WO2009075367A1 - レジンコーテッドサンドの温度調節ユニット及び温度調節装置 - Google Patents
レジンコーテッドサンドの温度調節ユニット及び温度調節装置 Download PDFInfo
- Publication number
- WO2009075367A1 WO2009075367A1 PCT/JP2008/072717 JP2008072717W WO2009075367A1 WO 2009075367 A1 WO2009075367 A1 WO 2009075367A1 JP 2008072717 W JP2008072717 W JP 2008072717W WO 2009075367 A1 WO2009075367 A1 WO 2009075367A1
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- WO
- WIPO (PCT)
- Prior art keywords
- gas
- ingot
- temperature
- heated
- housing
- Prior art date
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Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B22—CASTING; POWDER METALLURGY
- B22C—FOUNDRY MOULDING
- B22C19/00—Components or accessories for moulding machines
- B22C19/04—Controlling devices specially designed for moulding machines
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B22—CASTING; POWDER METALLURGY
- B22C—FOUNDRY MOULDING
- B22C13/00—Moulding machines for making moulds or cores of particular shapes
- B22C13/08—Moulding machines for making moulds or cores of particular shapes for shell moulds or shell cores
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B22—CASTING; POWDER METALLURGY
- B22C—FOUNDRY MOULDING
- B22C15/00—Moulding machines characterised by the compacting mechanism; Accessories therefor
- B22C15/23—Compacting by gas pressure or vacuum
- B22C15/24—Compacting by gas pressure or vacuum involving blowing devices in which the mould material is supplied in the form of loose particles
Definitions
- the present invention is useful for manufacturing a temperature control device used for temperature control of a resin coated sand (hereinafter referred to as “RCS”) used in manufacturing a mold by a shell mold method.
- RCS resin coated sand
- the present invention relates to a temperature control unit and a temperature control device manufactured by installing the temperature control unit in a sand hopper of a shell mold molding device (shell mold machine).
- the preheating device used in the preheating method for the shell vertical RCS as disclosed in Japanese Patent Application Laid-Open No. Sho 5 4-4 8 6 3 2 has large components and is fixed as a unit. Because it has become large and needed a large installation space. Such a large-sized shell vertical RCS preheating device has a problem in terms of energy saving because of its high energy consumption, and also lacks ease of installation. For this reason, attempts have been made to shift to preheating devices that can be easily installed in a small installation space for each shell mold making device. For example, in the apparatus disclosed in Japanese Utility Model Publication No. 5 1-1 1 6 9 15, the shell hopper RCS sand hopper and shell mold molding, which were directly connected in the conventional shell mold molding apparatus, were used.
- a device for supplying dry hot air is provided as a preheating device between the die for the shell and the blow head for supplying the shell vertical RCS.
- a preheating device in the apparatus used in the shell mold molding method disclosed in Japanese Patent Laid-Open No. 6-1 4 2 8 3 7, as a preheating device, a double-layered shell cage with an inner tank and an outer tank is used. An RCS heating device is installed, and the shell-type RCS charged in the inner tank is heated by heat exchange with steam from the multiple bubbling nozzles arranged at the bottom of the inner tank. Warm intermittent air (3 seconds at 5 second intervals) is blown up, fluidized and fluidized, heated, and then discharged from the lower discharge port of the inner tank to the mold. Yes.
- the object of the present invention is to solve the above-mentioned problems in the prior art, and to provide a small RCS temperature that can easily and economically include a temperature control device for preheating the shell vertical RCS for each shell mold molding device. It is to provide an adjustment unit. Another object of the present invention is to provide the above-mentioned temperature control unit in the sand hopper of the shell mold molding apparatus, thereby making it possible to squeeze the required amount of RCS to an appropriate temperature. An object of the present invention is to provide a temperature control device that can be processed.
- the inventors of the present invention quickly attached a gas passage at room temperature by attaching a heater to an ingot formed inside and using it as a heat exchanger.
- the present inventors have found that it can be heated to an appropriate temperature to produce warm air, and based on this knowledge, the present invention has been completed by repeating further studies to overcome the intended problem.
- the present invention includes a housing in which a plurality of heated gas blowing holes are formed, and a gas passage that is accommodated in the housing and extends from the gas introduction hole to the gas discharge hole. And a heater attached to the ingot for heating the ingot, and the gas introduced from the gas introduction hole into the gas passage is passed through the gas passage.
