JP2527861B2 - Drying method for thick ceramic products - Google Patents

Description

Detailed Description of the Invention

[0001]

BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for producing a thick ceramic product such as a suspended insulator having a fold, and more particularly to a method for drying the product.

[0002]

2. Description of the Related Art Conventionally, the drying of a thick ceramic product having a complicated shape having a fold portion such as a suspension insulator is performed at a low temperature in the initial stage in order to prevent cracks which are likely to occur in the initial stage of the drying.
Drying was performed slowly and slowly in a humidified state, and after the shrinkage of the product was completed (content of water content: 9 to 10 wt%), the drying was switched to high temperature and the whole was dried. That is, a thick ceramic product having a complicated shape to be dried, for example, a suspension insulator shown in FIG.
It was general to perform warm air drying according to the schedule shown in (1) to dry a thick ceramic product having an initial moisture content of 16.0 to 22.0 wt% to a moisture content of 1.0 wt% or less. In FIG. 2, the shape of the suspension insulator is a diameter D = 20.
0 ~ 500 mm, height H = 100 ~ 150 mm, thickness T = 20 ~ 50 mm
Is generally used, and as an example of porcelain composition, SiO ₂ :
66.33 wt%, Al ₂ O ₃ : 23.32 wt%, K ₂ O + Na ₂ O: 2.82 wt
%, Sintering temperature: 1220 ° C., porcelain bending strength: about 1470 kg / cm ² is used.

[0003]

[Table 1]

[0004]

However, in the above-mentioned conventional drying method, although complicated temperature, humidity and air volume are controlled and the ceramic product with a complicated shape can be suitably dried, at the end of the drying process. (The water content is 1
There is a problem that it takes a very long time to reach (wt% or less). Here, in order to shorten the drying time, the drying time is 0 to 1
It is also conceivable that the drying condition is tightened by a method of raising the temperature above the atmospheric temperature shown in Table 1 above, setting the humidity below Table 1 below, or increasing the air volume above Table 1 after 4 hours. However, if the drying conditions are so tight, cracks occur in the folds and the like of the material to be dried, and thus there is a problem that it is difficult to shorten the drying time in the conventional method for drying thick ceramic products. .

Further, far-infrared ray drying has been attempted for thick ceramic products, but far-infrared ray has a rapid heat transfer, but since it is only on the surface, a drying imbalance occurs in each part of the product, resulting in dry drying. As it is a cause, it is only used for thin plates that do not easily dry out and ceramic parts with a large number of pores such as chamotte bricks. It was not applied to thick ceramic products in shape.

The present invention is intended to solve the above-mentioned problems and to provide a method for drying a ceramic product having a complicated shape and a thick wall, which can greatly reduce the drying time as compared with the conventional drying method.

[0007]

The method of drying thick-walled ceramic products of complex shape according to the present invention uses far infrared rays as a heat source, and the humidity is not controlled. It is characterized in that the complex shape thick ceramic product is dried in a furnace.

[0008]

In the above-mentioned structure, far infrared rays are used instead of the conventional warm air drying, the humidity is not controlled, and the arrangement of the far infrared rays at the initial temperature of 80 ° C. or higher and lower than 140 ° C. By adjusting the distance between the heaters, etc., the water distribution on each surface of the material to be dried is made uniform, and an appropriate water gradient from the surface to the inside is formed. Even if it is dried at a high temperature, which is not considered by common sense, no scratches such as ribs occur.
Therefore, it is possible to speed up the drying until the end of drying shrinkage of the product having a water content of 9 to 10 wt%, and it is possible to raise the temperature in the initial stage of drying to a high temperature, though it is less than 140 ° C. at the maximum, so that the drying time is significantly increased. Can be shortened to When drying suspended insulators as an example of a complex shape thick ceramic product, in the furnace, the suspended insulators are arranged side by side so that the folds face downward in the direction of gravity,
Radiating far-infrared rays from above and below is preferable because drying can be efficiently achieved and the drying time can be shortened. In the following, the state of "no humidity control" is also referred to as a non-humidified state.

[0009]

EXAMPLES FIGS. 1 (a) to 1 (c) are views showing a state in which the drying method of the present invention is carried out. In the present embodiment, FIG.
As shown in the cross section of the entrance, for example, the width of the bottom of the entrance 6
The same number of far-infrared heaters 2 are provided on the ceiling and the bottom of a drying furnace 1 having a length of 00 mm and a height of 700 mm, respectively, and further drying should be performed on a net shelf 3 provided between the far-infrared heaters on the ceiling and the bottom. The suspension insulator 4 is placed and dried. A temperature sensor 5 composed of a pair of thermocouples is provided on the side surface of the drying furnace 1 at a position not directly receiving far-infrared rays and at a position close to a suspension insulator to control the temperature inside the furnace, and the suspension insulator 4 as shown in the drawing, It is preferable to arrange the suspension insulators in a row so that the folds face downward in the direction of gravity. Each far-infrared heater 2 has a planar shape of 70 mm × 140 mm, 200 V, 4 V, as shown in the plan view of FIG.
A 00W heater is used. Needless to say, the drying furnace 1 may be a single furnace or a tunnel furnace. Further, in FIG. 1A, the distances P ₁ and P ₂ between the far infrared heater 2 and the product surface are preferably 100 mm or more and 250 mm or less.

