JP4362712B2 - Crucible melting and holding furnace - Google Patents

Crucible melting and holding furnace Download PDF

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JP4362712B2
JP4362712B2 JP2004024260A JP2004024260A JP4362712B2 JP 4362712 B2 JP4362712 B2 JP 4362712B2 JP 2004024260 A JP2004024260 A JP 2004024260A JP 2004024260 A JP2004024260 A JP 2004024260A JP 4362712 B2 JP4362712 B2 JP 4362712B2
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crucible
holding
melting
chamber
furnace
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JP2005214555A (en
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民雄 岡田
忠男 佐々木
了一 岸田
英雄 吉川
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Nippon Crucible Co Ltd
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本発明は、被溶解材を投入し予熱する予熱タワーと、坩堝を用いた坩堝式の溶解用坩堝室と保持用坩堝室を構成要素として含む連続溶解型の坩堝式溶解保持炉に関する。本明細書において、被溶解材とは、アルミニウム、亜鉛、銅合金等の非鉄金属インゴットを初め、それらのリターン材、切粉、空缶、スクラップ材やそれらをプレス加工等により押し固めたもの、もしくは、鉄、ゴム、プラスチック等の部品が付いた非鉄金属材を含む意味で用いられている。   The present invention relates to a preheating tower for charging a material to be melted and preheating, a crucible type melting crucible chamber using a crucible, and a continuous melting type crucible melting and holding furnace including a holding crucible chamber as constituent elements. In this specification, the material to be melted includes non-ferrous metal ingots such as aluminum, zinc, and copper alloys, their return materials, chips, empty cans, scrap materials, and those that are pressed and pressed, etc., Or it is used to include non-ferrous metal materials with parts such as iron, rubber, and plastic.

この種の坩堝式溶解保持炉は、図4のように被溶解材aの予熱タワー100と、該予熱タワー100の直下に設置される溶解用坩堝炉101と、坩堝炉101に並置した保持用坩堝炉102とを備えている。また、溶解用坩堝炉101は、溶解用坩堝103、溶解用坩堝室104及びバーナー105から成り、保持用坩堝炉102は、保持用坩堝107、保持用坩堝室106及びバーナー105Aから成っている。そして、予熱タワー100から溶解用坩堝炉102に供給される被溶解材aをバーナー105で溶かし、溶解溶湯は溶解用坩堝103の樋108によって連続的に保持用坩堝107に向かって溢流し、保持用坩堝107では溶湯をバーナーで目標の鋳造温度にまで昇温されたのちに汲出される(例えば、特許文献1参照。)。   As shown in FIG. 4, this type of crucible melting and holding furnace includes a preheating tower 100 of a material to be melted a, a melting crucible furnace 101 installed immediately below the preheating tower 100, and a holding furnace juxtaposed in the crucible furnace 101. A crucible furnace 102 is provided. The melting crucible furnace 101 includes a melting crucible 103, a melting crucible chamber 104, and a burner 105. The holding crucible furnace 102 includes a holding crucible 107, a holding crucible chamber 106, and a burner 105A. Then, the material to be melted a to be supplied from the preheating tower 100 to the melting crucible furnace 102 is melted by the burner 105, and the molten molten metal continuously overflows toward the holding crucible 107 by the rod 108 of the melting crucible 103. In the crucible 107, the molten metal is pumped out after being heated up to a target casting temperature by a burner (see, for example, Patent Document 1).

溶解用坩堝室104内で発生する燃焼排ガスは、溶解用坩堝室104と溶解用坩堝103の間の周隙109を上昇して予熱タワー100内に予熱源として供給される一方、保持用坩堝室106内で発生する燃焼排ガスは、保持用坩堝室106と保持用坩堝107との間の隙間110を上昇して排ガス流路111から溶解用坩堝室104内及び予熱タワー100内に流入して溶解用坩堝室104内で発生する燃焼排ガスと合流する。そして、予熱タワー100内で予熱された被溶解材aは絶えず予熱タワー100内を降下して坩堝103の溶湯中で溶かされるので、溶解溶湯の温度は、常に低温(被溶解材の融点に近い温度)に維持される。   Combustion exhaust gas generated in the melting crucible chamber 104 rises in the gap 109 between the melting crucible chamber 104 and the melting crucible 103 and is supplied to the preheating tower 100 as a preheating source, while the holding crucible chamber. Combustion exhaust gas generated in 106 rises through the gap 110 between the holding crucible chamber 106 and the holding crucible 107 and flows into the melting crucible chamber 104 and the preheating tower 100 from the exhaust gas flow path 111 and dissolves. The combustion exhaust gas generated in the crucible chamber 104 is joined. And since the to-be-melted material a preheated in the preheating tower 100 falls continuously in the preheating tower 100 and is melted in the molten metal of the crucible 103, the temperature of the molten metal is always low (close to the melting point of the to-be-melted material). Temperature).

予熱タワー100内への被溶解材aの投入指示は、予熱タワー100の頂部の開閉蓋112の排気孔113を通過する熱交換後の燃焼排ガスの温度を熱電対114で感知することにより行われ、予熱タワー100内の被溶解材aの量が少なくなれば熱交換後の排ガス温度が上昇し、燃焼排ガスの温度が設定範囲を超えると、熱電対114がこれを感知して投入指示を出して開閉蓋112を開き、溶解用坩堝室104のバーナー105による加熱を停止させる。被溶解材aの追加投入が完了すると、開閉蓋112を閉じてバーナー105による加熱を再開する。   The instruction to input the material to be melted a into the preheating tower 100 is performed by sensing the temperature of the combustion exhaust gas after the heat exchange passing through the exhaust hole 113 of the opening / closing lid 112 at the top of the preheating tower 100 with the thermocouple 114. If the amount of the material to be melted a in the preheating tower 100 decreases, the exhaust gas temperature after heat exchange rises. When the temperature of the combustion exhaust gas exceeds the set range, the thermocouple 114 detects this and gives a charging instruction. Then, the opening / closing lid 112 is opened, and the heating of the melting crucible chamber 104 by the burner 105 is stopped. When the additional charging of the material to be melted a is completed, the opening / closing lid 112 is closed and heating by the burner 105 is resumed.

