JPH0451483B2 - - Google Patents

Description

[Detailed description of the invention]

The present invention relates to a novel tellurium-cobalt amorphous compound material and a method for producing the same. In recent years, with the development of electronics and related technologies, research has been actively conducted on oxide-based ceramics, mainly tellurium dioxide (TeO ₂ ), and their single crystals. Research is being conducted as a conversion element material in fields such as gas-electricity, photoacoustic polarization, and X-ray spectroscopy, as well as as a catalyst material, magnetic material, and the like. _{TeO2 and Co2O3}
There are only a few documents describing stable compounds with amorphous compounds, and although studies on the single crystallization of these compounds are being actively conducted. No research has been conducted. The present invention provides a tellurium-cobalt amorphous oxide that has been completely unknown heretofore. That is, the present invention provides Te _(1-X) Co _2X O _(2+X) (however, 0<X≦
0.4) A novel tellurium-cobalt amorphous compound material having the composition, and tellurium dioxide and cobalt oxide corresponding to Te _(1-x) Co _2x O _(2+x) (where x is the same as above). The present invention relates to a method for producing a tellurium-cobalt amorphous compound material, which comprises heating and melting a mixture thereof and then ultra-quenching the mixture. The tellurium-cobalt amorphous oxide of the present invention is
Magnetic materials, photoresponsive magnetic elements, temperature-responsive magnetic elements, magnetic memory materials, ion conductive materials, magnetic tapes, catalysts, light-transparent conductive materials, dielectric materials, optical
It is useful as an electric switching element, a thermo-electrical switching element, etc. The tellurium-cobalt amorphous oxide of the present invention is
It is manufactured as follows. The raw material used in the present invention is a mixture of tellurium dioxide and cobalt oxide, and its composition ratio is such that Te _(1-X) Co _2X O _(2+X) (0<X≦0.4) It is a ratio. A raw material mixture having the above composition ratio is heated and melted, and then cooled extremely rapidly. The heating and melting may be carried out at a temperature higher than the temperature at which these raw material mixtures are sufficiently melted, preferably in a temperature range of about 50 to 200°C higher than the melting temperature, and particularly preferably in a temperature range of about 80 to 150°C higher than the melting temperature. There are no particular restrictions on the atmosphere during heating, and heating is usually performed in air. Next, the melt of the raw material mixture is ultra-quenched. Ultra-quenching is an essential requirement for the method of the present invention, and only through this can a new amorphous compound be obtained. Ultra-rapid cooling is usually performed at a cooling rate of about 10 ⁴ to ^{10 6} °C/sec. This ultra-rapid cooling can be carried out by a wide variety of methods as long as it can be cooled at the above-mentioned cooling rate.The melt of the raw material mixture is ejected onto the surface of the roll rotating at high speed and solidified in the atomic arrangement of the liquid state. A typical example is the method of forcing people to do something. An example of a quenching apparatus for a molten raw material mixture used in carrying out the method of the present invention will be described below with reference to the drawings. FIG. 1 shows a front view of the rapid cooling device main body 3 installed on the pedestal 1. As shown in FIG. The quenching device includes dielectric heating coils 5, 5..., a raw material heating tube 7, a support 9 for the tube 7, a nozzle 11 for spouting the molten raw material, a quenching roll 13, and a cooling nozzle 1 for the nozzle 11.
5, the main components include an air nozzle 17 for preventing swirling, a fine adjustment mechanism 19 for the nozzle 11, an air cylinder 21, a receiving box 23 for the cooled material, a cooling material outlet 25, etc. By installing a fan for cooling the roll inside the cooling roll 13 and providing an air blowing port at the end of the roll surface, the molten raw material can be rapidly cooled stably. FIG. 2 shows details of the support 9. In FIG.
