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JP3157330B2 - Smoke exhaust system - Google Patents
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JP3157330B2 - Smoke exhaust system - Google Patents

Smoke exhaust system

Info

Publication number
JP3157330B2
JP3157330B2 JP05015293A JP5015293A JP3157330B2 JP 3157330 B2 JP3157330 B2 JP 3157330B2 JP 05015293 A JP05015293 A JP 05015293A JP 5015293 A JP5015293 A JP 5015293A JP 3157330 B2 JP3157330 B2 JP 3157330B2
Authority
JP
Japan
Prior art keywords
smoke
molten metal
furnace
metal storage
furnaces
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Lifetime
Application number
JP05015293A
Other languages
Japanese (ja)
Other versions
JPH06238431A (en
Inventor
敏之 中尾
博 長浜
勝己 長尾
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Mazda Motor Corp
Original Assignee
Mazda Motor Corp
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Mazda Motor Corp filed Critical Mazda Motor Corp
Priority to JP05015293A priority Critical patent/JP3157330B2/en
Publication of JPH06238431A publication Critical patent/JPH06238431A/en
Application granted granted Critical
Publication of JP3157330B2 publication Critical patent/JP3157330B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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  • Casting Support Devices, Ladles, And Melt Control Thereby (AREA)
  • Waste-Gas Treatment And Other Accessory Devices For Furnaces (AREA)

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【産業上の利用分野】この発明は、例えば、砂型鋳造等
に用いられる溶湯を収容する低周波溶解炉からの煙を排
煙するような排煙装置に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a smoke exhaust device for exhausting smoke from a low-frequency melting furnace containing molten metal used in, for example, sand casting.

【0002】[0002]

【従来の技術】従来、実開昭62−1725号公報に記
載のような粉塵回収装置がある。すなわち、吸引ブロア
を備える集塵機に接続された搬送ダクトと、この搬送ダ
クトに接続され複数の粉塵発生設備にそれぞれ臨む吸引
ダクトと、これら各吸引ダクトにそれぞれ設けられ各吸
引ダクトを開閉する弁機構と、上述の各粉塵発生設備の
駆動状態を検出して複数の粉塵発生設備の停止台数が増
加するに従って上述の吸引ブロアの回転数を低下させる
と共に該停止粉塵発生設備に臨む吸引ダクトに設けられ
た弁機構を閉弁させる制御機構とを備えた装置である。
2. Description of the Related Art Conventionally, there is a dust collecting device as described in Japanese Utility Model Laid-Open No. Sho 62-1725. That is, a transport duct connected to a dust collector having a suction blower, a suction duct connected to the transport duct and facing each of a plurality of dust generating facilities, and a valve mechanism provided in each of the suction ducts to open and close each suction duct. The driving state of each of the dust generating facilities described above is detected, and as the number of stopped dust generating facilities increases, the rotational speed of the suction blower is reduced and the suction duct is provided in the suction duct facing the stopped dust generating facilities. And a control mechanism for closing the valve mechanism.

【0003】この従来装置によれば、粉塵発生設備の停
止台数に対応して、単一の吸引ブロアの回転数を低下さ
せ、かつ弁機構を制御するので、吸引ブロアの能力を有
効に活用しつつ、同吸引ブロアのエネルギ消費を抑制す
ることができる利点がある反面、次のような問題点があ
った。
According to this conventional apparatus, the number of rotations of a single suction blower is reduced and the valve mechanism is controlled in accordance with the number of stopped dust generating facilities, so that the capacity of the suction blower is effectively utilized. While there is an advantage that the energy consumption of the suction blower can be suppressed, there are the following problems.

【0004】すなわち、上述の粉塵回収装置は単に粉塵
発生設備の停止台数のみに対応して吸引ブロアの回転数
を制御するものであるから、この従来装置を例えば溶湯
を溶解および収容する低周波溶解炉から発生される煙を
回収する装置に適用した場合、この低周波溶解炉は、そ
の運転・停止状態と炉蓋の開閉状態との両者により煙発
生量が異なるため、上述の従来装置では充分な制御を行
なうことができない問題点があった。
That is, since the above-mentioned dust collecting apparatus merely controls the number of rotations of the suction blower in accordance with only the number of stopped dust generating facilities, this conventional apparatus is used, for example, for low-frequency melting and melting of molten metal. When applied to a device that collects smoke generated from a furnace, this low-frequency melting furnace has a different amount of smoke generation depending on both the operation / stop state and the opening / closing state of the furnace lid, so that the above-described conventional apparatus is not sufficient. There was a problem that it was not possible to perform a proper control.

【0005】[0005]

【発明が解決しようとする課題】この発明の請求項1記
載の発明は、複数の溶湯収容炉の運転・停止状態と炉蓋
の開閉状態とに対応した煙発生状態に基づいて排煙手段
の煙回収能力をコントロールすることで、充分な制御を
行なうことができると共に、溶湯収容炉内の溶湯の温度
低下を抑制することができる排煙装置の提供を目的とす
る。
The invention according to claim 1 of the present invention is based on a smoke generation means based on a smoke generation state corresponding to the operation / stop state of a plurality of molten metal storage furnaces and the open / close state of the furnace lid. It is an object of the present invention to provide a smoke exhaust device capable of performing sufficient control by controlling the smoke recovery capacity and suppressing a decrease in the temperature of the molten metal in the molten metal storage furnace.

【0006】この発明の請求項2記載の発明は、上記請
求項1記載の発明の目的と併せて、炉蓋外周縁に沿って
配設されるリングフードを用いることで、煙回収能力の
大幅な向上を図ることができる排煙装置の提供を目的と
する。
The invention according to claim 2 of the present invention, in addition to the object of the invention according to claim 1, uses a ring hood disposed along the outer peripheral edge of the furnace lid, thereby greatly increasing the smoke recovery capacity. It is an object of the present invention to provide a smoke exhaust device capable of achieving significant improvement.