かかる坩堝式溶解保持炉は、溶解用坩堝室104及び保持用坩堝室106の両室から発生するすべての燃焼排ガスを被溶解材aと熱交換して被溶解材aの予熱に利用することによって省エネルギー化が図られ、また、酸化物の発生が少なくなるという利点がある。   Such a crucible type melting and holding furnace heats all the combustion exhaust gas generated from both the melting crucible chamber 104 and the holding crucible chamber 106 with the melted material a and uses it for preheating the melted material a. There are advantages in that energy saving is achieved and generation of oxides is reduced.

しかしながら、保持用坩堝107の容量が大きい場合や被溶解材aの融点が高い場合などには、溶解温度や保持温度が高くなり、燃焼排ガスが大量に発生し、燃焼排ガスの温度が高くなるので、溶解用坩堝室103で発生する燃焼排ガスの熱交換だけで被溶解材aを十分に予熱できることになる。したがって、両室から発生する全ての高温の燃焼排ガスを被溶解材aの予熱として利用すると、予熱タワー100内が高温化することにより、予熱タワー100内に被溶解材aが充分に充填された状態であっても、熱交換後の排ガス温度が排ガス感知の設定温度を超えることが多くなり、その結果、前記投入指示が頻繁に行われて被溶解材aのオーバーチャージの原因になるなど被溶解材aの投入管理に支障をきたす。   However, when the capacity of the holding crucible 107 is large or the melting point of the material to be melted a is high, the melting temperature and the holding temperature are increased, a large amount of combustion exhaust gas is generated, and the temperature of the combustion exhaust gas is increased. The material to be melted a can be sufficiently preheated only by heat exchange of the combustion exhaust gas generated in the melting crucible chamber 103. Therefore, when all the high-temperature combustion exhaust gas generated from both chambers is used as the preheating of the material to be melted a, the temperature of the preheating tower 100 is increased, so that the material to be melted a is sufficiently filled in the preheating tower 100. Even in such a state, the exhaust gas temperature after heat exchange often exceeds the set temperature for exhaust gas detection, and as a result, the input instruction is frequently performed, causing overcharge of the material to be melted a. It interferes with the input management of the melting material a.

なお、熱交換後の排ガスの感知温度を高温に設定して材料のオーバーチャージは避けることも考えられるが、合流して形成される高温の排ガスと被溶解材aの熱交換率が低下して有効利用が図れず、省エネ効果を損なうことになる。
特開2000−130948号公報
Although it is conceivable to avoid overcharge of the material by setting the sensing temperature of the exhaust gas after heat exchange to a high temperature, the heat exchange rate between the hot exhaust gas formed by joining and the material to be melted a decreases. Effective use cannot be achieved and the energy saving effect will be impaired.
JP 2000-130948 A

本発明は、上記の点に鑑みてなされたものであって、熱交換後の排ガスの感知温度を高温に設定しなくても、被溶解材のオーバージャージを防ぐことができ、排ガスを有効に利用できる坩堝式溶解保持炉を提供する。   The present invention has been made in view of the above points, and even if the detection temperature of the exhaust gas after heat exchange is not set to a high temperature, it is possible to prevent over-jersey of the material to be melted, and to effectively exhaust the exhaust gas. A crucible melting and holding furnace that can be used is provided.

本発明の坩堝式溶解保持炉は、被溶解材を予熱するための予熱タワーと、前記予熱タワーの下方に設置され、前記予熱タワーから前記被溶解材の供給を受ける溶解用坩堝と、前記溶解用坩堝を収容する溶解用坩堝室と、前記溶解用坩堝を加熱する溶解用加熱手段と、前記溶解用坩堝から溶湯の供給を受ける保持用坩堝と、前記保持用坩堝を収容する保持用坩堝室と、前記保持用坩堝を加熱する保持用加熱手段と、を備えた溶解保持炉において、前記溶解用坩堝室及び保持用坩堝室は、共用側壁を介して隣接しており、前記保持用坩堝は、内部が仕切り部により受湯室と汲み出し室とに仕切られ、前記受湯室及び汲み出し室は、前記仕切り部の下方で連通しており、前記共用側壁に形成された開口に接続されて前記受湯室の上側を覆う排湯フードと、前記開口及び排湯フードを介して前記溶解用坩堝から前記保持用坩堝の前記受湯室に溶湯を供給する移送部とを備えており、前記仕切り部は、前記排湯フードの先端から下方に延びるように設けられており、前記保持用坩堝室と前記保持用坩堝の口部との間の隙間を仕切り体で塞いで前記保持用坩堝と前記保持用坩堝室との間に形成される燃焼室を密封構造にすることにより、前記保持用加熱手段により生じる高温排ガスが前記溶解用坩堝室及び前記予熱タワーに流れ込むのを防止するように構成したことを特徴とする。 The crucible melting and holding furnace of the present invention includes a preheating tower for preheating a material to be melted, a melting crucible installed below the preheating tower and receiving the material to be melted from the preheating tower, and the melting A melting crucible chamber for housing the melting crucible; a melting heating means for heating the melting crucible; a holding crucible for receiving a supply of molten metal from the melting crucible; and a holding crucible chamber for accommodating the holding crucible And a holding heating means for heating the holding crucible, the melting crucible chamber and the holding crucible chamber are adjacent to each other via a common side wall, and the holding crucible is And the interior is partitioned into a hot water receiving chamber and a pumping chamber by a partition, and the hot water receiving chamber and the pumping chamber communicate with each other below the partition, and are connected to an opening formed in the shared side wall. A draining hot water covering the upper side of the hot water reception room And a transfer part that supplies the molten metal from the melting crucible to the hot water receiving chamber of the holding crucible through the opening and the hot water hood, and the partition part is formed from the tip of the hot water hood. The holding crucible chamber is formed between the holding crucible chamber and the holding crucible chamber by closing a gap between the holding crucible chamber and the opening of the holding crucible with a partition. The combustion chamber is sealed to prevent high temperature exhaust gas generated by the holding heating means from flowing into the melting crucible chamber and the preheating tower.

