KR19980046777A - Manufacturing method of magnesia-zirconia ceramic porous body - Google Patents

Abstract

The present invention relates to a method for producing a magnesia-zirconia-based ceramic porous body, and an object thereof is to coat an oil-based slurry and an aqueous slurry made of magnesia and zirconia powder as a main component on a polyurethane porous body, thereby reducing pore blocking and mechanical strength. An object of the present invention is to provide an excellent magnesia-zirconia-based ceramic porous body.

The present invention for achieving the above object is a method for producing a magnesia-zirconia ceramic porous body, 1.0-2.5% by weight of polyvinylbutyral (polyvinlybutyral), 15-30 in the mixed powder consisting of magnesia and zirconia Preparing an oil-based slurry by mixing methylethylketone by weight and 2.5-4.0% by weight of oleic acid; Coating the prepared oil-based slurry on a porous polyurethane body, and then heat-treating 0.5-1 hours at a temperature range of 1400-1500 ° C. to form a primary coating layer; To a mixed powder composed of magnesia zirconia, 2.5-4.5 wt% polyvinylalcohol, 15-30 wt% distilled water at pH 7-8 and 0.2-0.6 wt% sodium hexametaphosphate ) To prepare an aqueous slurry; And coating the prepared aqueous slurry on the coating layer formed by the oil-based slurry, followed by heat treatment for 4-6 hours at a temperature range of 1550-1650 ° C. to form a secondary coating layer. The summary relates to a method for producing a porous body.

Description

Manufacturing method of magnesia-zirconia ceramic porous body

The present invention relates to a method for producing a magnesia-zirconia-based ceramic porous body used for a molten steel refining filter and a waste heat storage device.

In general, a ceramic porous body is manufactured by coating an aqueous slurry on a polyurethane porous body, followed by drying and heat treatment. Aqueous slurry prepared by mixing additives and ceramic powder in distilled water has low coating property on the urethane porous body, so that the thickness of the coated slurry is thin and mechanical durability due to the formation of voids at the corners of the porous body as indicated by reference numeral 2 in FIG. There is a problem that there is a limit to the improvement. In order to solve this problem, U.S. Patent Nos. 4789140 and 4866011 use a double coating method of first coating a slurry having excellent coating property on a porous polyurethane body, and then reapplying a ceramic slurry thereon. However, the slurry used in the above technique has a high viscosity and thus has a disadvantage in that it is not applicable to a porous body having a small hole formed as shown by reference numeral (1) of FIG.

The magnesia-zirconia system has a high affinity with alumina inclusions in the molten steel and has a high melting point and specific heat. However, in the case of the porous body manufactured by the conventional method, there is a disadvantage that the mechanical strength is low or the hole is severely blocked and thus cannot be used as the structure.

In order to solve the above problems, the present inventors have repeatedly studied and experimented and proposed to the present invention based on the results. The present invention is an oil-based slurry and water-based slurry prepared mainly from magnesia and zirconia powder in a porous polyurethane body. The purpose of the present invention is to provide a magnesia-zirconia-based ceramic porous body having little pore blockage and excellent mechanical strength by coating the slurry.

1 is a schematic diagram of a porous ceramic body

The present invention is a method for producing a magnesia-zirconia-based ceramic porous body, 1.0-2.5% by weight of polyvinylbutyral, 15-30% by weight of methyl ethyl in a mixed powder consisting of magnesia and zirconia Preparing an oil-based slurry by mixing methyl ethylketone and 2.5-4.0 weight% of oleic acid; Coating the prepared oil-based slurry on a porous polyurethane body, and then heat-treating 0.5-1 hours at a temperature range of 1400-1500 ° C. to form a primary coating layer; To a mixed powder composed of magnesia zirconia, 2.5-4.5 wt% polyvinylalcohol, 15-30 wt% distilled water at pH 7-8 and 0.2-0.6 wt% sodium hexametaphosphate ) To prepare an aqueous slurry; And coating the prepared aqueous slurry on the coating layer formed by the oil based slurry, followed by heat treatment for 4-6 hours at a temperature range of 1550-1650 ° C. to form a secondary coating layer. It relates to a method for producing a porous body.

Hereinafter, the present invention will be described in more detail.

The materials applied to the present invention have the following characteristics.