9. A cooling water discharge path 31, a blow air introduction path 35 equipped with a needle valve 33, a fine adjustment mechanism 37 for the distance between the surface of the roll 13 and the nozzle 11, and a rectifying perforated plate 39 for uniformly extruding the raw material melt. We are prepared. When carrying out the method of the present invention using the quenching device 3 shown in FIGS. 1 and 2, a raw material mixture of a predetermined composition is first stored in a tube 7 having a nozzle 11 for blowing out the melt. The tube 7 is preferably made of a material that is sufficiently durable under high-temperature oxidizing atmosphere conditions, such as platinum, platinum-rhodium, iridium, silicon nitride, boron nitride, or the like. Note that the material of the portion not in direct contact with the raw material melt may be high melting point ceramics, glass, or metal. The shape of the nozzle opening is appropriately determined depending on the target product; for example, a round shape is used for a thin linear material, and a slit-like shape is used for a wide product. The shape of the nozzle opening may be oval or other shape. The raw material mixture stored in the tube 7 is then heated to a temperature equal to or higher than its melting point to form a melt, and then is poured from the mouth of the nozzle 11 onto the surface of the roll 13 rotating at high speed under constant gas pressure. It is blown out and rapidly cooled on the roll surface. The blowing angle of the raw material melt between the nozzle opening and the roll surface may be perpendicular to the roll surface if the width of the target compound is approximately 3 mm or less;
If it is more than mm, the angle is 0° to 45° with respect to the normal to the roll surface. Although these blowout angle adjustment mechanisms can be incorporated into the device itself as a mechanism that can set a predetermined angle, it is preferable to process the nozzle itself. The heating method for the raw material mixture is not particularly limited, but it is usually carried out in a furnace equipped with a heating element, a dielectric heating furnace, or a condensing heating furnace. The temperature of the raw material melt is preferably 50 to 200°C, preferably 80 to 150°C higher than its melting point. At this time, if it is too close to the melting point,
While the melt is being blown out onto the roll surface, there is a risk that it will cool and solidify near the nozzle, and conversely, if the temperature becomes too high, it tends to be difficult to rapidly cool the melt on the roll surface. The pressurizing gas used to blow the melt onto the roll surface is preferably an inert gas, such as argon, nitrogen, helium, etc., but in order to maintain the melt raw material in an oxidized state, dry compression is recommended. Air is preferred. The gas pressure depends on the size of the nozzle opening, but is usually 0.1 to 2.0 Kg/ ^cm2 , preferably 0.5 to 1.0.
It is about Kg/ ^cm2 . Further, the distance between the nozzle opening and both sides of the roll when blowing out the raw material melt is preferably about 0.01 to 1.0 mm, more preferably about 0.05 to 0.5 mm. If smaller than 0.01mm, the paddle amount will be very small and you will not get uniform material, while 1.0mm
If it is larger than , the amount of paddle may be excessive,
Furthermore, if the thickness is greater than the thickness of the puddle formed by the interfacial tension of the composition melt, there may be a tendency for the puddle to be difficult to form. The material of the roll includes copper and its alloy having good thermal conductivity, the above-mentioned materials having a hard chrome plating layer, copper, stainless steel styrene, and the like. The circumferential speed of the roll is 5 m/s to 35 m/s, preferably 10
m/sec to 20 m/sec, and by rapidly cooling the raw material melt, the desired amorphous compound material of good quality can be obtained. In this case, if the peripheral speed of the roll is 5 m/sec or less, it is not very preferable because it tends to be difficult to become amorphous. When the peripheral speed of the roll is higher than 35 m/sec, the shape of the target material obtained becomes extremely thin and becomes scaly or fine powder, but in terms of material structure, it is still the amorphous compound material of the present invention. It is. When producing the compound of the present invention under reduced pressure or high vacuum or in an inert gas atmosphere as the atmosphere in which the melt raw material is blown onto the rotating roll surface, reduction of the raw material melt at high temperature occurs, Oxygen atoms in the composition atoms decrease, and the resulting material becomes colored purple