また、前記保持用加熱手段をリジェネレイティブバーナとし、該リジェネレイティブバーナを前記保持用坩堝室の壁部に形成される開口に取り付けるのが望ましい。   Further, it is desirable that the holding heating means is a regenerative burner, and the regenerative burner is attached to an opening formed in a wall portion of the holding crucible chamber.

また、前記保持用加熱手段を電熱ヒーターとし、該電熱ヒーターを前記保持用坩堝室の内壁面に配設するのが望ましい。   Further, it is desirable that the holding heating means is an electric heater, and the electric heater is disposed on the inner wall surface of the holding crucible chamber.

また、前記保持用坩堝を鉄製坩堝とし、該坩堝の口部から外鍔を突設し、該外鍔を前記仕切り体とするのが望ましい。   Further, it is desirable that the holding crucible is an iron crucible, an outer casing is projected from the mouth of the crucible, and the outer casing is used as the partition body.

本発明の坩堝式溶解保持炉によれば、前記保持用加熱手段により生じる高温排ガスが前記溶解用坩堝室及び前記予熱タワーに流れ込むのを防止するように構成したので、溶解用坩堝室で発生する加熱ガスのみを被溶解材の予熱に利用することができる。したがって、大容量の保持用坩堝を用いる場合や高融点の被溶解材を対象とする場合の被溶解材のオーバーチャージを防止でき、また、被溶解材の投入管理が容易になる。   According to the crucible type melting and holding furnace of the present invention, the high temperature exhaust gas generated by the holding heating means is prevented from flowing into the melting crucible chamber and the preheating tower. Only the heated gas can be used for preheating the material to be melted. Therefore, it is possible to prevent the material to be melted from being overcharged when a large-capacity holding crucible is used or when the material to be melted has a high melting point, and it becomes easy to manage the material to be melted.

また、前記保持用坩堝室と前記保持用坩堝の口部との間の隙間を仕切り体で塞いで前記保持用坩堝と前記保持用坩堝室との間に形成される燃焼室を密封構造にすることにより、前記高温排ガスが前記溶解用坩堝室及び前記予熱タワーに流れ込むのを防止するように構成すれば、前記保持用加熱手段により生じる高温排ガスの前記溶解用坩堝室及び前記予熱タワーへの流入を容易に防ぐことができる。   In addition, a gap between the holding crucible chamber and the opening of the holding crucible is closed with a partition body, and the combustion chamber formed between the holding crucible and the holding crucible chamber is made to have a sealed structure. Thus, if the high temperature exhaust gas is prevented from flowing into the melting crucible chamber and the preheating tower, the high temperature exhaust gas generated by the holding heating means flows into the melting crucible chamber and the preheating tower. Can be easily prevented.

また、前記燃焼室を密封構造とし、前記保持用加熱手段をリジェネレイティブバーナとすれば、高温の燃焼排ガスと空気を充分に熱交換して排ガス温度を低温にできるので、省エネルギー化が可能になり、しかも、被溶解材のオーバーチャージをなくすと共に被溶解材を十分に予熱できる。   In addition, if the combustion chamber has a sealed structure and the holding heating means is a regenerative burner, the exhaust gas temperature can be lowered by sufficiently exchanging heat between the high-temperature combustion exhaust gas and air, thus enabling energy saving. In addition, overmelting of the material to be melted can be eliminated and the material to be melted can be sufficiently preheated.

また、前記燃焼室を密封構造とし、前記保持用加熱手段を電熱ヒーターとすれば、高い電熱効率で保持加熱できるので、省エネルギー化が可能になり、しかも、被溶解材のオーバーチャージをなくすと共に被溶解材を十分に予熱できる。   Further, if the combustion chamber has a sealed structure and the holding heating means is an electric heater, it can be held and heated with high electric heating efficiency, so that energy saving can be achieved, and the overcharge of the melted material is eliminated and the covering is eliminated. The melting material can be sufficiently preheated.

また、前記溶解用坩堝から溢流する溶湯を前記保持用坩堝に連続的に移送する移送部及び該−移送部を流れる溶湯に、前記保持用坩堝内の溶湯からの熱気及び前記溶解用坩堝室からの高温排ガスを接触させるための流路を備えれば、移送部を流れる溶湯の温度低下を防止して溶湯の固化を防止することができる。   Further, the molten metal overflowing from the melting crucible is continuously transferred to the holding crucible, and the molten metal flowing in the holding transfer crucible is supplied with hot air from the molten metal in the holding crucible and the melting crucible chamber. If the flow path for making the high temperature exhaust gas from contact is provided, the temperature fall of the molten metal which flows through a transfer part can be prevented, and solidification of a molten metal can be prevented.

