesia device body, wherein a feeding hole (1), a discharging hole (2), a material pushing device (3), a base (4), a microwave layer (5), a first refractory beam (6), a microwave emitter (7), a heat insulating layer (8), a wave-transparent layer (9), a wave-absorbing layer (10), a second refractory beam (11) and a hearth (12) are arranged in the electric melting magnesia device body;
the feed inlet (1) is arranged at the upper end of the fused magnesia device body, and the discharge outlet (2) is arranged at the lower end of the fused magnesia device body;
the microwave layer (5) is arranged on the base (4), the material pushing device (3) is arranged on the microwave layer (5), and the first fire-resistant beam (6) is arranged on the material pushing device (3);
the microwave emitter (7) and the heat insulating layer (8) are both arranged between the first refractory beam (6) and the second refractory beam (11);
the wave-transparent layer (9) and the wave-absorbing layer (10) are arranged on the inner wall of the hearth (12).
2. A magnesite microwave/arc heating co-production apparatus as claimed in claim 1, characterised in that the microwave emitter (7) passes through the wave-absorbing layer (10) and does not pass through the wave-transparent layer (9).
3. A magnesite microwave/arc heating co-production apparatus as claimed in claim 1, characterised in that the microwave emitters (7) and the heat insulating layers (8) are alternately arranged on both sides of the furnace (12).
4. The magnesite microwave/arc heating co-production fused magnesia device as claimed in claim 1, wherein the feed inlet (1) is of an inverted trapezoidal structure.
5. The magnesite microwave/arc heating co-production fused magnesia device according to claim 1, wherein the discharge port (2) is in a wedge-shaped structure.
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| Publication number | Priority date | Publication date | Assignee | Title |
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| CN113548874A (en) * | 2021-09-03 | 2021-10-26 | 辽宁荣邦科技有限公司 | Method and device for producing fused magnesia by magnesite through microwave/electric arc heating |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
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| CN113548874A (en) * | 2021-09-03 | 2021-10-26 | 辽宁荣邦科技有限公司 | Method and device for producing fused magnesia by magnesite through microwave/electric arc heating |
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