JP2013146741A - Solution treatment furnace - Google Patents

Solution treatment furnace Download PDF

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JP2013146741A
JP2013146741A JP2012007089A JP2012007089A JP2013146741A JP 2013146741 A JP2013146741 A JP 2013146741A JP 2012007089 A JP2012007089 A JP 2012007089A JP 2012007089 A JP2012007089 A JP 2012007089A JP 2013146741 A JP2013146741 A JP 2013146741A
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sand
casting
heat treatment
furnace
treatment furnace
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JP5890183B2 (en
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Hideo Hoshiyama
英男 星山
Nobuki Matsuo
伸樹 松尾
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Honda Motor Co Ltd
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Abstract

PROBLEM TO BE SOLVED: To provide a solution treatment furnace that enables regeneration of core sand through the use of heat on heat treatment, while tar caused by burning of an organic binder is removed at the same time as an aluminum casting is subjected to solution treatment.SOLUTION: A solution treatment furnace, in which an aluminum casting cast by a die provided with a sand core is subjected to solution treatment, includes: a first heat treating furnace having an inlet to which a casting before shakeout after casting is input; a second heat treating furnace having an outlet; a shutter provided between the first heat treating furnace and the second treating furnace; a conveyer for casting transportation that transports the casting from the inlet to the outlet; and a conveyer for sand transportation provided under the conveyer for casting transportation in the first heat treating furnace. The conveyer for casting transportation is configured to have a mesh structure on a surface where the casting is placed, and causes the core sand when the sand core is collapsed to pass through downward and then fall onto the conveyer for sand transportation.

Description

本発明は、鋳造品に対して溶体化を行う溶体化炉に係り、特に、溶体化と同時に中子砂の再生を行う溶体化炉に関するものである。   The present invention relates to a solution furnace for solutionizing cast products, and more particularly to a solution furnace for regenerating core sand at the same time as solution forming.

例えば、エンジンのシリンダヘッドにおいては、吸気ポート、排気ポート、ウォータージャケット等の複雑な形状を有する空洞部が形成されている。このような複雑な空洞部を有する製品は、金型内部に予め砂中子を用いて鋳造することにより製造される。この砂中子における中子砂は、従来から、天然の砂粒を骨材とし、その表面に有機バインダを塗工した中子砂が使用されている。   For example, in a cylinder head of an engine, a hollow portion having a complicated shape such as an intake port, an exhaust port, or a water jacket is formed. A product having such a complicated cavity is manufactured by casting in advance inside a mold using a sand core. As the core sand in the sand core, conventionally, core sand in which natural sand particles are used as an aggregate and an organic binder is applied on the surface thereof has been used.

従来、このような砂中子を用いた鋳造品においては、鋳造終了後に鋳造品を室温近くにまで冷却し、砂中子を構成していた砂を鋳造品から排出し、その後、溶体化のために再加熱される。しかしながら、これらの工程では、エネルギーロスが多く、実用上問題を有するものであった。そこで、この問題を解決する方法として、鋳造品の熱を利用して、降温前に熱処理炉に投入することで、エネルギーロスを削減する鋳物製品の製造方法が開発されている(例えば、特許文献1参照)。特許文献1における技術は、鋳造品を冷却することなく、固化直後の溶湯の余熱(400℃〜500℃)を利用して熱処理炉で焼き入れ処理及び焼き戻し処理を行うと同時に、砂中子の粘結剤を溶湯の熱で崩壊させて砂落しを行う方法である。   Conventionally, in a cast product using such a sand core, the cast product is cooled to near room temperature after the casting is finished, and the sand constituting the sand core is discharged from the cast product, and then the solution is formed. To be reheated. However, these processes have many energy losses and have practical problems. Therefore, as a method for solving this problem, a casting product manufacturing method has been developed that uses the heat of the casting product and puts it in a heat treatment furnace before cooling down to reduce energy loss (for example, Patent Documents). 1). The technology in Patent Document 1 uses a residual heat (400 ° C. to 500 ° C.) of the molten metal immediately after solidification to perform quenching and tempering treatment in a heat treatment furnace without cooling the casting, and at the same time, sand core. This is a method of removing sand by disintegrating the binder with the heat of the molten metal.