以下に本発明の坩堝式溶解保持炉の実施形態を添付図面に基づき説明する。   Embodiments of a crucible melting and holding furnace of the present invention will be described below with reference to the accompanying drawings.

実施形態1
図1に本実施形態の坩堝式溶解保持炉の全体が概略的に示され、該溶解保持炉Aは、アルミニウムインゴット等の被溶解材aの予熱タワー1と、該予熱タワー1の直下に設置される溶解用坩堝炉2と、溶解用坩堝炉2に並置される保持用坩堝炉3とを備えている。
Embodiment 1
FIG. 1 schematically shows the entire crucible melting and holding furnace of the present embodiment. The melting and holding furnace A is installed in a preheating tower 1 of a material to be melted a such as an aluminum ingot, and immediately below the preheating tower 1. The melting crucible furnace 2 is provided, and the holding crucible furnace 3 juxtaposed to the melting crucible furnace 2 is provided.

溶解用坩堝炉2は、溶解用坩堝室4と、溶解用坩堝室4の炉蓋41と、溶解用坩堝室4内に坩堝台5を介し設置される溶解用坩堝6と、溶解用坩堝6を加熱するバーナー(溶解用加熱手段)Bとを備え、該坩堝6と溶解用坩堝室4及び炉蓋41との間には周隙7が形成され、該周隙7は矢印のようにバーナーBの燃焼排ガス(高温ガス)が流れる上昇通路となる。   The melting crucible furnace 2 includes a melting crucible chamber 4, a furnace lid 41 of the melting crucible chamber 4, a melting crucible 6 installed in the melting crucible chamber 4 via a crucible base 5, and a melting crucible 6 And a peripheral space 7 is formed between the crucible 6, the melting crucible chamber 4 and the furnace lid 41. The peripheral space 7 is a burner as indicated by an arrow. It becomes an ascending passage through which the B combustion exhaust gas (hot gas) flows.

保持用坩堝炉3は、保持用坩堝室8と、保持用坩堝室8の炉蓋81と、保持用坩堝室8内に坩堝台9を介し設置される保持用坩堝10と、保持用坩堝10を加熱するセルフ型のリジェネレイティブバーナー(保持用加熱手段)RBとを備えている。保持用坩堝室8の壁部には開口8aが形成され、開口8aにはリジェネレイティブバーナーRBが取り付けられている。   The holding crucible furnace 3 includes a holding crucible chamber 8, a furnace lid 81 of the holding crucible chamber 8, a holding crucible 10 installed in the holding crucible chamber 8 via a crucible base 9, and a holding crucible 10 A self-type regenerative burner (heating means for holding) RB. An opening 8a is formed in the wall of the holding crucible chamber 8, and a regenerative burner RB is attached to the opening 8a.

炉蓋81は、保持用坩堝室8と保持用坩堝10の口部との間に形成される隙間82を塞ぐ仕切り体を兼ね、これにより保持用坩堝室8と保持用坩堝10との間に形成される燃焼室83を密閉構造にし、高温の燃焼排ガスが溶解用坩堝室4及び予熱タワー1に流れ込むのを防止している
溶解用坩堝室4及び保持用坩堝室8には断熱材、例えばセラミック系の断熱材で内張りが施され、その境界部には共用側壁13が設けられている。
The furnace lid 81 also serves as a partition that closes the gap 82 formed between the holding crucible chamber 8 and the opening of the holding crucible 10, and thereby, between the holding crucible chamber 8 and the holding crucible 10. The formed combustion chamber 83 has a sealed structure and prevents high-temperature combustion exhaust gas from flowing into the melting crucible chamber 4 and the preheating tower 1. The melting crucible chamber 4 and the holding crucible chamber 8 include a heat insulating material such as A lining is applied with a ceramic heat insulating material, and a common side wall 13 is provided at the boundary portion.

リジェネレイティブバーナーRBは、燃焼排ガスを回収して炉の熱効率を向上させるバーナーである。   The regenerative burner RB is a burner that recovers combustion exhaust gas and improves the thermal efficiency of the furnace.

坩堝台5,9は坩堝6,10の底部からの加熱を可能にするために、筒状にして側部に燃焼ガスの流通溝5a,9aを備えている。   In order to enable heating from the bottom of the crucibles 6, 10, the crucible bases 5, 9 have a cylindrical shape and are provided with combustion gas flow grooves 5 a, 9 a on the sides.

保持用坩堝10は内部が仕切り部18により受湯室19と汲み出し室20とに仕切られ、両室19,20は仕切り部18の下方で連絡口21により連通し、受湯室19において溶解坩堝6からの溶湯17を受け取る構成になっている。   The holding crucible 10 is partitioned into a hot water receiving chamber 19 and a pumping chamber 20 by a partition portion 18, and both chambers 19, 20 communicate with each other via a communication port 21 below the partition portion 18. 6 is configured to receive molten metal 17 from 6.

