JP2008000687A - Method for sorting fireproof raw material - Google Patents

Abstract

<P>PROBLEM TO BE SOLVED: To provide a method for sorting fireproof raw material in every purity accurately and efficiently. <P>SOLUTION: Fireproof raw material is sorted into grades according to purity by a color sorting machine comprising a belt conveyer 2 transferring fireproof raw material particles 1 with the purity of 90 mass% or more and a particle size of 20 mm or less and discharging to air from a transfer end part; fluorescent lamps 3 irradiating the discharged fireproof raw material particles 1 with light from upper and lower sides; a CCD camera 4 detecting reflection light from the fireproof raw material particles 1 and transmitting light; an air jetting nozzle 5 jetting an air by a given threshold of the detected light; and a sorting vessel 6 containing particles sorted by the jetted air. <P>COPYRIGHT: (C)2008,JPO&INPIT

Description

  The present invention relates to a method for sorting refractory raw materials based on purity.

In the present invention, the purity of the refractory raw material means the content ratio by mass% of the main chemical components constituting the refractory. For example, if the magnesia raw material constituting the refractory is an electrofused magnesia clinker, it means the content ratio of MgO in the clinker, and if the zirconia raw material is an electrofused zirconia clinker, ZrO ₂ in the clinker and The total content of CaO, Y ₂ O ₃ , or MgO stabilizing material means the content of the total content of Al ₂ O ₃ and MgO in the clinker in the case of an electrofused spinel clinker. To do.

  Alumina, magnesia, silica, mullite, silicon carbide, etc. are used as refractory raw materials for the production of refractory nozzles used for lining and refining of various furnaces for iron and steel, non-ferrous metals, cement ceramic furnaces, incinerators, etc. It is done.

  For example, magnesia carbon brick is generally used as a refractory for a steelmaking furnace, and an electrofused magnesia clinker is mainly used as a magnesia raw material as a refractory raw material for that purpose. It is said that the higher the purity of this electrofused magnesia clinker, the better the magnesia carbon brick that can be obtained. On the other hand, in the case of a magnesia fired brick used as a permanent brick used at a location in contact with the furnace wall of a steelmaking furnace, a material having a very high purity is not required.

  Thus, the refractory raw material is divided according to the required purity for each application, as seen in the example of the electrofused magnesia clinker.

  The electrofused magnesia clinker is manufactured by an electrofusion method in which magnesia clinker obtained from natural magnesite or seawater is melted in an electric furnace. For example, Patent Document 1 discloses that magnesia clinker is a raw material magnesia having a purity of 99.8% by mass or more. In addition, it is described that high-purity and high-quality single crystal magnesia is obtained by embedding electrodes and electromelting.

  Further, in Patent Document 2, magnesia clinker obtained from seawater is melted in a cylindrical electric furnace, and after cooling, a cylindrical ingot is taken out, and an unmelted part and a semi-melted part of the ingot are separated, It is described that the fused magnesia purity can be increased to 95 mass% or more by coarsely pulverizing a portion melted and crystallized at the center of the material into a lump of 50 to 100 mm and selecting according to the crystal size. Yes.

  However, in this method, since the sorting is a large block of 50 to 100 mm and human judgment, there is a limit to the accuracy of sorting, and it is difficult to obtain a high-purity electrofused magnesia clinker. .

  For this reason, in order to obtain a high-purity electrofused magnesia clinker, there is only a method of using an expensive raw material that has been purified to a high purity in advance as in Patent Document 1, and the obtained method is very laborious. Therefore, the obtained refractory raw material becomes expensive and can be used only for limited applications.

  Therefore, in order to make a high-purity electrofused magnesia clinker as a practical refractory material, it is preferable to rely on an improvement in sorting accuracy rather than increasing the purity of the starting material in advance.

  Although it is not a refractory raw material, as a means for selecting impurities in granular materials such as soybeans, rice, and resin pellets, for example, in Patent Document 3, a granular material is dropped with a certain fall trajectory, and each falling granular material is irradiated. Irradiate light to compare the transmitted light quantity and reflected light quantity of each granular object with a predetermined threshold value to determine a granular object having a different color part to discriminate between a non-defective product and a defective product, and a signal is sent to the ejection delay control means A method is disclosed in which a blast means is operated at a predetermined delay time and a defective product is selected and removed by this blast.

In addition, as an example of using color sorting for sorting refractories, Patent Document 4 classifies the presence or absence of a slag infiltrated layer using a color sorter when sorting the presence or absence of slag infiltration in a used refractory. It is described.
JP-A-5-170430 JP-A-8-183653 JP 2000-197855 A JP 2003-88845 A

  The present invention provides a method for sorting refractory raw materials according to purity with high accuracy and efficiency.

