Apparatus And Method For Producing Casting Mold

Abstract

An apparatus and a method for producing a casting mold are provided, according to which the casting mold having a complex shape can be obtained with stable quality. The apparatus comprises a mold having a cavity therein, a steam supply unit, a steam supply passage connected to the cavity, steam discharge passages, flow regulators disposed in the steam discharge passages to regulate an amount of the steam discharged from the cavity, and a control unit for controlling the flow regulators. After a resin-coated sand prepared by coating a refractory aggregate with a binder resin is injected into the cavity of the heated mold, superheated steam is supplied into the cavity. At this time, the control unit controls the flow regulators such that the cavity is uniformly filled with the superheated steam.

Description

BRIEF EXPLANATION OF THE DRAWINGS

FIG. 1 is a schematic view of an apparatus of producing a casting mold according to a preferred embodiment of the present invention;

FIG. 2A is a graph showing a narrow particle-size distribution of a resin-coated sand;

FIG. 2B is a schematic view showing a filling state of the resin-coated sand having the narrow particle-size distribution;

FIG. 3A is a graph showing a wide particle-size distribution of a resin-coated sand; and

FIG. 3B is a schematic view showing a filling state of the resin-coated sand having the wide particle-size distribution.

BEST MODE FOR CARRYING OUT THE INVENTION

Referring to the attached drawings, an apparatus and a method for producing a casting mold of the present invention are explained below in detail according to preferred embodiments.

As shown in FIG. 1, the apparatus for producing the casing mold according to the subject embodiment is mainly composed of a mold 1 having a cavity 40 of a desired shape therein, a sand supply unit 3 for supplying a resin-coated sand into the cavity, a steam supply unit 7 for supplying superheated steam into the cavity, a steam supply passage 10 used to supply the superheated steam from the steam supply unit 7 into the cavity 40, a plurality of steam discharge passages (20, 21, 22) for discharging the superheated steam from the cavity, electromagnetic valves (30, 31, 32) disposed at the steam discharge passages, a suction pump 5 connected to a discharge port, which is formed at a confluence portion of ends of the steam discharge passages, and a control unit 4 for controlling the suction pump and the electromagnetic valves such that the cavity is uniformly filled with the superheated steam. In the drawing, the numeral 2 designates the resin-coated sand filled in the cavity, which is prepared by coating a refractory aggregate with a binder resin such as thermosetting resin. The numeral 60 designates a heater used to heat the mold. If necessary, a serge tank may be disposed at the upstream side of the suction pump.

As a material for the mold 1, a metal material or a heat-resistant resin material is available. The structure and the shape of the mold are not specifically limited. For example, the mold may be formed with a plurality of segment patterns, which can be coupled to each other to obtain the cavity of a desired shape in the mold. The mold 1 shown in FIG. 1 can be divided into upper and lower patterns, and the cavity 40 is obtained in the mold by coupling them to each other.

The sand supply unit 3 is slidable on a rail 80, and can be connected to the steam supply passage 10. When the steam supply passage 10 is connected to the sand supply unit 3, it functions as a sand supply passage for injecting the resin-coated sand 2 into the cavity 40.

The steam supply unit 7 comprises a steam generator 70 for generating steam having, for example, a temperature of 110° C. to 180° C., and a heating device 72 for generating superheated steam by raising the steam temperature without considerably increasing the pressure of the steam supplied from the steam generator 70. To superheat the steam, it is preferred to use a microwave. The superheated steam is defined as a steam obtained by further heating a saturated steam at its saturation temperature or more. In the present invention, the superheated steam supplied into the cavity preferably has a steam pressure of 1.5˜10 kgf/cm² and a temperature of 150° C. to 700° C., more preferably 200° C. to 600° C.