溶解用坩堝6と保持用坩堝10とは、溶解用坩堝6の胴部に設けられる溢流タイプの排出口15並びに該排出口15に接続する、樋形の移送部16を介し接続され、溶湯17を溶解用坩堝6内から排出口15を溢流させながら移送部16を経て保持用坩堝10内に連続的に移送できる構成になっている。移送部16は共用側壁13に形成された開口14a内を通って保持用坩堝10の受湯室19内の溶湯の液面の上方の位置まで延出されている。移送部16は樋形には限定されず、例えばパイプ形であっても良い。   The melting crucible 6 and the holding crucible 10 are connected via an overflow-type discharge port 15 provided in the body of the melting crucible 6 and a bowl-shaped transfer unit 16 connected to the discharge port 15. 17 can be continuously transferred from the melting crucible 6 into the holding crucible 10 via the transfer unit 16 while overflowing the discharge port 15. The transfer part 16 extends through the opening 14 a formed in the shared side wall 13 to a position above the liquid level of the molten metal in the hot water receiving chamber 19 of the holding crucible 10. The transfer unit 16 is not limited to a bowl shape, and may be a pipe shape, for example.

溶湯17の連続的移送は、坩堝6,10内の液面のヘッド差を利用して行われる。溶解用坩堝6の胴部に対する排出口15の形成位置は、該坩堝6内に常時滞留させる溶湯17の液量ひいては液面高さを考慮し、選択決定すればよい。   The continuous transfer of the molten metal 17 is performed by utilizing the head difference between the liquid levels in the crucibles 6 and 10. The formation position of the discharge port 15 with respect to the body portion of the melting crucible 6 may be selected and determined in consideration of the amount of the molten metal 17 that stays in the crucible 6 and the liquid level.

溶解用及び保持用坩堝6,10としては、黒鉛坩堝が適当であるが、必要に応じて鉄製坩堝(鋳鉄、普通鋼、特殊鋼など)とすることもできる。   As the melting and holding crucibles 6 and 10, graphite crucibles are suitable, but iron crucibles (cast iron, ordinary steel, special steel, etc.) can be used as necessary.

保持用坩堝10内の受湯室19の上側は排湯フード14bで覆われ、排湯フード14bと共用側壁13の開口14aとによって移送部16の周囲に流路14が形成されている。そして、保持用坩堝10内の溶湯の熱気は、該流路14によって移送部16の出湯口16aに導かれることにより、移送部16を流れる溶湯が溶湯の熱気に晒されて加熱を受け、移送中の溶湯17の温度降下が防止される。   The upper side of the hot water receiving chamber 19 in the holding crucible 10 is covered with a hot water hood 14 b, and a flow path 14 is formed around the transfer section 16 by the hot water hood 14 b and the opening 14 a of the shared side wall 13. Then, the hot air of the molten metal in the holding crucible 10 is guided to the hot water outlet 16a of the transfer unit 16 by the flow path 14, so that the molten metal flowing through the transfer unit 16 is exposed to the hot air of the molten metal and is heated and transferred. The temperature drop of the molten metal 17 inside is prevented.

保持用坩堝室8に溢流した溶湯17は使用温度まで上昇せられ、汲み出し室20より鋳湯される。また、受湯室19内では必要に応じて各種の溶湯処理や溶湯表面に溜まる酸化物等の除去等が適宜行われる。   The molten metal 17 overflowing into the holding crucible chamber 8 is raised to the operating temperature and is cast from the pumping chamber 20. Further, in the hot water receiving chamber 19, various types of molten metal treatment, removal of oxides accumulated on the molten metal surface, and the like are appropriately performed as necessary.

坩堝6,10からは亀裂等を通じて溶湯17が漏れることがあり、漏出溶湯を炉外に排出するために、例えば共用側壁13の下端部と保持用坩堝室8の側壁下端部とに図外のドレン排出口が形成されている。   The molten metal 17 may leak from the crucibles 6 and 10 through cracks and the like, and in order to discharge the leaked molten metal to the outside of the furnace, for example, the lower end of the shared side wall 13 and the lower end of the side wall of the holding crucible chamber 8 are not shown. A drain outlet is formed.

溶解用坩堝炉2の溶解用坩堝室4は、無蓋有底筒形を呈していて、上部の炉蓋41を介して筒形の予熱タワー1が2段重ね状態且つ同心状に設置されている。炉蓋41の下端は溶解用坩堝6の上端上方で、坩堝6内に向けて開口し、予熱タワー1を通じ被溶解材aを坩堝6内に投入できる構成になっている。    The melting crucible chamber 4 of the melting crucible furnace 2 has an uncovered bottomed cylindrical shape, and a cylindrical preheating tower 1 is installed in a two-stage stacked state and concentrically via an upper furnace lid 41. . The lower end of the furnace lid 41 opens above the upper end of the melting crucible 6 and opens into the crucible 6, so that the material to be melted a can be put into the crucible 6 through the preheating tower 1.

溶解用坩堝室4内の周隙7の上端側は予熱タワー1内に、溶解用坩堝6の上端と炉蓋41に形成された垂壁41Aの下端との間の環状空隙24を介し連通され、燃焼排ガスを予熱タワー1内に予熱源として供給できる構成になっている。なお、燃焼排ガスは矢印のように垂壁41Aによって一旦下方に流れるので、溶解用坩堝6内に位置する溶湯浸漬前の被溶解材aも予熱できる。  The upper end side of the gap 7 in the melting crucible chamber 4 is communicated with the preheating tower 1 via an annular gap 24 between the upper end of the melting crucible 6 and the lower end of the hanging wall 41A formed in the furnace lid 41. The combustion exhaust gas can be supplied into the preheating tower 1 as a preheating source. Since the combustion exhaust gas once flows downward by the hanging wall 41A as shown by the arrow, the material to be melted a before being immersed in the molten metal located in the melting crucible 6 can also be preheated.