  As a result of various studies under the assumption that there is a correlation between the purity and color of the refractory raw material, in the case of a refractory raw material having a relatively high purity, there is a correlation between the purity and the color. I found out that As a result, when sorting using a color sorter, we found that it was possible to sort into multiple groups depending on its purity, and that higher quality refractory raw materials could be obtained.

  That is, the present invention is a method for selecting a refractory raw material, characterized in that particles of the refractory raw material having a purity of 90% by mass or more and a particle size of 20 mm or less are selected by grade according to the purity by color selection.

  The refractory raw material particles may be crushed after roughly sorting the refractory raw material ingot taken out of the electric furnace.

  The color referred to in the present invention means a color feeling in which hue, lightness, and transparency are combined, and a commercially available color sorter can be used for the detection.

  In color selection, the refractory raw material particles are transferred by a transfer means and discharged from the transfer end portion into the air. The emitted refractory raw material particles are irradiated with light, and the irradiated light is detected by an optical discriminating means. This can be performed by a color sorter that sorts the jet flow according to the threshold value against the refractory raw material particles. Optical discriminating means such as a CCD camera, phototransistor, solar cell, etc., detection light as reflected light and / or transmitted light, and threshold values as hue, brightness, saturation, reflected light quantity, and / or Or it is more preferable that it is a color sorter which can set the amount of transmitted light. This type of color sorter can be used with high efficiency for sorting refractory materials.

  In order to color-select the particles of the refractory raw material with high accuracy, the purity of the raw material to be selected is preferably 90% by mass or more, more preferably 95% by mass or more. When the purity is less than 90% by mass, the correlation between the purity and the color is low, and the accuracy of sorting is inferior.

  As the purity of 90% by mass or more, a value obtained by sampling a refractory raw material to be selected and measuring a chemical component can be used. By color-selecting the refractory raw material particles under these conditions, the refractory raw material particles are clearly sorted into a plurality of groups according to purity, and as a result, a high-purity refractory raw material can be obtained efficiently.

  If the refractory raw material for sorting is obtained by the electromelting method, the difference in chemical composition is large depending on the mass of the electromelted material. And For example, the purity of electrofused magnesia is defined as the purity of magnesite before being put into an electric furnace or the loss of ignition loss (igloss) of seawater magnesia clinker.

  Moreover, the precision of color selection can be made high by grind | pulverizing the particle size of the refractory raw material selected to 20 mm or less, Preferably it is 10 mm or less. When the particle size exceeds 20 mm, the accuracy of sorting by color sorting becomes insufficient.

  In order to color-select the particles of the refractory raw material according to the present invention, the particle size is adjusted in advance to be 20 mm or less. This is because, after pulverizing the refractory raw material, the sieve opening is 20 mm or less. By letting it pass, the particle size can be made 20 mm or less. For example, a refractory raw material that has passed through a sieve having a sieve opening of 10 mm can also be used. However, the smaller the portion of fine powder having a particle size of 0.2 mm or less, the better the sorting accuracy. For this purpose, it is desirable to use a refractory raw material that has been sized so that its proportion is 10% by mass or less. In the refractory raw material, the accuracy of sorting is improved as the particle size range is narrow, but it is difficult to obtain a refractory raw material with a narrow particle size range in a high yield by the current pulverization technique. Therefore, if the upper limit of the particle size is 20 mm or less, it can be selected with sufficient accuracy and at low cost. However, if necessary, the upper limit of the particle size is 10 mm or less, further 5 mm or less, and the lower limit of the particle size is 0.2% or less. By making it below, it is possible to sort with higher accuracy by narrowing the range of particle size.

  Specifically, after roughly selecting the crushed grains of the ingot taken out from the electric furnace, it is further pulverized so that the particle size is 20 mm or less, and if necessary, the particle size is 0.2 mm or less to 10 mass% or less. The particle size ratio is adjusted, and the particle size adjusted refractory raw material particles are sorted by grade according to the purity by a color sorter.

  The ingot taken out after being melted and cooled in an electric furnace produces a large crystal immediately inside the unmelted part on the outer peripheral side, gradually becomes a small crystal toward the center, and finally the center part solidified contains impurities. The ingot becomes a non-uniform structure as an accumulated part. Therefore, the larger the crystal diameter, the higher the purity because the proportion of grain boundaries containing impurities decreases.

  As described above, since the regions having different crystal diameters are layered in the radial direction in the ingot, it is very difficult to separate a portion having a desired crystal diameter from other portions with high accuracy. On the other hand, raw material particles obtained by pulverizing an ingot to a particle size of 20 mm or less have a higher correlation between purity and color, and therefore can be sorted with high accuracy by using a color sorter.