First, polyvinyl butyral and polyvinyl alcohol used as additives for interlinking raw material powders have high solubility in methyl ethyl ketone and distilled water used as solvents, and high dry strength of the construction body.

Oreic acid and hexametaphosphate are suitable as additives to disperse raw material powders because they have good adsorption to magnesia powder and zirconia powder and excellent affinity with the solvent used. In addition, oleic acid and hexametaphosphate adsorb on the surface of the raw powder to prevent the coagulation of powder particles, thereby dispersing the particles in a solvent.

Methyl ethyl ketone is suitable as a solvent because of its high wettability to magnesia and zirconia powder and its high solubility in dispersants and binders.

In the case of the aqueous slurry, it is preferable to use distilled water of pH 7-8 as a solvent because general water is used, since the concentration of dissolved ions is high and the variation in viscosity and peptizing property of the prepared slurry is severe.

Polyurethane porous body is excellent in elasticity and easy to manufacture, so it is suitable as a structure to coat the slurry in the manufacture of the ceramic porous body.

The present invention using the material as described above using a mixed powder of magnesia and zirconia, the following will be described in more detail by dividing the manufacturing process step by step.

First, in the present invention, 1.0-2.5% by weight of polyvinyl butyral, 15-30% by weight of methyl ethyl ketone, and 2.5-4.0% by weight of oleic acid are mixed with the mixed powder consisting of magnesia and zirconia. To obtain an oil-based slurry.

The polyvinyl butyral should be added in the range of 1.0-2.5% by weight. The reason is that when the added amount is less than 1.0% by weight, the dry strength of the slurry is low, so that the porous structure is easily collapsed during heat treatment, and the viscosity of the slurry is lowered. In addition, when the amount added is more than 2.5% by weight, the viscosity of the slurry is high, and the pores of the porous body during coating are severe.

The methyl ethyl ketone should be added in the range of 15-30% by weight. The reason is that if the content is less than 15% by weight, the viscosity of the slurry is high without uniform mixing of the raw material powder, and if the content is more than 30% by weight, the viscosity of the slurry is lowered, so that the thickness of the coating layer is thin or uncoated and flows down. .

The oleic acid should be added in the range of 2.5-4.0% by weight. The reason is that when the added amount is less than 2.5% by weight, the peptizing property of the slurry is poor, and when it is more than 4.0%, the slurry has a high viscosity and the coating property of the slurry on the urethane porous body is poor.

Next, in the present invention, after coating the prepared oil-based slurry on a porous polyurethane body, a step of heat-treating for 0.5-1 hours at a temperature range of 1400-1500 ℃ goes through the step of forming a primary coating layer.

If the firing is performed at a temperature lower than 1400 ° C. or the holding time is less than 0.5 hour, the strength of the fired porous body is low, and thus, the rotary coating cannot be performed. In addition, when firing at a temperature higher than 1500 ℃ or the holding time exceeds 1 hour, since the dense coating layer is formed after the heat treatment, the slurry does not penetrate into the coating layer when coating the aqueous slurry. Therefore, the interlayer adhesion is not sufficient, and the interlayer peeling occurs during the heat treatment after coating the aqueous slurry. Therefore, in the present invention, the primary coating layer is formed by heat-treating 0.5-1 hours in the temperature range of 1400-1500 ° C.

Next, in the present invention, 2.5-4.5% by weight of polyvinyl alcohol, 15-30% by weight of distilled water having a pH of 7-8 and 0.2-0.6% by weight of hexameta to the mixed powder consisting of magnesia and zirconia Sodium phosphate is mixed to produce an aqueous slurry.

The polyvinyl alcohol should be added in the range of 2.5-4.5% by weight. The reason is that when the added amount is less than 2.5% by weight, the appropriate dry strength is not expressed and the viscosity of the slurry is low, and when the amount is more than 4.5% by weight, the slurry has a high viscosity and severe pore blocking occurs during coating.

The distilled water should be added in the range of 15-30% by weight. The reason is that if the added amount is less than 15% by weight, the viscosity of the slurry is high and the pore clogging of the porous body during coating is severe. If the amount is more than 30% by weight, the viscosity of the slurry is low, so that a thin or uniform coating layer is not formed. .