予熱タワー1の上端には被溶解材aの投入口27があり、該投入口27には開閉蓋28が備えられ、該開閉蓋28には燃焼排ガスの排気口29が設けられている。該開閉蓋28には排気孔を通過する熱交換後の燃焼排ガスの温度を感知するための熱電対25が取り付けられている。排気口29の形成は、燃焼排ガスをドラフト効果により周隙7内から環状空隙24を経て予熱タワー1内に上昇気流として導くために必要である。開閉蓋28の開閉は駆動装置を備えた自動開閉機構により行うことができる。   At the upper end of the preheating tower 1, there is an inlet 27 for the material to be dissolved a. The inlet 27 is provided with an opening / closing lid 28, and the opening / closing lid 28 is provided with an exhaust port 29 for combustion exhaust gas. A thermocouple 25 for sensing the temperature of the combustion exhaust gas after the heat exchange passing through the exhaust hole is attached to the open / close lid 28. The formation of the exhaust port 29 is necessary in order to guide the combustion exhaust gas as an updraft from the circumference 7 through the annular gap 24 into the preheating tower 1 by the draft effect. The opening / closing lid 28 can be opened / closed by an automatic opening / closing mechanism equipped with a driving device.

溶解用坩堝6の取り替えや該坩堝6内の残湯汲み出し等を行うために予熱タワー1は、図1に示す2段重ねの位置より適宜移動させることができる構成になっている。予熱タワー1の全重量は台車30により支えられ、該台車30は溶解用坩堝室4に支持固定されたガイドレール31上を走行可能であり、該レール31上での台車30の走行により、予熱タワー1を溶解用坩堝室4の炉蓋4Aとの2段重ねの第1位置から2段重ねが解かれる第2位置、即ち溶解用坩堝室4の上端開口を完全にフリーと成し得る位置まで、スライド変位させることができる構成になっている。台車30を第1位置と第2位置とでそれぞれ停止させるために、各種の位置規制手段を採用することができる。  In order to replace the melting crucible 6 or pump out the remaining hot water in the crucible 6, the preheating tower 1 can be appropriately moved from the two-tiered position shown in FIG. 1. The total weight of the preheating tower 1 is supported by a carriage 30, and the carriage 30 can run on a guide rail 31 supported and fixed to the melting crucible chamber 4. The second position where the two-stage stack is unwound from the first position where the tower 1 is overlapped with the furnace cover 4A of the melting crucible chamber 4, that is, the position where the upper end opening of the melting crucible chamber 4 can be made completely free. Up to this point, the structure can be slid. In order to stop the cart 30 at the first position and the second position, various position restricting means can be employed.

図1は溶解保持炉の平常運転時の状況を示し、溶解用坩堝室4の底部からその内部に供給された燃焼ガスは溶解用坩堝6を加熱しつつ周隙7内を上昇し燃焼排ガスとなり、この燃焼排ガスは周隙7上端からこれに連通する環状空隙24を経て予熱タワー1内に入り、予熱タワー1内のインゴット等aと熱交換し予熱源として有効利用された後に、開閉蓋28の排気口29を経て炉外に排出される。炉外排出の燃焼排ガスの温度は被溶解材aとの熱交換により、例えば375℃以下に低下する。この燃焼排ガスの温度低下は、作業環境の改善につながる。一方、保持用坩堝室8は上述のように密閉構造となっているので、保持用坩堝室8の高温の燃焼排ガスが予熱タワー1や溶解用坩堝室4に流れ込んでバーナBの燃焼排ガスと合流することはない。   FIG. 1 shows the situation during normal operation of the melting and holding furnace. The combustion gas supplied from the bottom of the melting crucible chamber 4 to the inside of the melting crucible chamber 6 rises in the circumferential space 7 while heating the melting crucible 6 and becomes combustion exhaust gas. The combustion exhaust gas enters the preheating tower 1 from the upper end of the circumferential space 7 through the annular gap 24 communicating therewith, and exchanges heat with an ingot or the like a in the preheating tower 1 and is effectively used as a preheating source. Is discharged to the outside of the furnace through the exhaust port 29. The temperature of the flue gas discharged from the furnace is reduced to, for example, 375 ° C. or less by heat exchange with the material to be melted a. This temperature reduction of the combustion exhaust gas leads to improvement of the working environment. On the other hand, since the holding crucible chamber 8 has a sealed structure as described above, the high-temperature combustion exhaust gas in the holding crucible chamber 8 flows into the preheating tower 1 and the melting crucible chamber 4 and merges with the combustion exhaust gas from the burner B. Never do.

被溶解材aは、溶解用坩堝6の溶湯17内に浸漬されている下端部のものから順に溶解されて行く。被溶解材aは溶解が進むにつれて自重降下し溶湯内に浸漬して行き、常に溶湯17中で溶かされるので、溶湯17の温度はアルミの融点近傍の低い温度に略々一定に保持される。   The material to be melted a is melted in order from the lower end portion immersed in the molten metal 17 of the melting crucible 6. The material to be melted a falls under its own weight as the melting progresses, soaks in the molten metal, and is always melted in the molten metal 17, so that the temperature of the molten metal 17 is kept substantially constant at a low temperature near the melting point of aluminum.

溶解用坩堝6内の溶湯17は、ヘッド差によって排出口15を溢流しつつ移送部16を経て保持用坩堝10の受湯室19内に連続的に移送されて行き、連続的溶解保持が可能になる。   The molten metal 17 in the melting crucible 6 is continuously transferred to the hot water receiving chamber 19 of the holding crucible 10 through the transfer unit 16 while overflowing the discharge port 15 due to the head difference, and can be continuously melted and held. become.