ところが、上記技術においては、単に鋳造後に冷却することなく熱処理と砂落しを同時に行うだけでは、砂中子に用いられている粘結剤を焙焼した際に発生するヤニにより、熱処理炉が損傷するおそれがあった。   However, in the above technology, if the heat treatment and the sand removal are simultaneously performed without cooling after casting, the heat treatment furnace is damaged due to the resin generated when the binder used in the sand core is roasted. There was a risk.

また、最近時では、砂中子に用いた中子砂を再利用することで、コスト削減を図る試みがなされている。このような鋳造品から排出された中子砂を再利用するためには、砂の表面についた有機バインダを完全に除去する必要がある。しかしながら、従来の中子砂は、骨材の砂粒が球形ではなく、さらに、表面に凹凸を有する形状であるため、中子砂を焙焼により再生しても、表面の有機バインダが剥がれにくく、そのため、有機バインダごと表面を研磨する工程も必要であった。また、従来の中子砂は、天然の砂粒であるため、不均一組成で破砕性が悪く、熱処理時の膨張変態で割れ易いといった問題も有していた。   Recently, attempts have been made to reduce costs by reusing the core sand used for the sand core. In order to reuse the core sand discharged from such a cast product, it is necessary to completely remove the organic binder attached to the surface of the sand. However, in the conventional core sand, the aggregate sand particles are not spherical, and since the surface has irregularities, even if the core sand is regenerated by baking, the organic binder on the surface is difficult to peel off, Therefore, the process of grind | polishing the surface with an organic binder was also required. In addition, since conventional core sand is natural sand grains, it has a problem that it has a non-uniform composition and poor crushability, and is easily cracked by expansion transformation during heat treatment.

特開平6−210437号公報JP-A-6-210437

したがって、本発明は、上記課題を解決すべくなされたものであって、アルミニウム鋳造品の溶体化と同時に、有機バインダの焙焼により生じるヤニを除去しつつ、熱処理の熱を利用した中子砂の再生を可能とした溶体化炉を提供することを目的としている。   Accordingly, the present invention has been made to solve the above-described problems, and is a core sand that utilizes heat of heat treatment while removing a cast caused by roasting of an organic binder simultaneously with solutionization of an aluminum cast product. An object of the present invention is to provide a solution furnace capable of regenerating the steel.

本発明の溶体化炉は、砂中子を備えた金型によって鋳造されたアルミニウム鋳造品を溶体化する溶体化炉であって、鋳造後の砂落とし前の鋳造品を投入する投入口が設けられた第一熱処理炉と、排出口が設けられた第二熱処理炉と、上記第一熱処理炉と第二熱処理炉との間に設けられたシャッターと、上記投入口から上記排出口まで鋳造品を搬送する鋳造品搬送用コンベヤと、上記第一熱処理炉内の上記鋳造品搬送用コンベヤの下方に設けられた砂搬送用コンベヤとを備え、上記鋳造品搬送用コンベヤは、鋳造品を載置する面がメッシュ状構造を有し、砂中子が崩壊された際の中子砂を下方へ通過させ、上記砂搬送用コンベヤ上に落下させるよう構成されていることを特徴としている。   The solution furnace of the present invention is a solution furnace for solutionizing an aluminum cast product cast by a mold having a sand core, and is provided with an input port for introducing a cast product after casting and before sand removal. A first heat treatment furnace, a second heat treatment furnace provided with a discharge port, a shutter provided between the first heat treatment furnace and the second heat treatment furnace, and a cast product from the input port to the discharge port. A casting product transporting conveyor, and a sand transporting conveyor provided below the casting product transporting conveyor in the first heat treatment furnace, the casting product transporting conveyor placing a casting product The surface has a mesh-like structure, and is configured to allow the core sand when the sand core is collapsed to pass downward and to drop onto the sand conveying conveyor.