- the resin is heated by heat exchange with the ingot heated by the heater, and the gas heated by the ingot is discharged from the heated gas outlet hole of the housing.
- the gas passage of the ingot is preferably branched and extended from the gas introduction hole.
- the shape of the housing is an abacus bead shape.
- the temperature control unit is installed in a sand hopper to which a resin coated sand is supplied. A resin-coated sand temperature control device is provided.
- the temperature adjusting device further includes a temperature detector, and the heater is controlled based on the temperature detected by the temperature detector.
- the temperature adjustment unit according to the present invention has a gas passage provided therein. Since a heater with a heater attached is used as a heat exchanger and covered with a housing having a heated gas blowout hole, the following effects can be provided.
- the temperature control unit can be manufactured at low cost and can be miniaturized. Moreover, it requires little maintenance due to its structure.
- FIG. 1 is a longitudinal sectional view showing the structure of the temperature control unit.
- FIG. 2 is a plan view of a fixing plate for holding the heat exchanger in the housing used in the temperature control unit of Fig. 1.
- FIG. 3 is a perspective view of the heat exchanger of the temperature control unit of FIG.
- Fig. 4 is a longitudinal sectional view of the heat exchanger taken along line IV-IV in Fig. 3.
- Fig. 5 is a longitudinal sectional view showing an example of a temperature regulating device in which a temperature regulating unit is installed in the sand hopper. is there. BEST MODE FOR CARRYING OUT THE INVENTION
- FIG. 1 is a longitudinal sectional view showing an example of a temperature control unit according to the present invention.
- the temperature control unit U is composed of a metal housing (hereinafter referred to as “housing”) A and a heat exchanger B that are separable up and down.
- the heat exchanger B is held between two flanged fixing plates (for example, an iron plate) 5 inside the housing A, and the fixing plate 5 is, for example, fastened or welded using bolts and nuts. It is fixed to the housing A through a flange by an appropriate method.
- the heat exchanger B is held on the fixed plate 5 via a heat insulating material (eg, a heat insulating board) 6 as shown in FIG. 1 to minimize the transfer of heat to the fixed plate 5.
- the heat insulating material 6 is not necessarily provided.
- a gas supply pipe 1 connected to a gas supply device extends through the top of the housing A and introduces a gas that extends from the gas introduction hole of the heat exchanger B. Airtightly connected to tube 2.
- the “gas” in the present application includes not only air but also a mixture of an inert gas such as nitrogen gas and air, and the inert gas itself.
- the shape of the housing A is not particularly limited, but considering the smooth replenishment of the RCS to the fluid heating zone 10 (see FIG. 5) as will be described later, the horizontal plane may cause a natural flow of the RCS.
- the housing A has a sloped surface at an angle lower than the angle of repose at the lower part of the housing A.
- the longitudinal section of the housing A is a rhombus, an abacus bead, a parallelogram, a polygon (6 It can be made into a substantially spindle shape (a shape in which both ends of the cylinder are pointed) having a rectangular shape or an octagonal shape.
- a substantially spindle shape having a rhombus or abacus longitudinal cross section is preferable, and in particular, an abacus bead shape.
- the shape (substantially spindle shape with abacus longitudinal cross section) is preferred.
- the material of housing A is generally metal, particularly iron, from the viewpoint of cost and durability, but is not limited to this, and may be, for example, duralumin or aluminum. .
- fiber reinforced plastics such as SMC (sheet molding material) and BMC (bulk molding material) may be used.
- the angle of repose of RCS means the angle of inclination measured according to JACT test method S-5 (Food sand flow rate test method).
- heated gas blowout holes 4 for supplying hot air, that is, heated gas, for flowing and heating the RCS in the fluidized heating zone 10. are provided at desired intervals.
- the heated gas blowing hole 4 is perforated at a right angle or an acute angle (directly below) with respect to the inclined wall surface from the viewpoints of (1) to (3) below. Blowing out the heated gas can be realized.
- the shape of the heated gas blowing hole 4 is preferably a circular shape because it has a low blowing resistance (pressure loss) and is easy to process, but is not limited thereto. Furthermore, the size (diameter) of the heated gas outlet 4 is determined mainly considering the flow state of the RCS, but is preferably about 1.0 to 3.0 mm, especially 1.0 to 2. A range of 0 mm is preferred That's right.