As shown in FIG. 1, when the cavity 40 is formed by coupling the segment patterns, a sealing material is preferably disposed at the coupling potion therebetween to prevent a leakage of the superheated steam. Specifically, it is preferred that a concave is formed in the coupling portion of the mold to place an expandable rubber as the sealing material therein, and an air supply passage is formed to supply the air into the sealing material. In this case, since the sealing material is expanded by the air supplied through the air supply passage, and the expanded sealing material is pressed against coupling surfaces of the segment patterns, it is possible to effectively prevent the leakage of the superheated steam. In addition, there is an advantage that the casting mold can be safely produced without causing a deterioration of working conditions.

An opening amount of each of the electromagnetic valves (31, 32, 33) used as flow regulators is controlled by the control unit 4 according to an output of a temperature sensor (50, 51, 52) located in the vicinity of an entrance of the corresponding steam discharge passage. That is, an amount of the steam sucked in the respective steam discharge passage changes with the opening amount of the corresponding electromagnetic valve. Therefore, when the steam discharge passage is formed at a region of the cavity of the complex shape where the steam is hard to reach, and the opening amount of the electromagnetic valve is controlled such that a temperature detected by the temperature sensor located in the steam discharge passage is within a desired temperature range, the steam can be uniformly supplied all over the cavity.

From the viewpoint of uniformly supplying the steam into the cavity, it is also preferred that the control parameter for the electromagnetic valve comprises a void fraction of the resin-coated sand 2 filled in the cavity. That is, as shown in FIGS. 2A and 2B, when the resin-coated sand 2 has a narrow particle-size distribution, relatively large voids occur among particles of the resin-coated sand filled in the cavity, so that the void fraction becomes relatively large. In this case, the superheated steam supplied in the cavity can easily penetrate into the resin-coated sand through these voids to increase the steam amount discharged through the steam discharge passage 20. As a result, there is a fear that the steam amounts discharged through the steam discharge passages (21, 22) decrease. In such a case, according to the present invention, the operations of the electromagnetic valves are controlled by the control unit 4 so as to reduce the opening amount of the electromagnetic valve located in the steam discharge passage 20, and at the same time increase the opening amounts of the electromagnetic valves located in the steam discharge passages (21, 22).

On the other hand, as shown in FIGS. 3A and 3B, when the resin-coated sand 2 has a wide particle-size distribution, small-sized particles are positioned in a void formed among relatively large-sized particles of the resin-coated sand filled in the cavity, so that the void fraction becomes relatively small. In this case, the superheated steam supplied in the cavity becomes hard to penetrate into the resin-coated sand. Therefore, it is needed to increase the opening amount of the electromagnetic valve located in the steam discharge passage 20, as compared with the case of using the resin-coated sand having the small particles-size distribution. As a result, since the steam amounts discharged through the steam discharge passages (21, 22) may decrease, the suction pump is controlled to increase the steam discharge amount. In brief, the operations of the electromagnetic valves and the suction pump are controlled by the control unit 4 such that the opening amount of the electromagnetic valve located in the steam discharge passage 20 is slightly increased to ensure that the steam reaches the entrance of the steam discharge passage 20, and on the other hand the opening amounts of the electromagnetic valves located in the steam discharge passages (21, 22) are sufficiently increased to ensure that the steam reaches the entrances of the steam discharge passages (21, 22), and also the discharge amount of the suction pump is increased.

In addition, when producing a thick-walled casing mold, there is a fear that heat is not sufficiently supplied into a core portion of the resin-coated sand filled in the cavity, so that only a part of the resin-coated sand which contacts an inner surface of the heated mold is cured. In the past, the metal mold has been heated at a high temperature to solve this problem. However, since a toxic gas occurs at the time of curing the binder material at the high temperature, a deterioration of working conditions was unavoidable. According to the present invention, since the steam is forcibly sucked into the steam discharge passages, it is possible to reliably achieve a uniform supply of heat into the core portion of the resin-coated sand filled in the cavity. Therefore, the casing mold can be produced under improved safe working conditions. In addition, it is not needed to heat the mold at the high temperature, as compared with the past. Furthermore, there is an advantage that a heat-resistant resin material other than the metal material can be used as the mold material. In this case, an increase in degree of freedom of designing the mold and a reduction in production cost can be achieved.