【0007】[0007]

【課題を解決するための手段】この発明の請求項1記載
の発明は、溶湯収容炉から発生する煙を排煙する排煙装
置であって、複数の溶湯収容炉と、上記各溶湯収容炉に
それぞれ設けられ、これら各溶湯収容炉から発生する煙
を回収する複数の煙回収手段と、上記各煙回収手段と単
一の排煙手段とを連通する煙回収通路と、上記排煙手段
の煙回収能力を可変する可変手段と、上記煙回収通路に
介設され上記煙回収能力を分配する分配手段と、上記各
溶湯収容炉の運転・停止状態を検出する第1検出手段
と、上記各溶湯収容炉における炉蓋の開閉状態を検出す
る第2検出手段と、上記第1および第2の各検出手段に
基づいて煙回収に必要な全要求能力を演算する要求量演
算手段と、上記第1および第2の各検出手段に基づいて
複数の溶湯収容炉の煙回収能力の比率を演算する比率演
算手段と、上記要求量演算手段に基づいて上記可変手段
を介して排煙手段を制御すると共に、上記比率演算手段
に基づいて上記分配手段を駆動する制御手段とを備えた
排煙装置であることを特徴とする。
According to a first aspect of the present invention, there is provided a smoke exhaust device for exhausting smoke generated from a molten metal storage furnace, comprising a plurality of molten metal storage furnaces and each of the molten metal storage furnaces. A plurality of smoke recovery means for recovering smoke generated from each of these molten metal storage furnaces, a smoke recovery passage communicating each of the smoke recovery means and a single smoke discharge means, A variable means for varying the smoke recovery capacity, a distribution means interposed in the smoke recovery passage for distributing the smoke recovery capacity, a first detection means for detecting the operation / stop state of each of the molten metal storage furnaces, Second detection means for detecting the open / closed state of the furnace lid in the molten metal storage furnace; required amount calculation means for calculating the total required capacity required for smoke recovery based on the first and second detection means; A plurality of molten metal storage furnaces based on the first and second detection means; Ratio calculating means for calculating the ratio of the collecting capacity, and control means for controlling the smoke exhaust means via the variable means based on the required amount calculating means and driving the distribution means based on the ratio calculating means. Characterized in that it is a smoke exhaust device provided with:

【0008】この発明の請求項2記載の発明は、上記請
求項1記載の発明の構成と併せて、上記煙回収手段は上
記溶湯収容炉の炉蓋外周縁に沿って配設されたリングフ
ードにより構成された排煙装置であることを特徴とす
る。
According to a second aspect of the present invention, in addition to the configuration of the first aspect of the present invention, the ring hood is provided such that the smoke recovery means is disposed along the outer peripheral edge of the furnace lid of the molten metal storage furnace. Characterized in that it is a smoke exhaust device constituted by:

【0009】[0009]

【発明の効果】この発明の請求項1記載の発明によれ
ば、図8にクレーム対応図で示すように、第1検出手段
P1は複数の溶湯収容炉P2,P3の運転・停止状態を
検出し、第2検出手段P4は上述の複数の溶湯収容炉P
2,P3におけるそれぞれの炉蓋P5,P6の開閉状態
を検出する。また要求量演算手段P7は上述の各検出手
段P1,P4からの出力に基づいて煙回収に必要な全要
求能力を演算する一方、比率演算手段P8は上述の各検
出手段P1,P4からの出力に基づいて複数の溶湯収容
炉P2,P3に要する煙回収能力の比率を演算する。そ
して制御手段P9は、可変手段P10を介して上述の全
要求能力を満たす必要最小限の制御力にて排煙手段P1
1を駆動制御すると共に、分配手段P12,P13を上
述の比率に対応して駆動する。
According to the first aspect of the present invention, as shown in the claim correspondence diagram of FIG. 8, the first detecting means P1 detects the operation / stop state of the plurality of molten metal storage furnaces P2 and P3. The second detecting means P4 is connected to the plurality of molten metal storage furnaces P described above.
The open / closed state of the furnace lids P5 and P6 in P2 and P3 is detected. The required amount calculating means P7 calculates the total required capacity required for smoke recovery based on the output from each of the detecting means P1 and P4, while the ratio calculating means P8 calculates the output from each of the detecting means P1 and P4. Based on the above, the ratio of the smoke recovery capacity required for the plurality of molten metal storage furnaces P2 and P3 is calculated. Then, the control means P9 controls the smoke exhaust means P1 with the minimum necessary control force that satisfies the above-mentioned all required capabilities via the variable means P10.
1 and drive the distribution means P12 and P13 in accordance with the above ratio.

【0010】この結果、複数の溶湯収容炉P2,P3か
ら発生される煙は、運転、停止状態および炉蓋P5,P
6の開閉状態に対応した煙回収に必要最小限の能力に
て、煙回収手段P14,P15、煙回収通路P16を介
して単一の排煙手段P11に回収される。
As a result, the smoke generated from the plurality of molten metal storage furnaces P2 and P3 is in operation, in the stopped state, and in the furnace lids P5 and P3.
The smoke collection means P14 and P15 and the smoke collection passage P16 collect the smoke into a single smoke exhaust means P11 with the minimum necessary capacity for the smoke collection corresponding to the open / close state of No. 6.

【0011】このように、複数の溶湯収容炉の運転、停
止状態と炉蓋の開閉状態とに対応した煙発生状態に基づ
いて上述の制御手段が排煙手段の煙回収能力をコントロ
ールするので、充分な制御を行なうことができると共
に、炉蓋閉時には当該溶湯収容炉に対する煙回収能力が
小さくなるように制御されるので、溶湯収容炉内の溶湯
の温度低下を抑制することができる効果がある。
As described above, the above-mentioned control means controls the smoke collection capability of the smoke exhaust means based on the smoke generation state corresponding to the operation and stop states of the plurality of molten metal storage furnaces and the open / close state of the furnace lid. Sufficient control can be performed, and when the furnace lid is closed, the smoke recovery capability for the molten metal storage furnace is controlled so as to be small, so that there is an effect that a decrease in the temperature of the molten metal in the molten metal storage furnace can be suppressed. .