  As a refractory raw material applicable to the present invention, a synthetic refractory raw material such as a sintered refractory raw material or an electrofused refractory raw material can be used even if it is a natural refractory raw material. More preferably, it is an electromelting refractory raw material. In the case of magnesia, the electrofused refractory material has higher transparency as the crystal grain size is larger. Therefore, the crystal size can be divided into groups by color selection including transparency. For this reason, it is possible to sort grains by crystal size, that is, by purity, with considerably high accuracy. Other electromelting refractory materials include alumina, spinel, mullite, zirconia, alumina zirconia, magnesia, calcia and the like.

  By performing color selection, refractory raw materials can be automatically classified according to grade according to their purity, so that high-purity refractory raw materials can be obtained at low cost. And by using the refractory raw material classified by grade most suitable for a use, a high quality refractory can be obtained efficiently.

  Embodiments of the present invention will be described by way of examples.

  FIG. 1 shows an outline of the used color sorter. The color sorter shown in the figure includes a belt conveyor 2 that transfers the refractory raw material particles 1 and discharges them from the transfer end portion into the air, a fluorescent lamp 3 that irradiates the discharged refractory raw material particles 1 from above and below, A CCD camera 4 for detecting reflected light and transmitted light from the refractory raw material particles 1, a nozzle 5 for injecting the detected light with air at a predetermined threshold, and a sorting container for storing particles separated by the injected air 6 and.

  Table 1 shows the results of selecting the fused magnesia raw material using this color sorter.

  In the table, each of the examples and comparative examples shows the chemical components and physical characteristics measured by performing color selection twice, sorting into three groups, and measuring each group.

  A to E shown in the raw material column of Table 1 indicate the magnesia raw material used before electromelting, and Table 2 shows the content of each magnesia raw material component. The mass% of MgO shows the purity as a magnesia raw material. Raw materials A, B, and C represent chemical components in which the portion excluding the loss of ignition of natural magnesite (Igloss: weight loss after holding at 1050 ° C. for 1 hour) is 100% by mass. Raw materials D and E represent chemical components of seawater magnesia clinker before electromelting.

The magnesia raw material shown in Table 2 was melted in an electric furnace of 1000 kVA and cooled as it was to prepare a fused magnesia ingot. While the ingot was divided, unnecessary portions such as an unmelted portion and a semi-melted portion on the outer peripheral portion were removed, and a lump of the molten portion was taken out. This lump was pulverized by a pulverizer, and the electrofused magnesia pulverized material that passed through a sieve having an opening of 10 mm was used as a test material for color selection as an example shown in Table 1 and a comparative example. The particle size distribution shown in Table 1 shows the result of measuring the particle size distribution of the pulverized material of electrofused magnesia. A sieve was used to measure the particle size distribution.

  Example 1 shown in Table 1 was electrofused with a purity of 96.5% by mass shown in A of Table 2, and was color-sorted into three grades: colorless and transparent G1a, white gray G1b, and brown gray G1c. It is a thing. The colorless and transparent portion of G1a has a high MgO purity of 98.7% by mass, a high bulk specific gravity, a low apparent porosity, and is dense. The white gray portion of G1b had a high MgO purity of 97.0% by mass, a high bulk specific gravity, a low apparent porosity, and was dense. However, the brown gray portion of G1c had a MgO purity as low as 95.0% by mass, a low bulk specific gravity and a high apparent porosity, and was relatively porous.

  In Example 2, A in Table 2 was used, and the purity thereof was the same as in Example 1. However, in the pulverized material of electrofused magnesia, the particle size of 0.2 mm or less was 10% by mass, which was larger than Example 1. It was. MgO in the transparent portion of G2a was 98.3% by mass, which was slightly lower than that of G1a, the bulk specific gravity was slightly lower, and the apparent porosity was slightly higher. The brownish gray part of G2c also has a slightly higher MgO, a slightly higher bulk specific gravity, a slightly lower apparent porosity, and a slightly sweeter overall discrimination. This is also a color sorter. Three types of grades were made.

  Example 3 uses A in Table 2 and the purity thereof is the same as that of Example 1. However, in the pulverized material of electrofused magnesia, the particle size of 0.2 mm or less is 15% by mass and more than Example 2. is there. Although the difference in chemical composition and physical properties between the three groups was smaller than in Example 2, it was possible to select three groups according to the purity of MgO.

  Example 4 is the case where B in Table 2 having an MgO purity of 92.6% by mass was used, but it was classified into three types of G4a (colorless and transparent), G4b (gray) and G4c (brown gray) with a color sorter. I was able to sort. The yield of the colorless and transparent material decreased to 5% by mass, and the brownish gray portion increased to 40% by mass, but what was selected was the amount of MgO indicating purity and the bulk specific gravity indicating density and apparent pores. The rate could be divided into three types.