or black. However, this colored product is also a compound of the present invention physically and can be used in a colored state. When heating and melting the raw material mixture in a tube, it is necessary to completely melt the mixture. However, before the mixture is completely molten, some of the molten material may flow out from the nozzle tip, so the nozzle tip is locally cooled to prevent the melt from flowing out. It is preferable to do so. A typical means for locally cooling the nozzle is to blow a cooling gas onto the tip of the nozzle, and the gas may be an inert gas such as argon, helium, nitrogen, etc., but dry, cold compressed air is more preferable. The novel amorphous compound material according to the present invention usually has a thickness of about 50 to 10 μm and is a very brittle material. For this reason, after the material is rapidly cooled and solidified on the roll surface, it is preferable that stress is not applied to the material as much as possible. One of the causes of stress addition is the large turbulent flow in the air layer on the roll surface caused by the wind phenomenon caused by roll rotation in the atmosphere. In order to prevent this turbulence and to improve the adhesion between the molten raw material mixture to be rapidly cooled and the roll surface, a countercurrent blowout nozzle for preventing wind blowing, that is, an air nozzle 17 for preventing swirling as shown in FIG. 1 may be installed. , a fan is fixedly installed inside the roll. In the latter case, the turbulent flow generated inside the roll due to rotation of the roll is absorbed into the roll through a variable-diameter air inlet provided at the end of the roll surface, and is discharged from the front of the roll axis, allowing air to flow over the roll surface. By moving the melt into the interior, the melt is pressed more tightly against the roll surface, and the roll itself can also be cooled by air blowing and movement. Further, in order to maintain the dimensional uniformity of the obtained material, if grooves for cutting the material are provided on the roll surface at right angles to the rotation direction, the material can be cut to a constant size. The tellurium-cobalt compound of the present invention has an atomic arrangement structure that changes greatly depending on the mixing ratio of raw materials, and can be broadly classified into the following types. First, if 0.40≧x>0, the amorphous compound is 100%
is obtained, and in the range 0.50≧x＞0.40
An oriented polycrystalline mixed amorphous compound containing a Co ₂ O ₃ crystal phase is obtained, and when x>0.50, a material mainly consisting of a Co ₂ O ₃ crystal phase is obtained. FIG. 3 shows the production range of the material of the present invention. The peripheral speed of the quenching roll of the quenching device used is
Within the range of 5 m/sec to 35 m/sec, no major changes are observed in the structure of the material obtained in each composition range. In order to identify the structure of the material of the present invention, the presence or absence of crystallinity was confirmed and structurally analyzed using X-ray diffraction and a polarizing microscope, and a very small portion was observed using a scanning electron microscope. The features of the present invention will be further clarified by examples below. Example 1 TeO ₂ (purity 99.9%) and Co ₂ O ₃ (purity 99.9%) were blended in a predetermined composition, mixed uniformly, and heated to 850°C.
The mixture was calcined for 30 minutes and used as a raw material for a composition. The obtained composition raw material was made into a platinum tube (diameter 10 mm x length 150 mm).
Filled with water, installed in the dielectric heating coil, oscillating tube fiber voltage 13V, anode voltage 10KV, grid current 120~
Dielectric heating was performed under the conditions of 150 mA and anode current of 1.2 to 1.8 A. The completely molten raw material was blown out onto the surface of a rotating rapid cooling roll using dry compressed air to rapidly cool it. Tables 1 and 2 show the composition and manufacturing conditions. Samples No. 1 to 20 and 26 in Tables 1 and 2
shows the amorphous oxide material of the present invention in ribbon form. In addition, No. 24 is a thin piece due to the high roll rotation speed, but it can be used in fields such as catalysts where there are no restrictions on shape. Note that nozzle shape A indicates a slit-like nozzle of 0.2 mm x 4 mm, and nozzle shape B indicates a circular nozzle with a diameter of 0.2 mm.