【0012】この発明の請求項2記載の発明によれば、
上記請求項1記載の発明の効果と併せて、上述の煙回収
手段を溶湯収容炉の炉蓋外周縁に沿設されるリングフー
ドで構成したので、煙回収能力の大幅な向上を図ること
ができる効果がある。
According to the second aspect of the present invention,
In addition to the effect of the first aspect of the present invention, since the above-mentioned smoke recovery means is constituted by a ring hood provided along the outer peripheral edge of the furnace lid of the molten metal storage furnace, it is possible to greatly improve the smoke recovery capacity. There is an effect that can be done.

【0013】[0013]

【実施例】この発明の一実施例を以下図面に基づいて詳
述する。図1は本発明の排煙装置を備えた砂型鋳造装置
全体を示す系統図で、鋳型を造型する静圧造型機1、上
型および下型に対応して造型された砂型にガス抜き孔を
穿孔する穿孔機2、上型のみを反転させる反転装置3、
砂型表面の砂欠片を払い落とすサンドカッタ4、必要に
応じて砂型内に中子を配設する中子セット装置5、注湯
時の圧力で砂型が膨張するため、予め砂型を押圧する重
錘セット装置6、砂型に形成されたキャビティ内に溶湯
を自動注湯する自動注湯機7を設け、これらの各装置1
〜7を平面から見て左方から右方に向けて略一直線状に
配設し、自動注湯後の部位を折返し点8として、この折
返し点8には平面から見て右方から左方へ延びる比較的
長い枠内冷却ライン9を接続している。
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS One embodiment of the present invention will be described below in detail with reference to the drawings. FIG. 1 is a system diagram showing an entire sand mold casting apparatus provided with a smoke exhaust device according to the present invention. In FIG. 1, a static pressure molding machine 1 for molding a mold and gas vent holes are formed in a sand mold molded corresponding to an upper mold and a lower mold. Drilling machine 2 for punching, reversing device 3 for reversing only the upper die,
Sand cutter 4 for removing sand fragments on the surface of the sand mold, core setting device 5 for disposing cores in the sand mold as required, and weight for pressing the sand mold in advance because the sand mold expands due to the pressure during pouring. A setting device 6 and an automatic pouring machine 7 for automatically pouring molten metal into a cavity formed in a sand mold are provided.
7 are arranged substantially in a straight line from left to right as viewed from the plane, and the part after the automatic pouring is referred to as a turning point 8, and this turning point 8 is located from the right to the left as viewed from the plane. A relatively long in-frame cooling line 9 is connected.

【0014】上述の枠内冷却ライン9の終端部の次段に
設定された解枠ステーション10には、鋳枠から鋳物内
蔵砂型を抜き取るパンチアップ装置11を配設し、この
パンチアップ装置11の次段にはオシレートコンベア1
2を介して砂と鋳物(製品)とを分離するドラムシェー
カ13を配設している。
A punching-up device 11 for extracting a sand mold with a built-in casting from a casting flask is provided at a release station 10 set at a stage next to the terminal end of the in-frame cooling line 9. Oscillate conveyor 1 in the next stage
2, a drum shaker 13 for separating sand and casting (product) is provided.

【0015】さらに上述のドラムシェーカ13の次段に
もオシレートコンベア14を配設し、このオシレートコ
ンベア14の砂落下口の下部からロータリスクリーン1
5を介して砂を矢印a方向へ搬送すべく構成する一方、
上述のオシレートコンベア14の製品出口部から取出さ
れた製品を、ハンガを有するオーバヘッドコンベア16
で矢印b方向へ搬送すべく構成している。
Further, an oscillating conveyor 14 is provided at the next stage of the above-mentioned drum shaker 13, and a rotary screen 1 is provided from the lower part of the sand falling port of the oscillating conveyor 14.
5 to convey the sand in the direction of the arrow a,
The product taken out from the product outlet of the above-mentioned oscillation conveyor 14 is transferred to an overhead conveyor 16 having a hanger.
To convey in the direction of arrow b.

【0016】上述の自動注湯機7の右方には、例えば2
基の低周波溶解炉17A,17Bを設け、これら第1お
よび第2の各低周波溶解炉17A,17Bから発生する
煙を煙回収ダクト18を介して吸引ファン19で吸引す
べく構成している。
On the right side of the above automatic pouring machine 7, for example, 2
The low-frequency melting furnaces 17A and 17B are provided, and smoke generated from the first and second low-frequency melting furnaces 17A and 17B is sucked by a suction fan 19 through a smoke collection duct 18. .

【0017】また上述の各低周波溶解炉17A,17B
の前部と自動注湯機7との間には軌道20,20を敷設
し、これらの軌道20,20上を移動する移動台車21
には取鍋22を上載する一方、図1に仮想線で示す如く
必要箇所は気流遮断、防音、防塵を兼ねる隔壁23,2
4で囲繞している。
Each of the low-frequency melting furnaces 17A and 17B described above
Tracks 20 and 20 are laid between the front of the machine and the automatic pouring machine 7, and a moving carriage 21 that moves on these tracks 20 and 20
The ladle 22 is placed on top of the partition wall 23, and as shown by phantom lines in FIG.
It is surrounded by 4.

【0018】ところで、上述の各低周波溶解炉17A,
17Bから発生される煙を回収および排煙する排煙装置
は図2、図3、図4に示す如く構成している。
By the way, each of the above-mentioned low-frequency melting furnaces 17A, 17A,
The smoke exhaust device that collects and emits the smoke generated from 17B is configured as shown in FIG. 2, FIG. 3, and FIG.