- Such an outer surface of the housing A may be subjected to a fluorine resin processing that promotes the flow of R CS.
- the housing A itself is heated by heat radiation from the heat exchanger B as described later, the inclined wall surface of the upper portion of the housing A is also heated to the extent that it does not affect the actual RCS heating process.
- a gas blowing hole may be provided to preheat (primary heating) the unheated RCS. If importance is placed on preventing the temperature of the heated gas from decreasing, the upper part or the whole of the eight-swing A may be covered with a wear-resistant heat insulating material.
- the heat exchanger B is for introducing the gas supplied from the gas supply device through the gas supply pipe 1 and the gas introduction pipe 2 as shown in FIGS.
- An arbitrary number of gas passages 9 extending from the gas introduction hole to the gas exhaust hole 3 and an arbitrary number of heat source accommodation holes are formed inside, and a heater 7 used as a heat source is inserted into the heat source accommodation hole.
- the heater 7 used as a heat source can be a rod-shaped electric heater such as a cartridge type self-heating element type.
- the gas supplied to the heat exchanger B having such a configuration exchanges heat with the ingot C heated by the heater 7 while passing through the gas passage 9 formed inside the ingot C. Then, the air is heated (ie, warmed) and discharged into the housing A through the gas discharge hole 3 opened on the outer peripheral surface (peripheral surface, bottom surface) of the ingot C.
- the ingot C used in the present invention is used as a heat exchange medium, it is required to be formed of a material that is easy to transfer heat and is difficult to cool.
- the material of ingot C is preferably an alloy mainly composed of non-ferrous metals such as aluminum and magnesium.
- an aluminum alloy is preferable.
- the shape of the ingot C is not particularly limited, and for example, a plate shape, a prismatic shape (cube, rectangular parallelepiped shape), a columnar shape, a spherical shape, a solid body with a tip portion cut and removed (a truncated cone, a truncated pyramid shape), etc.
- a cylindrical shape is particularly suitable.
- the position where the gas introduction hole is provided is not particularly limited, and on the outer peripheral surface (upper surface, peripheral surface, bottom surface) of the ingot C so as to express the maximum heat exchange efficiency.
- An appropriate position is selected, but it is preferable to select the top surface of ingot C from the viewpoint of ease of processing.
- the shape of the gas passage 9 continuing below the gas introduction hole is not particularly limited.
- a branched shape (a shape branched into a plurality of gas passages), a spiral shape, A bellows shape or the like may be appropriately selected in light of the shape of the ingot C.
- a branched passage is particularly preferable. That is, the ingot C is provided with one gas introduction hole and a plurality of gas discharge holes 3, and a plurality of gas passages 9 branch from the one gas introduction hole to reach each gas discharge hole 3. preferable.
- the manufacturing method of the heat source storage hole and the gas passage 9 as described above is not particularly limited, and for example, the following methods (1) to (3) can be adopted. From the viewpoint of easiness and heat exchange efficiency, the method (3) that can increase the surface area of the passage by tapping is particularly preferable.
- the size or size of the gas passage 9 is limited by the size of the drill blade or tap blade, and is generally selected from the range of 5 to 15 mm, but should be about 10 mm. Is preferred.
- FIG. 3 is a perspective view of the heat exchanger of FIG. 1
- FIG. 4 is a longitudinal sectional view of the heat exchanger along the line I V _IV of FIG.
- Ingot C is made of an aluminum alloy, and this ingot has a cylindrical shape with a diameter of 200 mm and a height of 200 mm.
- a gas introduction hole to which the gas introduction pipe 2 is connected is formed at the center of the upper surface of the ingot.
- gas discharge holes (outer periphery of the ingot C) are formed on the peripheral surface (outer peripheral surface and bottom surface) of the ingot C extending from the gas introduction hole.
- a gas passage 9 is formed to reach four gas discharge holes 3 at the bottom of the surface and four gas discharge holes 3 at the bottom.
- heat source storage holes are further formed at appropriate positions so that the temperature distribution due to heating of the heater 7 does not vary, and each of the heat source storage holes has a capacity of 3 kWh.