In addition, it is preferred to control the opening amounts of the electromagnetic valves in consideration of the void fraction by previously determining the void fraction of the resin-coated sand filled in the mold by a preliminary experiment, and inputting this void fraction through an input portion (not shown) formed in the control unit 4. For example, the void fraction is defined as a numerical value measured by the following method.

First, 100 ml of a mixture solution prepared such that a weight ratio of water:methanol is 7:3 is put in a measuring cylinder having a volume of 200 ml. Next, 100 ml of the resin-coated sand, which is measured by use of another measuring cylinder, is gradually added to the mixture solution, and then the measuring cylinder is sealed. After it is confirmed that the occurrence of air bubbles has stopped, a liquid level in the measuring cylinder is read off. The void fraction is provided by a difference between the liquid level (M ml) and the scale of 200 ml. Therefore, the void fraction (%) is defined as 200-M. As the solution, water including an interfacial active agent or another liquid may be used in place of the mixture of water and methanol.

A method for producing the casing mold with use of the apparatus described above is explained below in detail. First, the resin-coated sand 2 is injected into the heated mold 1 by the sand supply unit 3. The resin-coated sand can be prepared by coating a refractory aggregate with a binder material (binder resin) such as a thermosetting resin. As the thermosetting resin, for example, it is possible to use a phenol resin, furan resin, isocyanate resin, amine polyol resin or a polyether polyol resin. The mold is preferably heated at a curing temperature or more of the resin-coated sand, for example, 130° C. to 200° C.

Next, the superheated steam is supplied into the cavity 40 of the mold 1 by the steam supply unit 7 to cure the resin-coated sand The superheated steam preferably has the curing temperature or more of the resin-coated sand 2, for example, 200° C. to 600° C., and a steam pressure of 1.5˜10 kgf/cm². After the superheated steam supplied in the cavity heats the resin-coated sand at the temperature needed for curing, it is discharged from the cavity through the steam discharge passages (20, 21, 22). At this time, the electromagnetic valves (30, 31, 32) and the suction pump 5 are controlled by the control unit 4 such that the cavity is uniformly filled with the superheated steam.

According to the present invention, since the steam discharge passages are formed at different locations to forcibly discharge the superheated steam from the cavity, the superheated steam can be uniformly supplied all over the cavity. Therefore, even when producing the casing mold of a complex shape, it is possible to remarkably reduce the treatment time needed to cure the casing mold, and prevent variations in quality to stably provide the casting mold with uniform quality. In addition, when the binder material of the thermosetting resin is cured by use of the superheated steam, the occurrence of a toxic gas such as ammonia, formaldehyde and phenol can be remarkably reduced. Furthermore, even when a small amount of the toxic gas is generated, it is absorbed by the steam, and then discharged to prevent that the working conditions are deteriorated by the occurrence of the toxic gas. Thus, it is possible to achieve improvements in yield ratio and production efficiency of the casing mold, while preventing the deterioration of working conditions.

After the supply of superheated steam is continued until the curing of the resin-coated sand is completed, the casing mold of the cured resin-coated sand is removed from the cavity. To prevent that the moisture remains in the produced casing mold, the casing mold may be dried by a drying device. By the way, according to the present invention, since the steam uniformly supplied all over the cavity of the complex shape is forcibly removed through the steam discharge passages, dew condensation of the steam is hard to happen in the interior of the casing mold. Therefore, the drying process described above may be omitted.

In the above explanation, a single supply passage is used to supply the resin-coated sand and the superheated steam into the cavity. However, a plurality of supply passages may be formed depending on the shape and size of the cavity. In addition, the apparatus described above has three steam discharge passages. According to the shape of the cavity, two or four or more of the steam discharge passages may be formed at suitable locations. Moreover, it is not essential in the present invention that each of the steam discharge passages has the electromagnetic valve. Further, the suction pump may be connected to only a predetermined one or more of the steam discharge passages.

EXAMPLES

Examples 1-3 and Comparative Examples 1-3

The present invention is concretely explained below according to Examples.