本発明の溶体化炉によれば、第一熱処理炉及び第二熱処理炉を通してアルミニウム鋳造品の溶体化を行うと同時に、第一熱処理炉において、有機バインダの焙焼により生じるヤニを除去しつつ、熱処理の熱を利用した中子砂の再生を行うことができる。   According to the solution heat treatment furnace of the present invention, while the solution heat treatment of the aluminum casting product is performed through the first heat treatment furnace and the second heat treatment furnace, at the same time, in the first heat treatment furnace, while removing the spear caused by roasting of the organic binder, The core sand can be regenerated using the heat of the heat treatment.

また、本発明の溶体化炉においては、空気排出口及び空気供給口が、前記第一熱処理炉の上部及び下部にそれぞれ設けられ、さらに、上記空気排出口から排出された空気を加熱する加熱手段が備えられ、上記第一熱処理炉内の空気を循環及び加熱することが好ましい。この態様によれば、空気排出口から排出された第一熱処理炉内の空気を、加熱手段により加熱し、第一熱処理炉内の空気中に含まれるヤニを熱分解させ、その後、ヤニが熱分解された空気を空気供給口から再び第一熱処理炉内へ戻し、第一熱処理炉内のヤニを取り除くことができる。   In the solution furnace of the present invention, an air discharge port and an air supply port are provided at the upper and lower portions of the first heat treatment furnace, respectively, and heating means for heating the air discharged from the air discharge port It is preferable to circulate and heat the air in the first heat treatment furnace. According to this aspect, the air in the first heat treatment furnace discharged from the air discharge port is heated by the heating means to thermally decompose the ani included in the air in the first heat treatment furnace, and then the ani is heated. The decomposed air can be returned to the first heat treatment furnace again from the air supply port, and the dust in the first heat treatment furnace can be removed.

さらに、前記鋳造品搬送用コンベヤ及び前記砂搬送用コンベヤは、搬送方向及び搬送速度を同一に設定することが好ましい。このような構成によれば、第二加熱処理炉内に中子砂が持ち込まれることを防ぐことができる。   Furthermore, it is preferable that the casting product conveying conveyor and the sand conveying conveyor have the same conveying direction and conveying speed. According to such a configuration, core sand can be prevented from being brought into the second heat treatment furnace.

また、前記第一熱処理炉は、前記砂搬送用コンベヤによって搬送された中子砂を排出する砂用排出口を備えていることが好ましい。このような態様によれば、再生された中子砂を容易に砂用排出口から炉外へ脇出しすることができる。   Moreover, it is preferable that said 1st heat processing furnace is equipped with the discharge port for sand which discharges | emits the core sand conveyed by the said conveyor for sand conveyance. According to such an aspect, the regenerated core sand can be easily put out of the furnace through the sand discharge port.

本発明によれば、アルミニウム鋳造品の溶体化と同時に、有機バインダの焙焼により生じるヤニを除去しつつ、熱処理の熱を利用した中子砂の再生を可能とした溶体化炉を提供することができる。   According to the present invention, it is possible to provide a solution furnace capable of regenerating core sand using heat of heat treatment while removing the resin generated by roasting of an organic binder simultaneously with solution forming of an aluminum casting product. Can do.

本発明の溶体化炉の一実施形態を示した横断面図である。It is the cross-sectional view which showed one Embodiment of the solution heat treatment furnace of this invention. 本発明の溶体化炉の一実施形態を示した縦断面図である。It is the longitudinal cross-sectional view which showed one Embodiment of the solution heat treatment furnace of this invention.