- a heater 7 having an output is inserted.
- the heating by the heater 7 keeps the ingot C at a required temperature (for example, about 1550 ⁇ 5), and the gas flowing through the gas passage 9 is exchanged with the ingot C by heat exchange. Heated into hot air, that is, heated gas (for example, approximately 60 ⁇ 5), and discharged / supplied into the housing A from the gas discharge hole 3 formed on the peripheral surface of the ingot C It has become.
- a gas introduction hole to which the gas introduction pipe 2 is connected is formed in the center of the upper surface of the ingot C, and the ingot line is connected as shown in FIG.
- Eight upper vertical holes (in the direction of the central axis of the cylindrical ingot C) at a position where a cross is formed with the gas introduction hole as the base point on the upper surface (two symmetrically on the left and right and front and back across the gas introduction hole) A hole extending to the top).
- the upper vertical holes one upper horizontal hole formed so as to extend in the diametrical direction at the upper end part of the four upper vertical holes and the lower end part of the gas introduction hole aligned in the diameter direction.
- the bottom side of the ingot C has a short lower side so as to communicate with each lateral hole formed in the lower part of the ingot C at a position not aligned with the upper vertical hole extending from the top surface of the ingot C. Drill a vertical hole.
- the upper end portion of the upper vertical hole and the both end portions of the upper horizontal hole thus formed are sealed with a plug. Specifically, as shown in FIGS.
- the four heat source storage holes should not cross the upper side hole and the lower side hole at an appropriate position where the temperature distribution due to heating of the heater 7 does not vary and avoid the upper side hole. It is formed by drilling a vertical hole from the top surface of ingot C.
- the conditions of the gas supplied from the gas supply device are not particularly limited, but preferably the RCS in the fluid heating zone 10 is in a light flow state. In some cases, it is sufficient to have a blowing pressure and an air volume that can be maintained in a state of a slight blowing flow.
- a gas supply device include a compressor, a blower and a pressure cap.
- gas for example, compressed air
- the pressure is determined in accordance with the flow state of the RCS in the fluid heating zone 10, but is generally about 0.1 to 0.5 MPa, preferably 0.:! To 0. 2 MP a.
- the air volume may be adjusted according to the flow state of the RCS while paying attention to the occurrence of a short path, but is generally about 20 to 100 LZ.
- the supplied gas is preferably a dry gas such as dry air dehumidified by an arbitrary dehumidifier.
- the gas supply may be continuous or intermittent.
- FIG. 5 is a longitudinal sectional view showing an example of the temperature control device.
- Sand hopper D has been modified as a temperature control device by installing and fixing the temperature control unit U so that a space is formed as a fluid heating zone 10 between them.
- the RCS in the sand hopper D is covered by the heated gas discharge hole 4 on the inclined wall surface of the lower part of the housing A of the temperature control unit U. After being heated to a specified temperature while flowing or flowing with heated gas (hot air), it is discharged from the discharge port 12 of the sand hopper D into the blow head (not shown) of the molding device for shell mold. Become so.
- the RCS amount in the fluidized heating zone 10 is determined by adjusting the distance between the inner wall surface of the reduced diameter section 1 1 and the outer wall surface of the housing A of the temperature control unit U. It is adjusted to about 0 to 50 mm, preferably 25 to 35 mm.
- the heat treatment of RCS is determined according to the RCS required amount (2 to 3 times the RCS amount required for molding), and then the temperature of the heated gas (hot air) as described above and the blowing conditions
- the flow state of RCS, heating efficiency, etc. are adjusted according to (pressure, air volume, etc.).
- the temperature control device in Fig. 5 is a mechanism in which RCS is replenished sequentially from the top to the fluidized heating zone 10 as RCS is discharged after heat treatment, so both continuous molding and intermittent molding are possible. You are able to follow.
- the R CS amount corresponding to the volume of the fluid heating zone 10 is repeatedly heated, the R C S heat treatment can be performed quickly and uniformly and more efficiently than a large apparatus. Therefore, when waiting for the molding operation to resume, there is no long waiting time as in the case of a large device, and the waiting time can be eliminated.
- Sand hopper D is covered with an appropriate heat insulating material. As a result, heat treatment efficiency in the fluidized heating zone 10 is improved and RCS preheating (primary heating) is achieved by using waste heat from hot air.