In the drying furnace having the above-mentioned structure, a suspended insulator having an initial water content of 16.0 to 22.0 wt% is actually used.
When drying was performed according to the schedule shown in Table 2 below, the drying could be completed in 9 hours until the completion of the drying with the water content of 1.0 wt% or less. That is, using far-infrared rays, in a drying furnace at an initial temperature of 80 ° C., not only after the contraction complete moisture content of 9 to 10 wt%, but also from the beginning to the completion of the contraction without humidification, Under the condition of no circulation, it was possible to dry the complex shape thick ceramic product only by controlling the temperature as shown in Table 2.

[0011]

[Table 2]

Comparing the results in Tables 2 and 1 above, the far infrared rays of the present invention were used, and the far infrared rays were arranged in the non-humidified state, the initial temperature was less than 140 ° C. at the maximum, the number of the far infrared rays, and the material to be dried and the heater. It can be seen that the drying end time can be shortened to 1 / 2.5 to 1/3 of the conventional method by adjusting the distance and the like. It uses far-infrared rays, no humidification,
By adjusting the arrangement of far infrared rays, the number of the far infrared rays, and the distance between the object to be dried and the heater at an initial temperature of less than 140 ° C at the maximum, a uniform distribution of moisture on each surface of the object to be dried and appropriateness from the surface to the inside can be obtained. This is because, due to the formation of the water gradient, etc., the stress distribution becomes almost uniform, and even if it is dried at an altitude that is not considered in the conventional wisdom, it can be dried without causing cracks in the folds of the suspension insulator.

Further, in the drying method of the present invention, in order to investigate the influence of the initial furnace temperature and the effect of raising the furnace temperature after the completion of shrinkage of the water content of 10 wt%, the initial furnace temperature was set at 80 ° C., 90 ° C. ℃, 100 ℃, 110 ℃, 120
C., 130.degree. C., 140.degree. C., after which the initial furnace temperature was maintained as shown in Table 3 below, and when the initial furnace temperature was 80.degree. C. and 90.degree. C., and thereafter contained as shown in Table 3 below. The water content after 8 hours was measured for each of the cases where the water content was 10 wt% or less and the temperature was raised.
The results are shown in Table 3. The fact that the water content reached 10 wt% was known by measuring the weight of the material to be dried once every 30 minutes, and determining the water content at that time from the evaporated water content and the initial water content. .

[0014]

[Table 3]

From the results shown in Table 3, the higher the initial temperature is, the smaller the water content after 8 hours is, but at 140 ° C., there is a problem in that the water content is broken, so that the maximum content is less than 140 ° C. It can be seen that when the water content is 10 wt% or less and the temperature is higher than the initial in-furnace temperature, the water content after 9 hours becomes smaller than when the initial temperature is maintained for 8 hours. From this result, the initial furnace temperature is 140 at maximum.
It is necessary that the temperature is lower than 0 ° C., the range of 110 to 130 ° C. is preferable, and it is preferable that the content of water content is 10 wt% or less and the temperature is higher than the initial furnace temperature.

[0016]

As is apparent from the above description, according to the present invention, far infrared rays are used instead of the conventional warm air drying, and the far infrared rays are arranged in a non-humidified state at an initial temperature of less than 140 ° C. at the maximum. By adjusting the number, the distance between the object to be dried and the heater, etc., the moisture distribution on each surface of the object to be dried is made uniform, and an appropriate moisture gradient from the surface to the inside is formed. A uniform stress distribution is obtained, and even if it is dried at a high temperature, which is not considered in the conventional wisdom, scratches such as ribs do not occur. Therefore, it is possible to speed up the drying until the end of drying shrinkage of the product having a water content of 9 to 10 wt%, and it is possible to raise the temperature in the initial stage of drying to a high temperature, though it is less than 140 ° C. at the maximum, so that the drying time is significantly increased. Can be shortened to

[Brief description of drawings]

FIG. 1 is a diagram showing a state in which a drying method of the present invention is carried out.

FIG. 2 is a diagram showing a shape of a conventional suspension insulator.

[Explanation of Codes] 1 Drying furnace 2 Far infrared heater 3 Ami shelf 4 Suspended insulator 5 Temperature sensor

Claims (2)

(57) [Claims] 1. A thick ceramic product characterized by using a far infrared ray as a heat source and drying a thick ceramic product in a furnace in a heated state having an initial temperature of 80 ° C. or higher and lower than 140 ° C. without controlling humidity. How to dry the product. 2. The method for drying a thick ceramic product according to claim 1, wherein the thick ceramic product to be dried is a suspended insulator, and the suspended ceramic is dried such that the folds of the suspended insulator face downward in the direction of gravity.