保持用坩堝10の受湯室19内に流入した低温の溶湯17は燃焼ガスの加熱により必要な温度まで加熱保持され、注湯される。また受湯室19内で必要応じて各種溶湯処理や酸化物除去が図られる。受湯室19内の溶湯17は仕切り板18の下端の連絡口21を通じ汲み出し室20内に流入し、汲み出し使用に備える。   The low-temperature molten metal 17 that has flowed into the hot water receiving chamber 19 of the holding crucible 10 is heated and held to a required temperature by pouring the combustion gas and poured. Various molten metal treatments and oxide removal are performed in the hot water receiving chamber 19 as necessary. The molten metal 17 in the hot water receiving chamber 19 flows into the pumping chamber 20 through the communication port 21 at the lower end of the partition plate 18 to prepare for pumping use.

予熱タワー1内への被溶解材aの投入指示は、上述のように開閉蓋28の排気孔を通過する熱交換後の燃焼排ガスの温度を熱電対25で感知して行われ、予熱タワー1内の被溶解材aの量が少なくなれば熱交換後の排ガス温度が上昇し、燃焼排ガスの温度が設定範囲を超えると、熱電対25がこれを感知して投入指示を出して開閉蓋28を開き、溶解用坩堝室4のバーナーBによる加熱を停止させる。被溶解材aの追加投入が完了すると、開閉蓋28を閉じてバーナーBによる加熱を再開する。   The instruction to input the material to be melted a into the preheating tower 1 is performed by detecting the temperature of the combustion exhaust gas after the heat exchange passing through the exhaust hole of the opening / closing lid 28 with the thermocouple 25 as described above. If the amount of the material to be melted a decreases, the exhaust gas temperature after heat exchange rises. If the temperature of the combustion exhaust gas exceeds the set range, the thermocouple 25 senses this and gives an input instruction to open / close the lid 28. And the heating of the melting crucible chamber 4 by the burner B is stopped. When the additional charging of the material to be melted a is completed, the opening / closing lid 28 is closed and heating by the burner B is resumed.

熱交換後の排ガス温度は、被溶解材aの融点や予熱タワー1に充填される被溶解材aの量によって異なるが、被溶解材aが例えばADC12等の通常のアルミニウム材であれば、約300〜500℃の範囲に設定される。   The exhaust gas temperature after the heat exchange varies depending on the melting point of the material to be melted a and the amount of the material to be melted a that is filled in the preheating tower 1. It is set in the range of 300 to 500 ° C.

このように坩堝式溶解保持炉は、予熱タワー1と、溶解用および保持用の2つに仕切られた坩堝炉2,3からなる構造をもち、かつ溶解用坩堝炉2から保持用坩堝炉3内への移湯を連続的に行い溶湯の汲出しを保持用坩堝炉側から行う構成になっているので、予熱タワー1を溶解用坩堝炉2の上端開口部の上方に置くことにより、溶解用坩堝炉2内で発生する燃焼排ガスのみを予熱タワー1での予熱用に利用することが可能になる。   Thus, the crucible type melting and holding furnace has a structure comprising the preheating tower 1 and the crucible furnaces 2 and 3 divided into two for melting and holding, and from the melting crucible furnace 2 to the holding crucible furnace 3. Since the hot water is continuously transferred to the inside and the molten metal is pumped out from the holding crucible furnace side, the preheating tower 1 is melted by placing it above the upper end opening of the melting crucible furnace 2. Only the combustion exhaust gas generated in the crucible furnace 2 can be used for preheating in the preheating tower 1.

更に坩堝炉2,3の炉壁は溶湯と接触しないのでセラミックファイバー系断熱材による内張りを施すことが可能になる。セラミック系断熱材は軽量材のため蓄熱量が少なく、炉壁からの放熱量が小さくなり省エネとなる。   Furthermore, since the furnace walls of the crucible furnaces 2 and 3 do not come into contact with the molten metal, it is possible to apply a lining with a ceramic fiber heat insulating material. Ceramic heat insulating materials are light weight materials, so there is little heat storage, and the amount of heat released from the furnace wall is reduced, saving energy.

実施形態2
図2に示す坩堝式溶解保持炉は、保持用坩堝炉3にリジェネレイティブバーナーRBに代えて電熱ヒーターHを配設したものである。電熱ヒーターHは保持用坩堝室8の内壁面に配設され、電熱線の発熱により保持用坩堝10を加熱するようになっている。なお、第1の実施形態と同一又は類似の部分については、第1の実施形態に付された符号と同じ符号を図2に付すことによりその部分の説明を省略する。
Embodiment 2
In the crucible type melting and holding furnace shown in FIG. 2, an electric heater H is disposed in the holding crucible furnace 3 in place of the regenerative burner RB. The electric heater H is disposed on the inner wall surface of the holding crucible chamber 8 and heats the holding crucible 10 by the heat generated by the heating wire. In addition, about the part which is the same as that of 1st Embodiment, or a similar part, the code | symbol same as the code | symbol attached | subjected to 1st Embodiment is attached | subjected to FIG. 2, and description of the part is abbreviate | omitted.

実施形態1と同様に保持用坩堝炉3の燃焼室83は炉蓋81により密閉構造となっているので、電熱ヒーターHによる加熱ロスが少なくなり電熱効率の向上が図れる。   As in the first embodiment, the combustion chamber 83 of the holding crucible furnace 3 has a sealed structure by the furnace lid 81, so that the heating loss due to the electric heater H is reduced and the electrothermal efficiency can be improved.