- the above temperature control device it is formed between the inner wall surface of the reduced diameter portion 11 of the sand hopper D and the inclined outer wall surface of the lower portion of the housing A of the temperature control unit U. Since the mechanism to optimize the temperature of the shell vertical RCS in the fluidized heating zone is adopted, the following effects can be provided.
- the fluid heating zone 10 employs a mechanism in which unheated RCS is replenished from the top as the RCS for shell vertical molds is discharged after heat treatment. Heat treatment can be performed continuously while discharging in small increments.
- the RCS temperature measured by the temperature sensor 1 3 provided in the flow heating zone 10 as a temperature detector is converted into an electric signal (current or voltage). And the converted electric signal is taken into a temperature control device (not shown), and the operation of the heater 7 provided in the ingot C (heat exchanger B) is controlled by the temperature control device. Ingot C is maintained at a predetermined temperature.
- the temperature sensor 1 13 is provided in the fluid heating zone 10 and the temperature sensor 1 13 measures the temperature of the RCS in the fluid heating zone 10, but is shown in FIG. As shown in the figure, instead of or in addition to the temperature sensor 1 3 provided in the fluidized heating zone 10, the temperature range in the temperature sensor 1 3 and the outlet 1 2 attached to the housing A of the temperature control unit U The temperature sensor 1 3 is used to control the operation of the heater 7 so that the temperature of the temperature control unit U or the temperature of the RCS discharged from the outlet 1 2 falls within a predetermined temperature range. It may be.
- RCS is generally heated to about 40 to 70, preferably about 50 to 65, depending on the RCS temperature control apparatus and the temperature control method used therein according to the present invention.
- the obtained R CS can not only be improved in molding and quality, but also can be stably molded without being affected by the environmental temperature.
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Priority Applications (1)
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CN2008801204526A CN101896297B (zh) | 2007-12-11 | 2008-12-08 | 树脂覆膜砂的温度调节单元和温度调节装置 |
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JP2007320118A JP5173387B2 (ja) | 2007-12-11 | 2007-12-11 | レジンコーテッドサンドの温度調節ユニット及び温度調節装置 |
JP2007-320118 | 2007-12-11 |
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WO2009075367A1 true WO2009075367A1 (ja) | 2009-06-18 |
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PCT/JP2008/072717 WO2009075367A1 (ja) | 2007-12-11 | 2008-12-08 | レジンコーテッドサンドの温度調節ユニット及び温度調節装置 |
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JP (1) | JP5173387B2 (ja) |
CN (1) | CN101896297B (ja) |
WO (1) | WO2009075367A1 (ja) |
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JP6687400B2 (ja) * | 2016-01-26 | 2020-04-22 | リグナイト株式会社 | 鋳型製造装置 |
JP6687399B2 (ja) * | 2016-01-26 | 2020-04-22 | 株式会社大阪シェル | 鋳物砂の加熱装置 |
Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS59191540A (ja) * | 1983-04-14 | 1984-10-30 | Naniwa Seisakusho:Kk | 鋳型造型用砂の加温器 |
JP2001321886A (ja) * | 2000-05-18 | 2001-11-20 | Asahi Organic Chem Ind Co Ltd | 粉粒体の温度調節ユニット及びこれを用いた温度調節装置 |
-
2007
- 2007-12-11 JP JP2007320118A patent/JP5173387B2/ja active Active
-
2008
- 2008-12-08 CN CN2008801204526A patent/CN101896297B/zh active Active
- 2008-12-08 WO PCT/JP2008/072717 patent/WO2009075367A1/ja active Application Filing
Patent Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS59191540A (ja) * | 1983-04-14 | 1984-10-30 | Naniwa Seisakusho:Kk | 鋳型造型用砂の加温器 |
JP2001321886A (ja) * | 2000-05-18 | 2001-11-20 | Asahi Organic Chem Ind Co Ltd | 粉粒体の温度調節ユニット及びこれを用いた温度調節装置 |
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Publication number | Publication date |
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CN101896297B (zh) | 2012-06-13 |
JP2009142830A (ja) | 2009-07-02 |
CN101896297A (zh) | 2010-11-24 |
JP5173387B2 (ja) | 2013-04-03 |
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