The hexametaphosphate should be added in the range of 0.2-0.6% by weight. If the addition amount is less than 0.2% by weight, the peptizing property of the slurry is poor, and when the amount is more than 0.6%, the viscosity of the slurry is high and the hole is severely clogged when the slurry is coated on the calcined porous body.

Next, in the present invention, the prepared aqueous slurry is coated on the coating layer formed by the oil-based slurry, and then heat treated at a temperature range of 1550-1650 ° C. for 4-6 hours to form a secondary coating layer.

If the firing temperature is lower than 1550 ° C. or the holding time is shorter than 4 hours, the strength of the porous body is poor in high temperature stability. In addition, when the firing temperature is higher than 1650 ℃ or holding time is longer than 6 hours, there is almost no change in the physical properties of the porous body is not preferable in terms of manufacturing cost. Therefore, in the present invention, to form an aqueous coating layer by heat treatment for 4-6 hours in the temperature range of 1550-1650 ℃.

Magnesia and zirconia powder, which is a raw material powder used in the present invention, is not particularly limited. However, when the coarse particles are used, it is preferable to use a powder having a size of 500 mesh or less because the slurry becomes non-uniform and precipitates quickly. In addition, a polyurethane porous body can use a general thing. In addition, the solvent, the binder, and the peptizing agent, which are additives, are not particularly limited but are preferably 99% or more in order to minimize the influence of impurities.

Example

Polyurethane porous body was used that is known to have a hole size of 1.5mm. Magnesia and zirconia were powders of 500 mesh or less, and the urethane porous body was prepared in an oil-based slurry prepared by mixing polyvinyl butyral, methyl ethyl ketone, and oleic acid with respect to the magnesia and zirconia mixed powder in a weight ratio as shown in Table 1 below. It was impregnated and coated and then compressed with a press to remove excess slurry. After drying at room temperature, a calcined porous body was prepared by heat treatment at 1400-1500 ° C. for 0.5-1 hour.

In addition, magnesia and zirconia powder is coated with a porous porous body by impregnating a plastic porous body in an aqueous slurry prepared by mixing magnesia and zirconia mixed powder with polyvinyl alcohol, distilled water having a pH of 7-8, and sodium hexametaphosphate at a weight ratio as in Table 1 The excess slurry was then removed by rotating the porous body using a rotary coater. The surface-coated porous body was dried at room temperature and heat-treated at 1550-1650 ° C. for 4-6 hours to prepare a ceramic porous body.

In Table 1, polyvinyl butyrate is PVB, methyl ethyl ketone is MEK, oleic acid is OA, polyvinyl alcohol is PVA, distilled water is H, and hexametaphosphate is represented by PH. The viscosity of the slurry was measured by a commercially available rotary viscometer, showing the value when the viscometer showed the maximum shear rate. Peeling degree of each slurry was compared by measuring the sedimentation density, and the coating state and coating thickness of the slurry were evaluated by observing the surface state of the porous body formed by using the slurry.

The values measured as above are shown in Table 1 below.

As shown in Table 1, it can be seen that Example (1-3) according to the present invention has excellent physical properties compared to Comparative Example (4-16).

As described above, the present invention improves the mechanical durability of the magnesia-zirconia porous body so that the present invention can be applied as a high temperature structure such as a molten steel refining filter or a waste heat recovery machine.

Claims (1)

In the manufacturing method of magnesia-zirconia-based ceramic porous body, An oily slurry is prepared by mixing 1.0-2.5% by weight of polyvinyl butyral, 15-30% by weight of methyl ethyl ketone, and 2.5-4.0% by weight of oleic acid to a mixed powder consisting of magnesia and zirconia. Doing; Coating the prepared oil-based slurry on a porous polyurethane body, and then heat-treating 0.5-1 hours at a temperature range of 1400-1500 ° C. to form a primary coating layer; Aqueous slurry containing 2.5-4.5% by weight of polyvinyl alcohol, 15-30% by weight of distilled water having a pH of 7-8, and 0.2-0.6% by weight of hexametaphosphate, mixed with the mixed powder of magnesia zirconia. Preparing a; And Magnesia-zirconia-based ceramic porous body comprising the step of coating the prepared aqueous slurry on the coating layer formed by the oil-based slurry, followed by heat treatment for 4-6 hours at a temperature range of 1550-1650 ℃ to form a secondary coating layer. Manufacturing method.