【0019】すなわち、上述の各低周波溶解炉17A,
17Bにおけるそれぞれの炉蓋25,25の外周縁に沿
ってリングフード26,26を配設し、これら各リング
フード26,26には例えば耐熱性フレキシブルダクト
により構成される連通ダクト27,27およびスイベル
(swivel)28,28を介して独立回収ダクト29,2
9の上流端を連通接続し、これら各独立回収ダクト2
9,29の下流部を合流させて集合部30を形成し、こ
の集合部30と吸引ファン19の吸引部との間を、一本
の共通回収ダクト31で連通接続している。
That is, the low-frequency melting furnaces 17A, 17A,
Ring hoods 26, 26 are arranged along the outer peripheral edges of the respective furnace lids 25, 25 in 17B, and these ring hoods 26, 26 have communication ducts 27, 27 and a swivel, for example, composed of heat-resistant flexible ducts. (Swivel) Independent recovery duct 29,2 via 28,28
9 is connected in communication with the upstream end of each of these independent collection ducts 2.
The downstream portions 9 and 29 are joined to form a collecting portion 30, and the collecting portion 30 and the suction portion of the suction fan 19 are connected by a single common collection duct 31.

【0020】ここで、上述の煙回収ダクト18は独立回
収ダクト29,29と共通回収ダクト31とにより構成
される一方、上述の吸引ファン19にはファンモータ3
2の回転力が、同ファンモータ32の回転軸に嵌合した
原動プーリ33と、ベルト34と、ファン側の従動プー
リ35とを介して伝達される。
Here, the above-mentioned smoke collecting duct 18 is composed of independent collecting ducts 29, 29 and a common collecting duct 31, while the above-mentioned suction fan 19 has a fan motor 3
2 is transmitted via a driving pulley 33 fitted to the rotation shaft of the fan motor 32, a belt 34, and a driven pulley 35 on the fan side.

【0021】また、上述の各スイベル28,28はそれ
ぞれの低周波溶解炉17A,17Bの傾動支点もしくは
傾動支点近傍に配設される一方、これら各低周波溶解炉
17A,17Bは、溶解室36を構成するライニング部
材37と、炉蓋25と、傾動用シリンダと、通電コイル
(図示せず)とを備え、この通電コイルへの通電により
炉内の溶解金属(材料)中に誘導電流を生じさせ、ジュ
ール熱によって材料を溶解して、溶湯Mになすものであ
る。
The above-mentioned swivels 28, 28 are disposed at or near the tilting fulcrum of the low-frequency melting furnaces 17A, 17B, while the low-frequency melting furnaces 17A, 17B are provided with a melting chamber 36. And a furnace cover 25, a tilting cylinder, and an energizing coil (not shown). When an electric current is supplied to the energizing coil, an induced current is generated in the molten metal (material) in the furnace. Then, the material is melted by Joule heat to form the molten metal M.

【0022】さらに上述の各低周波溶解炉17A,17
Bと一体的に傾動される炉体38,38の上面には、出
湯時に煙を出湯口39,39側へ強制流動させるための
第1、第2のエア吐出装置40,41を取付けている。
Further, each of the low-frequency melting furnaces 17A, 17
First and second air discharge devices 40, 41 for forcibly flowing smoke to the tap holes 39, 39 at the time of tapping are attached to the upper surfaces of the furnace bodies 38, 38 that are tilted integrally with B. .

【0023】上述の各低周波炉17A,17Bの軌道2
0を隔てた反対側には架構42を立設し、この架構42
の上部には出湯時の煙を吸引回収する吸引ファン43,
43(但し、図面では一方のみを示す)を取付けると共
に、各低周波溶解炉17A,17Bの傾動時(図4参
照)における出湯口39,39上方および移動台車21
上の取鍋22上方と対向して、煙回収フード44,44
を配設し、これら各煙回収フード44,44を上述の架
構42に固定している。
The orbit 2 of each of the low-frequency furnaces 17A and 17B described above.
A frame 42 is erected on the opposite side of the frame
The suction fan 43 that sucks and collects smoke from the hot water
43 (however, only one is shown in the drawing), and at the time of tilting of each of the low-frequency melting furnaces 17A, 17B (see FIG. 4), above the tap holes 39, 39 and the movable carriage 21.
Opposite to the upper ladle 22, the smoke collection hoods 44, 44
Are arranged, and these smoke collection hoods 44, 44 are fixed to the above-mentioned frame 42.

【0024】上述の各煙回収フード44,44の連通口
45,45と、上述の各吸引ファン43,43の吸引部
とを連通ダクト46,46で互に連通接続し、これら各
吸引ファン43,43の吐出部には排煙ダクト47,4
7を接続している。
The communication ports 45, 45 of the smoke collecting hoods 44, 44 and the suction portions of the suction fans 43, 43 are connected to each other via communication ducts 46, 46, and the suction fans 43, 43 are connected to each other. , 43 are provided at the discharge section.
7 is connected.

【0025】一方、上述の煙回収ダクト18における独
立回収ダクト29,29の内部には単一の吸引ファン1
9の煙回収能力を分配するための分配手段としての第1
バルブ48、第2バルブ49を各別に取付け、これら各
バルブ48,49を、第1、第2の各アクチュエータ5
0,51(図6参照)で開閉駆動すべく構成している。
On the other hand, a single suction fan 1 is provided inside the independent collecting ducts 29, 29 in the above-mentioned smoke collecting duct 18.
9 as the distribution means for distributing the smoke recovery capacity
A valve 48 and a second valve 49 are separately mounted, and these valves 48 and 49 are connected to the first and second actuators 5 respectively.
It is configured to open and close at 0, 51 (see FIG. 6).