A resin-coated sand used in the subject Examples was prepared, as described below. First, 680 parts by weight of phenol, 680 parts by weight of 37% formalin and 101 parts by weight of hexamethyltetramine were put in a reaction vessel. A resultant mixture was heated up to 70° C. by taking about 60 minutes, and then reacted by keeping as it is for 5 hours. The thus obtained reaction product was dewatered at 90° C. under a reduced pressure of 100 Torr, and then cooled to obtain a resol-type phenol resin having a softening point of 80° C.

Next, 30 kg of a Flattery sand heated at 145° C. and 450 g of the resol-type phenol resin were put in a Wahl mixer, and kneaded for 30 seconds. Subsequently, 450 g of water was added to the mixer, and a resultant mixture was further kneaded until sand particles are disrupted. After 30 g of calcium stearate was further added to the mixer, and a resultant mixture was kneaded for 30 seconds, aeration was performed to obtain a resin-coated sand having a resin amount of 1.5% by weight ratio. A void fraction of the resin-coated sand is 42%.

To produce the casting mold, the apparatus of FIG. 1 was used. The resin-coated sand 2 described above was injected at a pressure of 2.5 MPa from the sand supply unit 3 connected to the steam supply passage 10 into the cavity 40 of the metal mold 1 heated at 160° C. Next, the sand supply unit 3 was disconnected from the steam supply passage 10, and the steam supply unit 7 was connected to the steam supply passage 10. A saturated steam of 165° C. was generated under a pressure of 7 kgf/cm² by the steam generator 70, and then superheated by the heating device 72 to obtain superheated steam of 400° C. The superheated steam was supplied for 10, 20 or 30 seconds into the cavity 40 having the resin coated sand 2 therein to produce the casting mold. The casting molds of Comparative Examples 1 to 3 were produced by use of an apparatus, which has the same cavity shape, but does not have the electromagnetic valve as the flow regulator, the suction pump and the control unit.

	TABLE 1
	Steam	Temperature of	Quality of
	Supply	Steam Discharge Passage	Casting
	Time (sec)	20	21	22	Mold
Example 1	10	115	113	115	◯
Example 2	20	123	122	121	◯
Example 3	30	132	130	129	◯
Comparative	10	125	82	79	X
Example 1
Comparative	20	134	93	90	X
Example 2
Comparative	30	138	108	110	Δ
Example 3

Temperatures measured at the vicinities of the entrances of the respective steam discharge passages (20, 21, 22) and evaluation results of the casting molds, each of which was removed from the metal mold, are shown in Table 1. As the evaluation standards, “◯” designates that the casting mold has good quality, “Δ” designates that the casting mold partially has an uncured portion, and “×” designates that the casting mold is unusable.

In Examples 1 to 3, the temperatures of the steam discharge passages are relatively uniform. In addition, even when the steam was supplied for a short time period, the inside of the cavity was uniformly heated. As a result, the casting molds with stable quality were obtained. On the other hand, in Comparative Examples 1 to 3, since the suction of the steam into the steam discharge passages was not controlled, the temperatures measured at the vicinities of the entrances of the steam discharge passages (21, 22) were relatively low. In addition, as the steam supply time was longer, the quality of the casing mold was slightly improved. However, when the steam supply time was short, a defective casing mold occurred due to nonuniform temperature distribution in the cavity.

Thus, the results of the subject Examples show that the casting mold having the complex shape can be stably produced by supplying the steam for the short time period.

Examples 4-6 and Comparative Examples 4-6

A resin-coated sand used in the subject Examples was prepared according to the substantially same manner as the Examples 1 to 3 except for using Unimin 90 sand in place of the Flattery sand. A void fraction of this resin-coated sand is 37%. By using this resin-coated sand, casting molds were produced as in the cases of Examples 1 to 3 and Comparative Examples 1 to 3. Results are shown in Table 2.