以下、図面を用いて本発明の溶体化炉について具体的に説明する。図1は本発明の溶体化炉の一実施形態を示した横断面図であり、図2は本発明の溶体化炉の一実施形態を示した縦断面図である。   Hereinafter, the solution furnace of the present invention will be specifically described with reference to the drawings. FIG. 1 is a transverse sectional view showing an embodiment of the solution furnace of the present invention, and FIG. 2 is a longitudinal sectional view showing an embodiment of the solution furnace of the present invention.

本発明の溶体化炉1は、砂中子を備えた金型によって鋳造されたアルミニウム鋳造品2を溶体化すると同時に、溶体化処理の熱を利用して中子砂の表面を被覆している有機バインダを焙焼することにより中子砂を再生することができる溶体化炉である。図1に示されているように、本発明の溶体化炉1においては、鋳造品2の搬送方向に沿って第一熱処理炉3及び第二熱処理炉4が設けられており、第一熱処理炉3の上流側の側面及び第二熱処理炉4の下流側の側面には、それぞれ開閉自在に開口された投入口5及び排出口6が設けられている。そして、この投入口5から排出口6にわたって鋳造品搬送用コンベヤ7が備えられ、鋳造後の砂落とし前の鋳造品2を投入口5から投入すると、溶体化処理の後、排出口6から砂が除去された鋳造品2が搬出される。   The solution furnace 1 of the present invention forms a cast aluminum product 2 cast by a mold having a sand core and simultaneously coats the surface of the core sand using the heat of solution treatment. This is a solution furnace capable of regenerating core sand by roasting an organic binder. As shown in FIG. 1, in the solution furnace 1 of the present invention, a first heat treatment furnace 3 and a second heat treatment furnace 4 are provided along the conveying direction of the cast product 2. 3, an inlet 5 and an outlet 6 that are openable and closable are provided on the side of the upstream side 3 and the side of the downstream side of the second heat treatment furnace 4, respectively. A casting product conveyor 7 is provided from the charging port 5 to the discharging port 6, and when the cast product 2 before sand removal after casting is charged from the charging port 5, sand is discharged from the discharging port 6 after the solution treatment. The removed casting 2 is carried out.

また、上記の第一熱処理炉3内には、鋳造品搬送用コンベヤ7の下方において、鋳造品搬送用コンベヤ7と平行に砂搬送用コンベヤ8が備えられ、鋳造品搬送用コンベヤ7による鋳造品2の搬送速度と同一速度で中子砂9が搬送される。さらに、上記の鋳造品搬送用コンベヤ7は、鋳造品2を載置する面がメッシュ状構造を有し、砂中子が崩壊された際の中子砂9を下方へ通過させ、砂搬送用コンベヤ8上に落下させるよう構成されている。   In the first heat treatment furnace 3, a sand transporting conveyor 8 is provided below the casting product transporting conveyor 7 in parallel with the casting product transporting conveyor 7. The core sand 9 is transported at the same speed as the transport speed 2. Further, the casting product conveying conveyor 7 has a mesh structure on the surface on which the casting product 2 is placed, and allows the core sand 9 when the sand core is collapsed to pass downward. It is configured to drop onto the conveyor 8.