【0026】上述の第1および第2の各エア吐出装置4
0,41は出湯時にエアカーテン52,53(図5参
照)を形成して、同出湯時に発生する煙を煙回収フード
44,44側へ強制流動させるためのもので、これらの
エアカーテン52,53の空気圧回路は例えば図5に示
す如く構成している。すなわち、モータ54で駆動され
るエアコンプレッサ55の吐出ライン56に、アフタク
ーラ57、空気圧タンク58、メインラインフィルタ5
9、ドライヤ60を介して各エアライン61,62を接
続し、これら各エアライン61,62を上述の各エア吐
出装置40,41に連通接続する一方、上述の空気圧タ
ンク58とメインラインフィルタ59との間の空気圧で
圧力スイッチ63を介して上述のモータ54を制御すべ
く構成している。なお、必要に応じて上述の各エアライ
ン61,62にはソレノイド開閉弁を設ける。
The above-described first and second air discharge devices 4
Numerals 0, 41 form air curtains 52, 53 (see FIG. 5) at the time of tapping and force the smoke generated at the time of tapping to flow toward the smoke collecting hoods 44, 44. The pneumatic circuit 53 is configured, for example, as shown in FIG. That is, an aftercooler 57, an air pressure tank 58, and a main line filter 5 are connected to a discharge line 56 of an air compressor 55 driven by a motor 54.
9. The respective air lines 61 and 62 are connected via the dryer 60, and the respective air lines 61 and 62 are connected to the respective air discharge devices 40 and 41, while the aforementioned air pressure tank 58 and the main line filter 59 are connected. The motor 54 is configured to be controlled via the pressure switch 63 with the air pressure between the motor 54 and the motor 54. It should be noted that a solenoid on-off valve is provided in each of the air lines 61 and 62 as required.

【0027】図6は排煙装置の制御回路を示し、CPU
70は第1低周波溶解炉17Aの運転、停止状態を検出
する第1電源スイッチ64と、第2低周波溶解炉17B
の運転、停止状態を検出する第2電源スイッチ65と、
第1低周波溶解炉17Aにおける炉蓋25の開閉状態を
検出する第1リミットスイッチ66と、第2低周波溶解
炉17Bにおける炉蓋25の開閉状態を検出する第2リ
ミットスイッチ67との各出力信号に基づいて、ROM
68に格納されたプログラムに従って、第1、第2の各
アクチュエータ50,51、周波数変換装置としてのイ
ンバータ69、第1、第2の各エア吐出装置40,41
を駆動制御し、またRAM71は必要なデータやマップ
等を記憶する。
FIG. 6 shows a control circuit of the smoke exhaust device,
Reference numeral 70 denotes a first power switch 64 for detecting the operation / stop state of the first low frequency melting furnace 17A, and a second low frequency melting furnace 17B.
A second power switch 65 for detecting the operation / stop state of the
Outputs of a first limit switch 66 for detecting the open / closed state of the furnace lid 25 in the first low-frequency melting furnace 17A and a second limit switch 67 for detecting the open / closed state of the furnace lid 25 in the second low-frequency melting furnace 17B. ROM based on signal
The first and second actuators 50 and 51, the inverter 69 as a frequency conversion device, and the first and second air discharge devices 40 and 41 in accordance with the program stored in the storage device 68.
, And the RAM 71 stores necessary data, maps, and the like.

【0028】ここで、上述のCPU70は、第1および
第2の各電源スイッチ64,65と、第1および第2の
各リミットスイッチ66,67の出力に基づいて煙回収
に必要な最小限の全要求能力を演算する要求量演算手段
(図7に示すフローチャートの第3ステップS3参照)
と、上述の各電源スイッチ64,65および各リミット
スイッチ66,67の出力に基づいて2基の低周波溶解
炉17A,17Bの煙回収能力の比率を演算する比率演
算手段(図7に示すフローチャートの第4ステップS4
参照)と、上述の要求量演算手段の演算結果に基づいて
可変手段としてのインバータ69を介してファンモータ
32の回転数乃至吸引ファン19による風量を可変制御
すると共に、上述の比率演算手段の演算結果に基づいて
分配手段による第1バルブ48、第2バルブ49を開閉
制御する制御手段(図7に示すフローチャートの第5ス
テップS5参照)とを兼ねる。
Here, the CPU 70 described above controls the minimum power required for smoke recovery based on the outputs of the first and second power switches 64 and 65 and the outputs of the first and second limit switches 66 and 67. Requested amount calculating means for calculating the total required capacity (refer to the third step S3 in the flowchart shown in FIG. 7)
And ratio calculating means for calculating the ratio of the smoke collection capacity of the two low-frequency melting furnaces 17A and 17B based on the outputs of the power switches 64 and 65 and the limit switches 66 and 67 (flow chart shown in FIG. 7). 4th step S4
), And variably controls the number of rotations of the fan motor 32 or the air flow rate by the suction fan 19 via an inverter 69 as a variable means based on the calculation result of the required amount calculation means. Based on the result, it also serves as a control unit (see the fifth step S5 in the flowchart shown in FIG. 7) for controlling the opening and closing of the first valve 48 and the second valve 49 by the distribution unit.

【0029】なお、この実施例においては各低周波溶解
炉17A,17Bの運転、停止、並びに炉蓋25の開閉
によるインバータ69の設定周波数と、各バルブ48,
49の開閉状態と、風量とは次の[表1]で示すように
設定され、これら設定内容は上述のRAM71にマップ
として記憶してもよい。
In this embodiment, the set frequency of the inverter 69 by operating and stopping the low-frequency melting furnaces 17A and 17B, and opening and closing the furnace lid 25, and the respective valves 48 and
The open / close state of 49 and the air volume are set as shown in the following [Table 1], and these set contents may be stored as a map in the RAM 71 described above.

【0030】[0030]

【表1】 [Table 1]

【0031】このように構成した排煙装置の作用を、図
7のフローチャートを参照して以下に詳述する。
The operation of the smoke exhaust device configured as described above will be described in detail below with reference to the flowchart of FIG.

【0032】第1ステップS1で、CPU70は第1お
よび第2の電源スイッチ64,65からの信号に基づい
て各低周波溶解炉17A,17Bの運転状態を読込む。
In a first step S1, the CPU 70 reads the operating state of each of the low-frequency melting furnaces 17A and 17B based on signals from the first and second power switches 64 and 65.

【0033】次に第2ステップS2で、CPU70は第
1および第2の各リミットスイッチ66,67からの信
号に基づいて各低周波溶解炉17A,17Bにおける炉
蓋25,25の開閉状態を読込む。
Next, in a second step S2, the CPU 70 reads the open / closed state of the furnace lids 25, 25 in each of the low frequency melting furnaces 17A, 17B based on the signals from the first and second limit switches 66, 67. Put in.