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【table】

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[Table] Reference Example 1 X-ray diffraction results for Samples No. 8, 10, 12, 13, and 15 of Example 1 above corresponding to x = 0.40 in Te _(1-x) Co _2x O _(2+x) is shown in Figure 4. The peripheral speed of the quenching roll changed from 5.18 m/sec (No. 8) to 34.54 m/sec.
It is clear that there is no significant change in the atomic arrangement structure of the material obtained within the range of seconds (No. 15). Reference Example 2 The differential thermal analysis results of Sample No. 7 of Example 1 above, which corresponds to x = 0.20 in Te _(1-x) Co _2x O _(2+x), were
As shown in the figure. In FIG. 5, Tc represents the crystallization temperature, Tg represents the glass transition point, and mp represents the melting point. Reference Example 3 A photograph showing the appearance of Sample No. 7 of Example 1, which corresponds to x=0.20 in Te _(1-x) Co _2x O _(2+x), is shown as a reference drawing. Reference Example 4 Scanning electron micrographs (20,000x and 620x) of Sample No. 7 of Example 1 are shown as reference drawings and 620x, respectively. Reference Example 5 The infrared absorption spectrum of Sample No. 3 of the above example corresponding to x=0.20 in Te _(1-x) Co _2x O _(2+x) is shown in FIG. Reference Example 6 Figure 7 shows the dielectric constant A and dielectric loss B versus frequency at 12.3°C of Sample No. 17 of Example 1, which corresponds to x = 0.10 in Te _(1-x) Co _2x O _(2+x). Shown below.

[Brief explanation of the drawing]

FIG. 1 is a front view of an example of a quenching device for melted raw materials used in the method of the present invention, and FIG.
FIG. 3 is a diagram showing the composition range of the material of the present invention; FIG. 4 is an X-ray diffraction diagram of some of the material of the present invention; FIG. 5 is a diagram of the quenching device according to the invention. The differential thermal analysis diagram of one material, FIG. 6, and the infrared absorption spectrum of another material according to the present invention, FIG.
The figures show graphs respectively showing the dielectric constant and dielectric loss versus frequency of another material according to the invention. 1... Frame, 3... Rapid cooling device main body, 5, 5...
Dielectric heating coil, 7... raw material heating tube,
9... Support for raw material heating tube, 11... Nozzle for spouting molten raw material, 13... Roll for rapid cooling, 1
5... Cooling nozzle for nozzle 11, 17... Eddy current prevention air nozzle, 19... Fine adjustment mechanism for nozzle 11, 21... Air cylinder, 23... Cooled material receiving box, 25... Cooling material take-up exit, 2
7... Valve, 29... Cooling water introduction path, 31...
Cooling water discharge path, 33... Needle valve, 35...
...Blow air introduction path, 37... Mechanism for finely adjusting the distance between the roll 13 and the nozzle 11, 39... Perforated plate for rectification.

Claims (1)

[Claims] A tellurium-cobalt amorphous compound material having a composition of 1 Te _(1-X) Co _2X O _(2+X) (0<X≦0.4). 2 Te _(1-X) Co _2X characterized by heating and melting a mixture of tellurium dioxide and cobalt oxide and then ultra-quenching the melt at a cooling rate of 10 ⁴ to 10 ⁶ °C/sec.
A method for producing a tellurium-cobalt amorphous compound material having a composition of O _(2+X) (0<X≦0.4). 3. The method for producing a tellurium-cobalt amorphous compound material according to claim 2, wherein the raw material melt is ultra-quenched by contacting it with a solid. 4. Pour the raw material mixture into a heating tube equipped with a nozzle with a slit-shaped, circular, or elliptical outlet, heat and melt at a temperature 50 to 200°C higher than the melting point of the mixture, and then heat for 5 to 35 m. Claim 2: The molten material is blown out through the nozzle onto the surface of a roll rotating at a circumferential speed of 1/2 to cool it super rapidly.
2. Method for producing tellurium-cobalt amorphous compound material.