このような構成の本発明の溶体化炉1においては、まず、砂中子を備えた金型によって鋳造されたアルミニウム鋳造品2が、鋳造品搬送用コンベヤ7により搬送されて投入口5から第一熱処理炉3内に投入さる。そして、約500℃に加熱された溶体化炉1内で熱処理が開始されると、鋳造品2内の砂中子を構成する中子砂9の表面を被覆している有機バインダが焙焼され、砂中子が中子砂9に崩壊される。すると、崩壊された中子砂9が鋳造品2内から崩れ落ち、鋳造品搬送用コンベヤ7の載置面のメッシュ状構造を通過して、下方に配置された砂搬送用コンベヤ8上に落下する。この際、落下した中子砂9は、焙焼によって表面から有機バインダが完全に取り除かれた状態であることが好ましいが、まだ有機バインダが残っている場合においても、炉内温度が約500℃であることから、砂搬送用コンベヤ8による搬送の間にも有機バインダの焙焼が継続され、中子砂9の再生がさらに進められる。ここで、本発明の溶体化炉1においては、鋳造品を任意方向へ回転させる機構、鋳造品の砂排出穴へ熱風を吹き込む機構等、鋳造品2から砂中子を積極的に崩壊落下させる手段を備えてもよい。   In the solution furnace 1 of the present invention having such a configuration, first, an aluminum casting 2 cast by a mold having a sand core is transported by a casting transporting conveyor 7 and is fed from the inlet 5 to the first. One heat treatment furnace 3 is charged. When the heat treatment is started in the solution furnace 1 heated to about 500 ° C., the organic binder covering the surface of the core sand 9 constituting the sand core in the casting 2 is roasted. The sand core is collapsed into the core sand 9. Then, the collapsed core sand 9 collapses from the cast product 2, passes through the mesh-like structure on the placing surface of the cast product transport conveyor 7, and falls onto the sand transport conveyor 8 disposed below. . At this time, the core sand 9 that has fallen is preferably in a state in which the organic binder has been completely removed from the surface by roasting, but even when the organic binder still remains, the furnace temperature is about 500 ° C. Therefore, roasting of the organic binder is continued during the conveyance by the sand conveying conveyor 8, and the core sand 9 is further regenerated. Here, in the solution furnace 1 of the present invention, the sand core is actively collapsed and dropped from the casting 2 such as a mechanism for rotating the casting in an arbitrary direction and a mechanism for blowing hot air into the sand discharge hole of the casting. Means may be provided.

また、このような砂搬送用コンベヤ8上の有機バインダ焙焼を促進するために、砂搬送用コンベヤ8上の中子砂9に対して熱風を吹き付ける方法、流動床のように下側から熱風を吹き上げる方法等により、中子砂9を攪拌することもできる。その後、再生された中子砂9は、砂用排出口10から炉外へ脇出しされる。なお、第一熱処理炉3内における中砂子9の滞在時間としては、イグロス(砂表面の有機汚れ分)が完全に無くなるまでの時間以上であり、砂の種類や大きさ、バインダの種類や被覆厚さ等に応じて変更する必要がある。さらに、本発明の溶体化炉においては、鋳造品搬送用コンベヤ7及び砂搬送用コンベヤ8は、搬送方向及び搬送速度を同一に設定することが好ましい。このような構成によれば、第二加熱処理炉4内に中子砂9が持ち込まれることを防ぐことができる。   Further, in order to promote such organic binder roasting on the sand transporting conveyor 8, a method of blowing hot air against the core sand 9 on the sand transporting conveyor 8, hot air from the lower side like a fluidized bed. The core sand 9 can also be agitated by a method of blowing up. Thereafter, the regenerated core sand 9 is put out of the furnace through the sand discharge port 10. The staying time of the medium sand piece 9 in the first heat treatment furnace 3 is longer than the time until Iglos (organic dirt on the sand surface) is completely eliminated, and the type and size of the sand, the type of the binder and the coating It is necessary to change according to thickness etc. Furthermore, in the solution furnace of the present invention, it is preferable that the casting product conveyor 7 and the sand conveyor 8 have the same conveying direction and conveying speed. According to such a configuration, it is possible to prevent the core sand 9 from being brought into the second heat treatment furnace 4.

さらに、上記の第一熱処理炉3と第二熱処理炉4との間には開閉自在なシャッター11が備えられており、加熱された空気をそれぞれの炉内で循環するよう構成されている。上述したような有機バインダの焙焼では、有機バインダが完全に揮発されずに、タール状のヤニとなって炉内に付着し、炉に損傷を与えるおそれがある。そのため、このようなヤニへの対策として、上記のようなシャッター11を備えることにより、第二加熱炉4にヤニが入り込むのを防止することができる。   Further, a shutter 11 that can be freely opened and closed is provided between the first heat treatment furnace 3 and the second heat treatment furnace 4, and is configured to circulate the heated air in each furnace. In the roasting of the organic binder as described above, the organic binder is not completely volatilized and becomes tar-like scum and adheres to the furnace, which may damage the furnace. Therefore, by providing the shutter 11 as described above as a measure against such a spear, it is possible to prevent the spear from entering the second heating furnace 4.