【0034】次に第3ステップS3で、CPU70は各
低周波溶解炉17A,17Bの運転、停止状態、並びに
各低周波溶解炉17A,17Bにおける炉蓋25,25
の開閉状態すなわち煙発生状態に対応して、2基の低周
波溶解炉17A,17Bから発生する煙を回収するのに
必要な全要求能力(必要最小限の値)を演算する。
Next, in a third step S3, the CPU 70 operates and stops each of the low-frequency melting furnaces 17A and 17B, as well as the furnace lids 25 and 25 in each of the low-frequency melting furnaces 17A and 17B.
The required capacity (required minimum value) required to recover the smoke generated from the two low-frequency melting furnaces 17A and 17B is calculated in accordance with the open / closed state, that is, the smoke generation state.

【0035】次に第4ステップS4で、CPU70は上
述各電源スイッチ64,65からのON,OFF信号
と、上述の各リミットスイッチ66,67からのON,
OFF信号とに基づいて、2基の低周波溶解炉17A,
17Bの煙回収能力の比率を演算する。すなわち上述の
必要最小限の値(具体的には風量)に相当する全要求能
力を2基の低周波溶解炉17A,17Bに対して如何に
分配するかという分配比率を求める。
Next, in a fourth step S4, the CPU 70 turns ON / OFF signals from the power switches 64, 65 and ON / OFF signals from the limit switches 66, 67.
Based on the OFF signal, two low-frequency melting furnaces 17A,
Calculate the 17B smoke recovery capacity ratio. That is, a distribution ratio is determined as to how to distribute the total required capacity corresponding to the above-described minimum value (specifically, the air volume) to the two low-frequency melting furnaces 17A and 17B.

【0036】次に第5ステップS5で、CPU70は必
要最小限の値としての全要求能力に対応して、インバー
タ69を介してファンモータ32を駆動制御すると共
に、上述の分配比率に対応して各アクチュエータ50,
51を介して第1バルブ48、第2バルブ49を開閉制
御する。
Next, in a fifth step S5, the CPU 70 controls the drive of the fan motor 32 via the inverter 69 in accordance with the total required capacity as a necessary minimum value, and in accordance with the distribution ratio described above. Each actuator 50,
The first valve 48 and the second valve 49 are controlled to open and close via 51.

【0037】以上の説明を上述の表1に基づいて更に詳
細に述べると、表1の上から1段目に示すように、第1
低周波溶解炉17Aが運転状態、該溶解炉17Aの炉蓋
25が開、第2低周波溶解炉17Bが運転状態、該溶解
炉17Bの炉蓋25が開で、図6に示す全てのスイッチ
64,65,66,67がONの時には、CPU70は
インバータ69の周波数を60Hz、全要求能力に相当
する風量を350 m3/min 、各バルブ48,49によ
る分配比率を50:50として、ファンモータ32を駆
動すると共に、アクチュエータ50,51を介して第1
バルブ48および第2バルブ49を共に開成する。
The above description will be described in more detail based on Table 1 described above.
When the low-frequency melting furnace 17A is operating, the furnace lid 25 of the melting furnace 17A is open, the second low-frequency melting furnace 17B is operating, the furnace lid 25 of the melting furnace 17B is open, and all switches shown in FIG. When the switches 64, 65, 66, and 67 are ON, the CPU 70 sets the frequency of the inverter 69 to 60 Hz, the air volume corresponding to the total required capacity to 350 m 3 / min, and the distribution ratio by the valves 48 and 49 to 50:50. While driving the motor 32, the first
The valve 48 and the second valve 49 are both opened.

【0038】上述の材料投入時に相当する上記条件下に
おいて各低周波溶解炉17A,17Bから発生する煙
は、リングフード26、連通ダクト27、スイベル2
8、独立回収ダクト29、集合部30、共通回収ダクト
31を介して吸引ファン19に回収された後に、この吸
引ファン19内のインペラの回転によりその吐出部から
排煙ダクト72を介して排煙される。
The smoke generated from each of the low-frequency melting furnaces 17A and 17B under the above-described conditions corresponding to the above-described material charging time is supplied to the ring hood 26, the communication duct 27, and the swivel 2
8, after being collected by the suction fan 19 through the independent collection duct 29, the collecting part 30, and the common collection duct 31, smoke is discharged from the discharge part thereof through the smoke discharge duct 72 by the rotation of the impeller in the suction fan 19. Is done.

【0039】一方、表1の上から6段目に示すように、
第1低周波溶解炉17Aが運転状態、同溶解炉17Aの
炉蓋25が閉、第2低周波溶解炉17Bが停止状態で、
図6に示す第1電源スイッチ64のみがONの時には、
CPU70はインバータ69の周波数を30Hz、全要
求能力に相当する風量を100 m3 /min 、各バルブ4
8,49による分配比率を100:0として、ファンモ
ータ32を駆動すると共に、各アクチュエータ50,5
1を介して一方の第1バルブ48を開成し、他方の第2
バルブ49を閉成して、稼動中の第1低周波溶解炉17
Aから発生する煙を、各要素26,27,28,29,
30,30,19,72を介して回収および排煙する。
On the other hand, as shown in the sixth row from the top of Table 1,
When the first low-frequency melting furnace 17A is in the operating state, the furnace lid 25 of the first melting furnace 17A is closed, and the second low-frequency melting furnace 17B is stopped,
When only the first power switch 64 shown in FIG. 6 is ON,
The CPU 70 sets the frequency of the inverter 69 to 30 Hz, the air volume corresponding to the total required capacity to 100 m 3 / min,
The fan motor 32 is driven while the distribution ratio of the actuators 50 and 5 is set to 100: 0.
1, one first valve 48 is opened and the other second valve 48 is opened.
The first low-frequency melting furnace 17 in operation is closed by closing the valve 49.
Smoke generated from A is transmitted to each element 26, 27, 28, 29,
Collect and exhaust via 30, 30, 19, 72.