	TABLE 2
	Steam	Temperature of	Quality of
	Supply	Steam Discharge Passage	Casting
	Time (sec)	20	21	22	Mold
Example 4	10	108	107	106	◯
Example 5	20	118	113	113	◯
Example 6	30	125	122	123	◯
Comparative	10	114	85	87	X
Example 4
Comparative	20	123	89	91	X
Example 5
Comparative	30	131	93	94	X
Example 6

According to the present invention, since the inside of the cavity was uniformly heated by controlling the temperatures of the steam discharge passages relatively uniform, the casing mold with stable quality could be produced irrespective of using the resin-coated sand with a lower void fraction. On the other hand, in the Comparative Examples 4 to 6, the temperature distribution in the cavity became nonuniform due to the decrease in void fraction of the resin-coated sand. In addition, even when the steam supply time was extended at the maximum, sufficiently high temperatures were obtained at the steam discharge passages (21, 22). Consequently, usable casing molds were not obtained by the steam supply times adopted in the subject Comparative Examples.

Thus, the results of the subject Examples show that even when using the resin-coated sand with a low void fraction, the casting mold having the complex shape can be efficiently produced by supplying the steam for the short time period.

INDUSTRIAL APPLICABILITY

As described above, in the case of producing the casing mold having a complex shape, the present invention can achieve a remarkable effect that the resin-coated sand can be uniformly cured in the mold by increasing a supply amount of superheated steam into intricate portions. In addition, it is possible to efficiently produce the casting mold with stable quality, and flexibly cope with the production of various shapes of the casing molds, without detracting the advantages brought by the conventional method for producing the casing mold by use of the superheated steam, which is disclosed in Japanese Patent Early Publication No. 2000-107835. Thus, according to the present invention, it is expected that the method of producing the casing mold by use of the superheated steam will become more widely utilized.

Claims

1. An apparatus for producing a casting mold comprising: a mold having a cavity therein;a steam supply unit configured to supply superheated steam into said cavity;a plurality of steam discharge passages configured to discharge the superheated steam from said cavity;a flow regulator disposed at least one of said steam discharge passages to regulate an amount of the steam discharged from said cavity; anda control unit configured to control said flow regulator such that said cavity is uniformly filled with the superheated steam.

2. The apparatus as set forth in claim 1, further comprising a temperature sensor located in the vicinity of an entrance of each of said steam discharge passages, and wherein said control unit controls said flow regulator such that a temperature detected by said temperature sensor is within a predetermined temperature range.

3. The apparatus as set forth in claim 1, wherein said flow regulator comprises an electromagnetic valve, and said control unit controls an opening amount of said electromagnetic valve.

4. The apparatus as set forth in claim 1, further comprising a suction pump connected to at least one of said steam discharge passages, and wherein said control unit controls a discharge amount of said suction pump.

5. The apparatus as set forth in claim 1, wherein said flow regulator comprises an electromagnetic valve, and a suction pump is connected to a discharge port, which is formed at a confluence portion of ends of said steam discharge passages, wherein said control unit controls an opening amount of said electromagnetic valve and a discharge amount of said suction pump.

6. The apparatus as set forth in claim 1, wherein said control unit controls said flow regulator according to a void fraction of a resin-coated sand filled in said cavity.

7. A method for producing a casting mold by use of an apparatus comprising a mold having a cavity therein, a steam supply unit configured to supply superheated steam into said cavity, a plurality of steam discharge passages configured to discharge the superheated steam from said cavity, a flow regulator disposed at least one of said steam discharge passages to regulate an amount of the steam discharged from said cavity, and a control unit configured to control said flow regulator such that said cavity is uniformly filled with the superheated steam, wherein the method comprises the steps of:

8. The method as set forth in claim 7, wherein the apparatus comprises a temperature sensor located in the vicinity of an entrance of each of said steam discharge passages, and said control unit controls said flow regulator such that a temperature detected by said temperature sensor is within a predetermined temperature range.

9. The method as set forth in claim 7, wherein the apparatus comprises a suction pump connected to at least one of said steam discharge passages, and said control unit controls a discharge amount of said suction pump.

10. The method as set forth in claim 7, wherein said control unit controls said flow regulator according to a control parameter comprising at least one of a temperature in said steam discharge passage, and a void fraction of said resin-coated sand filled in said cavity.