また、第一熱処理炉3においては、図2に示されるように、圧縮空気供給手段12を設けることが好ましい。この圧縮空気供給手段12は、炉内の雰囲気酸素濃度を濃くして、有機バインダの焙焼を促進することにより、ヤニの発生を低減させることができる。この際、圧縮空気供給手段12により供給される圧縮空気は、炉内に到達するまでに炉の廃熱等を利用して加熱されていることが好ましく、これにより、第一熱処理炉3内におけるエネルギーロスを避けることができる。   Further, in the first heat treatment furnace 3, it is preferable to provide a compressed air supply means 12 as shown in FIG. This compressed air supply means 12 can reduce the generation of spear by increasing the atmospheric oxygen concentration in the furnace and promoting the roasting of the organic binder. At this time, the compressed air supplied by the compressed air supply means 12 is preferably heated by using waste heat of the furnace or the like before reaching the inside of the furnace. Energy loss can be avoided.

さらに、本発明の溶体化炉1においては、空気排出口13及び空気供給口14が、第一熱処理炉3の上部及び下部にそれぞれ設けられ、さらに、空気排出口13から排出された空気を加熱する加熱手段15、及び、空気排出口13から空気供給口14へ空気を送るポンプ16が備えられていることが好ましい。ここで、有機バインダの焙焼により発生するヤニは空気より軽く、上方に滞留する傾向があるため、空気排出口13を第一熱処理炉3の上部に、また、上記の圧縮空気供給手段12及び空気供給口14を第一熱処理炉3の下部に設ける必要がある。   Furthermore, in the solution furnace 1 of the present invention, the air discharge port 13 and the air supply port 14 are respectively provided at the upper and lower portions of the first heat treatment furnace 3, and further heat the air discharged from the air discharge port 13. It is preferable that a heating unit 15 that performs the heating and a pump 16 that sends air from the air discharge port 13 to the air supply port 14 are provided. Here, the resin generated by roasting of the organic binder is lighter than air and tends to stay upward, so that the air discharge port 13 is located above the first heat treatment furnace 3 and the compressed air supply means 12 and It is necessary to provide the air supply port 14 in the lower part of the first heat treatment furnace 3.

このような構成においては、ポンプ16により第一熱処理炉3内の空気が空気排出口13から排出され、加熱手段15に送られ、加熱手段15により約700〜800℃の温度に加熱される。これにより、第一熱処理炉3内の空気中に含まれるヤニを熱分解させ、その後、ヤニが熱分解された空気が空気供給口14から再び第一熱処理炉3内へ戻され、第一熱処理炉3内のヤニが取り除かれる。   In such a configuration, the air in the first heat treatment furnace 3 is discharged from the air discharge port 13 by the pump 16, sent to the heating means 15, and heated to a temperature of about 700 to 800 ° C. by the heating means 15. Thereby, the spear contained in the air in the first heat treatment furnace 3 is pyrolyzed, and then the air in which the spear is pyrolyzed is returned to the first heat treatment furnace 3 from the air supply port 14 again. Any dirt in the furnace 3 is removed.