  Example 5 and Example 6 were the cases where D and E of Table 2 were used, respectively, but both could be divided into three greats with different MgO purity. In particular, in Example 6, since a high-purity starting material was originally used, sorting becomes more difficult, but the yield of a high-purity product having a MgO purity of 99.4% by mass can be selected as high as 33% by mass. It was.

  On the other hand, the comparative example 1 uses the starting material C whose MgO purity shown in Table 2 is 86.2 mass%. By the color sorter, it was divided into three types according to the darkness of the same brown. Among them, only one type of H1a had a slightly higher MgO purity of 86.3% by mass than the starting material, but the other two types of H1b and H1c had the same MgO purity. Further, the bulk specific gravity and apparent porosity, which show the fineness important as the quality of the refractory raw material, showed almost no difference in the three types, and the grade classification of MgO as the refractory production raw material could not be performed.

  Next, 80% by mass of each of the fusing magnesia raw materials G1a, G1b, G1c, G3a, G5a, and G6a selected in Example 1, Example 3, Example 5, and Example 6 shown in Table 1 and a purity of 98 20% by mass of graphite of 20% by mass and metal Al were mixed, kneaded using a phenol resin as a binder, and heat-treated at 250 ° C. after molding to produce a magnesia carbon brick. The physical properties and corrosion resistance are shown in Table 3.

As shown in the table, the denser high-quality raw material with higher MgO component, higher bulk specific gravity and lower apparent porosity, the higher the refractory brick obtained, the higher the bulk specific gravity, the lower the apparent porosity, the compression Good quality with high strength was obtained, and corrosion resistance to slag was excellent.

  Tables 4 and 5 show examples of color selection of partially stabilized zirconia clinker as a refractory material according to the present invention.

The example of Example 7 shown in Table 5 is a partially stabilized zirconia clinker having 95% by mass of the ZrO ₂ component and 4% by mass of the CaO component, and 94 of the zirconia starting material badelite having the components shown in Table 4, respectively. A composition comprising 6% by mass of calcium carbonate and 6% by mass of calcium carbonate was prepared by electromelting in an electric furnace.

  The obtained ingot was pulverized so as to have a particle size of 10 mm or less, and the sized product obtained by adjusting particles having a particle size of 0.2 mm or less to 10% by mass or less was selected using a color sorter shown in FIG.

  As shown in Table 5 as Example 7, the results of sorting could be sorted into two types, G7a (yellow) and G7b (red).

The selected G7a had a higher amount of ZrO ₂ , a lower amount of CaO, a higher bulk specific gravity, a lower apparent porosity and a higher density than G7b. Two kinds of the selected fused zirconia were mixed with 90% by mass and 10% by mass of graphite, respectively, and a zirconia graphite immersion nozzle for continuous casting was formed by CIP molding, and reduced and fired. Table 5 shows the physical properties of the refractory and the erosion test results with the continuous casting powder. The refractory using G7a has a higher bulk specific gravity than the refractory using G7b, has a low apparent porosity, is dense, and has an excellent corrosion resistance of 15%.

It is a figure which shows roughly the structure and function of a color sorter used in the Example.

Explanation of symbols

1 Refractory Raw Material Particles 2 Belt Conveyor 3 Fluorescent Lamp 4 CCD Camera 5 Injection Nozzle 6 Sorting Container

Claims (6)

  A method for selecting a refractory raw material, in which particles of the refractory raw material having a purity of 90% by mass or more and a particle size of 20 mm or less are selected according to purity by color selection.   The method for selecting a refractory raw material according to claim 1, wherein the particles of the refractory raw material are those obtained by roughly screening and then pulverizing an ingot of the refractory raw material taken out from the electric furnace.   The method for selecting a refractory material according to claim 1 or 2, wherein the particles of the refractory material are prepared by adjusting the content of particles having a particle size of 0.2 mm or less to 10 mass% or less.   In color selection, the refractory raw material particles are transferred by a transfer means and discharged from the transfer end portion into the air. The emitted refractory raw material particles are irradiated with light, and the irradiated light is detected by an optical discriminating means. The method for selecting a refractory raw material according to any one of claims 1 to 3, wherein the refractory raw material is sorted by applying a jet flow corresponding to the threshold value to the refractory raw material particles.   The method for selecting a refractory material according to claim 4, wherein the light for color selection detected by the optical discrimination means is transmitted light and / or reflected light. The method for selecting a refractory raw material according to any one of claims 1 to 5, wherein the refractory raw material is magnesia.

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