【0040】なお、その他の各種条件時には上述の表1
で示すようにインバータ69の周波数および必要最小限
の風量がそれぞれ設定され、第1バルブ48および第2
バルブ49が開閉制御される一方、出湯時には図4に示
す如く出湯中の低周波溶解炉17A,17Bに対応する
エア吐出装置40,41が駆動され、同装置40,41
のスリット状のエア吐出口から吐出されるエアによりエ
アカーテン52,53を形成し、このエアカーテン5
2,53で出湯中の低周波溶解炉17A,17Bおよび
取鍋22周辺から発生される煙を煙回収フード44,4
4側へ強制流動させ、かつ吸引ファン43の回転により
同煙回収フード44で吸引回収した煙を各要素45,4
6,43,47を介して排煙する。
In the case of other various conditions, the above Table 1 was used.
The frequency of the inverter 69 and the minimum required airflow are set as shown by
While the valve 49 is controlled to open and close, at the time of tapping, the air discharge devices 40 and 41 corresponding to the low-frequency melting furnaces 17A and 17B during tapping are driven as shown in FIG.
The air curtains 52 and 53 are formed by air discharged from the slit-shaped air discharge ports of the air curtain 5.
Smoke generated from the low-frequency melting furnaces 17A, 17B and the ladle 22 during tapping at 2 and 53 is supplied to the smoke recovery hoods 44 and 4, respectively.
4 and the smoke suctioned and collected by the smoke collection hood 44 by the rotation of the suction fan 43.
Exhaust smoke through 6, 43, 47.

【0041】このように複数の低周波溶解炉17A,1
7Bの運転・停止状態と、各溶解炉17A,17Bにお
ける炉蓋25,25の開閉状態とに対応した煙発生状態
に基づいて上述の制御手段(図7に示すフローチャート
の第5ステップS5参照)がインバータ69を介してフ
ァンモータ32の回転数を必要最小限にコントロールす
るので、吸引ファン19およびファンモータ32からな
る排煙手段の能力を有効に利用しつつ、該排煙手段の消
費エネルギを抑制することができるのは勿論、2つのパ
ラメータにより変化する煙発生状態に対応した充分な制
御を行なうことができる効果がある。
As described above, the plurality of low frequency melting furnaces 17A, 1
7B based on the smoke generation state corresponding to the operation / stop state of 7B and the open / close state of the furnace lids 25 in each of the melting furnaces 17A and 17B (see the fifth step S5 in the flowchart shown in FIG. 7). Controls the number of revolutions of the fan motor 32 to a necessary minimum via the inverter 69, so that the energy consumption of the smoke exhaust unit can be reduced while effectively utilizing the capacity of the smoke exhaust unit including the suction fan 19 and the fan motor 32. Of course, there is an effect that sufficient control corresponding to the smoke generation state that is changed by two parameters can be performed.

【0042】また上述の表1および図7のフローチャー
トからも明らかなように、炉蓋25の閉時には、当該低
周波溶解炉17A,17Bに対する煙回収能力が小さく
なるように制御されるので、当該低周波溶解炉17A,
17B内の溶湯Mの温度低下を抑制することができる効
果がある。
As is clear from the above-mentioned Table 1 and the flow chart of FIG. 7, when the furnace lid 25 is closed, the low-frequency melting furnaces 17A and 17B are controlled so as to reduce the smoke recovery capacity. Low frequency melting furnace 17A,
There is an effect that the temperature drop of the molten metal M in 17B can be suppressed.

【0043】加えて、煙回収手段として上述のリングフ
ード26を用いると、煙回収能力の大幅な向上を図るこ
とができると共に、低周波溶解炉17A,17Bの上方
余剰空間を同炉内部への材料投入用の材料投入搬送コン
ベアの配設スペースとして有効利用することができる効
果がある。
In addition, when the above-described ring hood 26 is used as the smoke collecting means, the smoke collecting capacity can be greatly improved, and the excess space above the low-frequency melting furnaces 17A and 17B can be provided inside the furnace. There is an effect that the material can be effectively used as a space for arranging a material charging conveyor for material charging.

【0044】この発明の構成と、上述の実施例との対応
において、この発明の溶湯収容炉は、実施例の第1およ
び第2の低周波溶解炉17A,17Bに対応し、以下同
様に、煙回収手段は、リングフード26に対応し、排煙
手段は、吸引ファン19およびファンモータ32に対応
し、煙回収通路は、煙回収ダクト18に対応し、分配手
段は、第1バルブ48および第2バルブ49に対応し、
第1検出手段は、第1電源スイッチ64および第2電源
スイッ65に対応し、第2検出手段は、第1リミットス
イッチ66および第2リミットスイッチ67に対応し、
可変手段は、インバータ69に対応し、要求量演算手段
は、CPU70制御による第3ステップS3に対応し、
比率演算手段は、CPU70制御による第4ステップS
4に対応し、制御手段は、CPU70制御による第5ス
テップS5に対応するも、この発明は、上述の実施例の
構成のみに限定されるものではない。
In correspondence between the configuration of the present invention and the above-described embodiment, the molten metal storage furnace of the present invention corresponds to the first and second low frequency melting furnaces 17A and 17B of the embodiment. The smoke collecting means corresponds to the ring hood 26, the smoke exhausting means corresponds to the suction fan 19 and the fan motor 32, the smoke collecting passage corresponds to the smoke collecting duct 18, and the distributing means corresponds to the first valve 48 and Corresponding to the second valve 49,
The first detecting means corresponds to the first power switch 64 and the second power switch 65, the second detecting means corresponds to the first limit switch 66 and the second limit switch 67,
The variable means corresponds to the inverter 69, the required amount calculation means corresponds to the third step S3 controlled by the CPU 70,
The ratio calculating means performs the fourth step S under the control of the CPU 70.
4, the control means corresponds to the fifth step S5 under the control of the CPU 70, but the present invention is not limited to only the configuration of the above-described embodiment.

【図面の簡単な説明】[Brief description of the drawings]

【図1】本発明の排煙装置を備えた砂型鋳造装置の系統
図。
FIG. 1 is a system diagram of a sand casting device provided with a smoke exhaust device of the present invention.