次いで、砂中子を崩壊により取り除いたアルミニウム鋳造品2は、第一熱処理炉3と第二熱処理炉4との間に設けられたシャッター11を適切に開き、鋳造品搬送用コンベヤ7により下流側へ搬送されて第二熱処理炉4内に送られる。第二熱処理炉4内においては、中子砂9が完全に取り除かれた鋳造品2を、有機バインダの焙焼により発生するヤニが含まれない雰囲気下で約500℃に加熱され、溶体化処理が継続される。このように、本発明の溶体化炉によれば、アルミニウム鋳造品の溶体化と同時に、有機バインダの焙焼により生じるヤニを除去しつつ、熱処理の熱を利用した中子砂の再生をすることができる。   Next, the aluminum casting 2 from which the sand core has been removed by collapsing is appropriately opened by the shutter 11 provided between the first heat treatment furnace 3 and the second heat treatment furnace 4, and the casting product conveyer 7 is provided on the downstream side. To the second heat treatment furnace 4. In the second heat treatment furnace 4, the cast product 2 from which the core sand 9 has been completely removed is heated to about 500 ° C. in an atmosphere that does not contain any spear generated by roasting of the organic binder, and is subjected to a solution treatment. Will continue. Thus, according to the solution furnace of the present invention, the core sand is regenerated using the heat of the heat treatment while removing the resin generated by roasting of the organic binder simultaneously with the solution forming of the aluminum casting product. Can do.

また、本発明の溶体化炉においては、砂中子に用いる中子砂が天然の砂粒を骨材としたものではなく、真球度が高く表面が平滑な骨材、例えば、人工砂をAl,SiOの燃焼火炎溶融で生成した骨材等を使用することが好ましい。このような骨材は、表面が平滑であるため、表面性状が維持されやすく、また、成分が均一であるため、硬度が高く、さらに、鋳造/再生温度で変態点を持たないため、割れにくいといった利点を有している。また、上記のような骨材を用いると、表面に塗工される有機バインダ量を減らすことができ、排砂性が向上される。これにより、溶体化処理時の加熱によって容易に中子砂を排出することができ、炉内に排出された砂に残留する有機バインダを溶体化処理の加熱で分解することができる。 In the solution furnace of the present invention, the core sand used for the sand core is not made of natural sand grains, but aggregates with high sphericity and a smooth surface, for example, artificial sand are made of Al. It is preferable to use an aggregate or the like generated by 2 O 3 or SiO 3 combustion flame melting. Since such an aggregate has a smooth surface, the surface properties are easily maintained, and since the components are uniform, the hardness is high, and furthermore, since there is no transformation point at the casting / regeneration temperature, it is difficult to break. It has the following advantages. Moreover, when the aggregates as described above are used, the amount of the organic binder applied to the surface can be reduced, and sand discharge performance is improved. Thereby, the core sand can be easily discharged by heating at the time of the solution treatment, and the organic binder remaining in the sand discharged into the furnace can be decomposed by the heat of the solution treatment.

1…溶体化炉、2…鋳造品、3…第一熱処理炉、4…第二熱処理炉、5…投入口、
6…排出口、7…鋳造品搬送用コンベヤ、8…砂搬送用コンベヤ、9…中子砂、
10…砂用排出口、11…シャッター、12…圧縮空気供給手段、13…空気排出口、
14…空気供給口、15…加熱手段、16…ポンプ
DESCRIPTION OF SYMBOLS 1 ... Solution furnace, 2 ... Cast article, 3 ... 1st heat treatment furnace, 4 ... 2nd heat treatment furnace, 5 ... Input port,
6 ... discharge port, 7 ... conveyor for casting products, 8 ... conveyor for sand transport, 9 ... core sand,
DESCRIPTION OF SYMBOLS 10 ... Sand discharge port, 11 ... Shutter, 12 ... Compressed air supply means, 13 ... Air discharge port,
14 ... Air supply port, 15 ... Heating means, 16 ... Pump

Claims (4)