図3は、保持用坩堝10は鉄製坩堝とし、該坩堝10の口部から炉蓋81を兼ねる外鍔10Aを突設し、該外鍔10Aで隙間82を塞いだ実施形態を示している。   FIG. 3 shows an embodiment in which the holding crucible 10 is an iron crucible, an outer casing 10A that also serves as a furnace lid 81 is projected from the mouth of the crucible 10, and the gap 82 is closed with the outer casing 10A.

本発明の実施形態1の坩堝式溶解保持炉を示す正面断面図である。It is a front sectional view showing the crucible type melting and holding furnace of Embodiment 1 of the present invention. 本発明の実施形態2の坩堝式溶解保持炉を示す正面断面図である。It is front sectional drawing which shows the crucible type | mold melting holding furnace of Embodiment 2 of this invention. 本発明の他の実施形態の坩堝式溶解保持炉の一部を示す正面断面図である。It is a front sectional view showing a part of a crucible type melting and holding furnace of another embodiment of the present invention. 従来の坩堝式溶解保持炉の正面断面図である。It is a front sectional view of the conventional crucible type melting and holding furnace.

符号の説明Explanation of symbols

1 予熱タワー
2 溶解用坩堝炉
3 保持用坩堝炉
4 溶解用坩堝室
B バーナー(溶解用加熱手段)
RB リジェネレイティブバーナー(保持用加熱手段)
H 電熱ヒーター(保持用加熱手段)
8 保持用坩堝室
10 保持用坩堝


1 Preheating tower 2 Melting crucible furnace 3 Holding crucible furnace 4 Melting crucible chamber B Burner (heating means for melting)
RB regenerative burner (heating means for holding)
H Electric heater (heating means for holding)
8 Holding crucible chamber 10 Holding crucible


Claims (4)

被溶解材を予熱するための予熱タワーと、前記予熱タワーの下方に設置され、前記予熱タワーから前記被溶解材の供給を受ける溶解用坩堝と、前記溶解用坩堝を収容する溶解用坩堝室と、前記溶解用坩堝を加熱する溶解用加熱手段と、前記溶解用坩堝から溶湯の供給を受ける保持用坩堝と、前記保持用坩堝を収容する保持用坩堝室と、前記保持用坩堝を加熱する保持用加熱手段と、を備えた溶解保持炉において、
前記溶解用坩堝室及び保持用坩堝室は、共用側壁を介して隣接しており、
前記保持用坩堝は、内部が仕切り部により受湯室と汲み出し室とに仕切られ、前記受湯室及び汲み出し室は、前記仕切り部の下方で連通しており、
前記共用側壁に形成された開口に接続されて前記受湯室の上側を覆う排湯フードと、前記開口及び排湯フードを介して前記溶解用坩堝から前記保持用坩堝の前記受湯室に溶湯を供給する移送部とを備えており、
前記仕切り部は、前記排湯フードの先端から下方に延びるように設けられており、
前記保持用坩堝室と前記保持用坩堝の口部との間の隙間を仕切り体で塞いで前記保持用坩堝と前記保持用坩堝室との間に形成される燃焼室を密封構造にすることにより、前記保持用加熱手段により生じる高温排ガスが前記溶解用坩堝室及び前記予熱タワーに流れ込むのを防止するように構成したことを特徴とする坩堝式溶解保持炉。
A preheating tower for preheating the material to be melted, a melting crucible installed below the preheating tower and receiving the material to be melted from the preheating tower, and a melting crucible chamber for housing the melting crucible A melting heating means for heating the melting crucible, a holding crucible for receiving a supply of molten metal from the melting crucible, a holding crucible chamber for housing the holding crucible, and a holding for heating the holding crucible A melting and holding furnace comprising:
The melting crucible chamber and the holding crucible chamber are adjacent to each other via a shared side wall,
The holding crucible is partitioned into a hot water receiving chamber and a pumping chamber by a partition part, and the hot water receiving chamber and the pumping chamber communicate with each other below the partition part,
A hot water hood connected to an opening formed in the shared side wall and covering the upper side of the hot water receiving chamber, and a molten metal from the melting crucible to the hot water receiving chamber of the holding crucible through the opening and the hot water hood And a transfer section for supplying
The partition is provided so as to extend downward from the tip of the hot water hood,
By closing the gap between the holding crucible chamber and the opening of the holding crucible with a partition, and forming a combustion chamber formed between the holding crucible and the holding crucible chamber with a sealed structure , crucible type melting and holding furnace wherein the hot exhaust gas caused by the holding heating means is configured to prevent the flow into the melting crucible chamber and the preheating tower.
前記保持用加熱手段をリジェネレイティブバーナとしたことを特徴とする請求項1に記載の坩堝式溶解保持炉。 The crucible melting and holding furnace according to claim 1 , wherein the holding heating means is a regenerative burner. 前記保持用加熱手段を電熱ヒーターとし、該電熱ヒーターを前記保持用坩堝室の内壁面に配設したことを特徴とする請求項1に記載の坩堝式溶解保持炉。 The crucible type melting and holding furnace according to claim 1 , wherein the holding heating means is an electric heater, and the electric heater is disposed on an inner wall surface of the holding crucible chamber. 前記保持用坩堝は鉄製坩堝であり、該坩堝の口部から外鍔を突設し、該外鍔を前記仕切り体としたことを特徴とする請求項1から3のいずれかに記載の坩堝式溶解保持炉。 The crucible type according to any one of claims 1 to 3 , wherein the holding crucible is an iron crucible, and an outer casing protrudes from a mouth portion of the crucible, and the outer casing is used as the partition body. Melting and holding furnace.
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