【図2】本発明の排煙装置を示す平面視図。FIG. 2 is a plan view showing the smoke exhaust device of the present invention.

【図3】図2の側面図。FIG. 3 is a side view of FIG. 2;

【図4】出湯時の説明図。FIG. 4 is an explanatory view at the time of tapping.

【図5】エア吐出装置に対する空気圧源を示す空気圧回
路図。
FIG. 5 is a pneumatic circuit diagram showing an air pressure source for the air discharge device.

【図6】制御回路ブロック図。FIG. 6 is a control circuit block diagram.

【図7】排煙制御を示すフローチャート。FIG. 7 is a flowchart showing smoke control.

【図8】クレーム対応図。FIG. 8 is a diagram corresponding to claims.

【符号の説明】[Explanation of symbols]

17A,17B…低周波溶解炉 18…煙回収ダクト 19…吸引ファン 25…炉蓋 26…リングフード 32…ファンモータ 48,49…バルブ 64,65…電源スイッチ 66,67…リミットスイッチ 69…インバータ S3…要求量演算手段 S4…比率演算手段 S5…制御手段 17A, 17B: Low frequency melting furnace 18: Smoke collection duct 19: Suction fan 25 ... Furnace lid 26 ... Ring hood 32 ... Fan motor 48, 49 ... Valve 64, 65 ... Power switch 66, 67 ... Limit switch 69 ... Inverter S3 ... Requested amount calculation means S4 ... Ratio calculation means S5 ... Control means

───────────────────────────────────────────────────── フロントページの続き (56)参考文献 特開 昭58−29567(JP,A) 特開 平4−32691(JP,A) 特開 昭62−144728(JP,A) 特開 昭62−56775(JP,A) 特開 昭62−56774(JP,A) 特開 昭52−103305(JP,A) 実開 平3−24361(JP,U) 実開 平1−143653(JP,U) 実開 昭54−136322(JP,U) 実開 昭55−77562(JP,U) (58)調査した分野(Int.Cl.7,DB名) B22D 43/00 F27D 17/00 104 ──────────────────────────────────────────────────続 き Continuation of front page (56) References JP-A-58-29567 (JP, A) JP-A-4-32691 (JP, A) JP-A-62-144728 (JP, A) JP-A-62-144728 56775 (JP, A) JP-A-62-56774 (JP, A) JP-A-52-103305 (JP, A) JP-A-3-24361 (JP, U) JP-A-1-143365 (JP, U) Japanese Utility Model Application Showa 54-136322 (JP, U) Japanese Utility Model Application Showa 55-77562 (JP, U) (58) Fields investigated (Int. Cl. 7 , DB name) B22D 43/00 F27D 17/00 104

Claims (2)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】溶湯収容炉から発生する煙を排煙する排煙
装置であって、複数の溶湯収容炉と、上記各溶湯収容炉
にそれぞれ設けられ、これら各溶湯収容炉から発生する
煙を回収する複数の煙回収手段と、上記各煙回収手段と
単一の排煙手段とを連通する煙回収通路と、上記排煙手
段の煙回収能力を可変する可変手段と、上記煙回収通路
に介設され上記煙回収能力を分配する分配手段と、上記
各溶湯収容炉の運転・停止状態を検出する第1検出手段
と、上記各溶湯収容炉における炉蓋の開閉状態を検出す
る第2検出手段と、上記第1および第2の各検出手段に
基づいて煙回収に必要な全要求能力を演算する要求量演
算手段と、上記第1および第2の各検出手段に基づいて
複数の溶湯収容炉の煙回収能力の比率を演算する比率演
算手段と、上記要求量演算手段に基づいて上記可変手段
を介して排煙手段を制御すると共に、上記比率演算手段
に基づいて上記分配手段を駆動する制御手段とを備えた
排煙装置。
1. A smoke exhaust device for exhausting smoke generated from a molten metal storage furnace, comprising: a plurality of molten metal storage furnaces; and a plurality of the molten metal storage furnaces. A plurality of smoke collecting means to be collected, a smoke collecting passage communicating each of the smoke collecting means and a single smoke exhausting means, a variable means for varying a smoke collecting ability of the smoke exhausting means, and a smoke collecting passage. Distribution means interposed for distributing the smoke collection capacity, first detection means for detecting the operation / stop state of each of the molten metal storage furnaces, and second detection for detecting the open / closed state of the furnace lid in each of the molten metal storage furnaces Means, required amount calculating means for calculating the total required capacity required for smoke recovery based on the first and second detecting means, and a plurality of molten metal storages based on the first and second detecting means. A ratio calculating means for calculating the ratio of the smoke recovery capacity of the furnace; Controls the flue gas section through the variable means based on the amount computing means, flue gas and control means for driving the dispensing means based on said ratio calculation means.
【請求項2】上記煙回収手段は上記溶湯収容炉の炉蓋外
周縁に沿って配設されたリングフードにより構成された
請求項1記載の排煙装置。
2. The smoke exhaust device according to claim 1, wherein said smoke collecting means is constituted by a ring hood disposed along an outer peripheral edge of a furnace lid of said molten metal storage furnace.
JP05015293A 1993-02-15 1993-02-15 Smoke exhaust system Expired - Lifetime JP3157330B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP05015293A JP3157330B2 (en) 1993-02-15 1993-02-15 Smoke exhaust system

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP05015293A JP3157330B2 (en) 1993-02-15 1993-02-15 Smoke exhaust system

Publications (2)

Publication Number Publication Date
JPH06238431A JPH06238431A (en) 1994-08-30
JP3157330B2 true JP3157330B2 (en) 2001-04-16

Family

ID=12851216

Family Applications (1)

Application Number Title Priority Date Filing Date
JP05015293A Expired - Lifetime JP3157330B2 (en) 1993-02-15 1993-02-15 Smoke exhaust system

Country Status (1)

Country Link
JP (1) JP3157330B2 (en)

Also Published As

Publication number Publication date
JPH06238431A (en) 1994-08-30

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