砂中子を備えた金型によって鋳造されたアルミニウム鋳造品を溶体化する溶体化炉であって、
鋳造後の砂落とし前の鋳造品を投入する投入口が設けられた第一熱処理炉と、
排出口が設けられた第二熱処理炉と、
上記第一熱処理炉と第二熱処理炉との間に設けられたシャッターと、
上記投入口から上記排出口まで鋳造品を搬送する鋳造品搬送用コンベヤと、
上記第一熱処理炉内の上記鋳造品搬送用コンベヤの下方に設けられた砂搬送用コンベヤとを備え、
上記鋳造品搬送用コンベヤは、鋳造品を載置する面がメッシュ状構造を有し、砂中子が崩壊された際の中子砂を下方へ通過させ、上記砂搬送用コンベヤ上に落下させるよう構成されていることを特徴とする溶体化炉。
A solution furnace for solutionizing an aluminum casting cast by a mold having a sand core,
A first heat treatment furnace provided with an inlet for introducing a cast product before casting after casting,
A second heat treatment furnace provided with a discharge port;
A shutter provided between the first heat treatment furnace and the second heat treatment furnace;
A casting product conveyor for conveying the casting product from the inlet to the outlet;
A sand transport conveyor provided below the cast product transport conveyor in the first heat treatment furnace,
The casting product conveyor has a mesh structure on the surface on which the casting is placed, and allows the core sand when the sand core is collapsed to pass downward and drop onto the sand conveyor. A solution furnace characterized by being configured as described above.
空気排出口及び空気供給口が、前記第一熱処理炉の上部及び下部にそれぞれ設けられ、さらに、上記空気排出口から排出された空気を加熱する加熱手段が備えられ、上記第一熱処理炉内の空気を循環及び加熱することを特徴とする請求項1に記載の溶体化炉。   An air discharge port and an air supply port are provided at the upper and lower portions of the first heat treatment furnace, respectively, and further provided with heating means for heating the air discharged from the air discharge port, The solution furnace according to claim 1, wherein air is circulated and heated. 前記鋳造品搬送用コンベヤ及び前記砂搬送用コンベヤは、搬送方向及び搬送速度を同一に設定することを特徴とする請求項1又は2に記載の溶体化炉。   The solution furnace according to claim 1 or 2, wherein the casting product conveyer and the sand conveyer have the same conveying direction and conveying speed. 前記第一熱処理炉は、前記砂搬送用コンベヤによって搬送された中子砂を排出する砂用排出口を備えていることを特徴とする請求項1〜3のいずれかに記載の溶体化炉。   The solution heat treatment furnace according to any one of claims 1 to 3, wherein the first heat treatment furnace includes a sand discharge port for discharging the core sand conveyed by the sand conveyance conveyor.
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Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US10239117B2 (en) 2015-11-27 2019-03-26 Matsushita Industry Corp. Core sand regeneration system
CN110496952A (en) * 2019-09-06 2019-11-26 江苏新安驰铝业有限公司 A kind of type core sand removal method of the turbocharger shell of low pressure casting

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JPH11156528A (en) * 1997-11-25 1999-06-15 Nippon Furnace Kogyo Kaisha Ltd Solution treatment furnace and solution treatment method
WO2002020195A1 (en) * 2000-09-07 2002-03-14 Taiho Industries Co., Ltd. Heat treating device and heat treating method for casting
JP2008501860A (en) * 2004-06-02 2008-01-24 コンソリデイテッド エンジニアリング カンパニー, インコーポレイテッド Integrated metal processing equipment

Patent Citations (3)

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Publication number Priority date Publication date Assignee Title
JPH11156528A (en) * 1997-11-25 1999-06-15 Nippon Furnace Kogyo Kaisha Ltd Solution treatment furnace and solution treatment method
WO2002020195A1 (en) * 2000-09-07 2002-03-14 Taiho Industries Co., Ltd. Heat treating device and heat treating method for casting
JP2008501860A (en) * 2004-06-02 2008-01-24 コンソリデイテッド エンジニアリング カンパニー, インコーポレイテッド Integrated metal processing equipment

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US10239117B2 (en) 2015-11-27 2019-03-26 Matsushita Industry Corp. Core sand regeneration system
CN110496952A (en) * 2019-09-06 2019-11-26 江苏新安驰铝业有限公司 A kind of type core sand removal method of the turbocharger shell of low pressure casting

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