JPS5973169A - Control device for low pressure casting - Google Patents

Control device for low pressure casting

Info

Publication number
JPS5973169A
JPS5973169A JP18427882A JP18427882A JPS5973169A JP S5973169 A JPS5973169 A JP S5973169A JP 18427882 A JP18427882 A JP 18427882A JP 18427882 A JP18427882 A JP 18427882A JP S5973169 A JPS5973169 A JP S5973169A
Authority
JP
Japan
Prior art keywords
furnace
pressure
gas
molten metal
valve
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.)
Pending
Application number
JP18427882A
Other languages
Japanese (ja)
Inventor
Sotoshiro Tetori
手取 外志朗
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.)
Toshiba Corp
Original Assignee
Toshiba 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 Toshiba Corp filed Critical Toshiba Corp
Priority to JP18427882A priority Critical patent/JPS5973169A/en
Publication of JPS5973169A publication Critical patent/JPS5973169A/en
Pending legal-status Critical Current

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B22CASTING; POWDER METALLURGY
    • B22DCASTING OF METALS; CASTING OF OTHER SUBSTANCES BY THE SAME PROCESSES OR DEVICES
    • B22D18/00Pressure casting; Vacuum casting
    • B22D18/08Controlling, supervising, e.g. for safety reasons

Landscapes

  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)

Abstract

PURPOSE:To eliminate instantaneously the difference between the pressure in a hermetic furnace and a set pressure by providing a mechanism for discharging the gas pressing the surface of the molten metal in the furnace to the outside of the furnace in addition to a mechanism for adjusting the introducing flow rate of said gas and controlling both in accordance with the command from an arithmetic device. CONSTITUTION:A deviation between the set value of the pressure in a holding furnace 1 from an arithmetic device and the detected value of the pressure in the furnace from a pressure gauge 9 is determined with a comparator in a casting device which feeds carrier gas into the furnace to increase the pressure in the furnace and feeds a molten metal 3 into the cavity 5 in a casting mold 4. A motor 15 is driven according to the deviation and a flow rate regulating valve 14 is operated to eliminate the deviation value, whereby the pressure in the furnace adaptive to an elapsed time is accomplished. On the other hand, the controlled pressure in the furnace is inputted to the arithmetic device which feeds an operation command, when said pressure exceeds a set pressure, to a solenoid valve 17 to discharge the gas in the furnace through a stop valve 16 thereby controlling the pressure in the furnace in conjunction with the operation of the valve 14. The pressure in the furnace is thus extremely quickly regulated to the set pressure and the molten metal speed is precisely controlled.

Description

【発明の詳細な説明】 〔発明の技術分野〕 この発明はアルミニウム等の鋳造に用いる低圧鋳造装置
の制御装置に係り、特に溶融アルミニウム保持炉内の気
体圧を制御する装置に関する。
DETAILED DESCRIPTION OF THE INVENTION [Technical Field of the Invention] The present invention relates to a control device for a low-pressure casting apparatus used for casting aluminum and the like, and particularly to a device for controlling gas pressure in a molten aluminum holding furnace.

〔発明の技術的背景〕[Technical background of the invention]

低圧鋳造装置による鋳型キャビティへの溶融アルミニウ
ム(以下、「溶湯」という)の供給は第1図に示すよう
な装置を用いておこなわれる。
The supply of molten aluminum (hereinafter referred to as "molten metal") to a mold cavity by a low-pressure casting device is carried out using a device as shown in FIG.

保持炉l内には溶湯3が入っており、ふた2により密閉
封入されている。この保持炉l内に空気等の搬送気体を
送シこみ、炉内気体圧(以下、[炉内圧」という)を高
めることにより、溶湯3火ストーク6ケ介して鋳型4の
内部に形成されたキャビティ5に送り込み、これを充填
するように構成されている。搬送気体は減圧弁7によυ
適当な圧力に減圧されて弁8を介して保持炉l内に導入
爆れるようになっている。また保持炉1内の気体圧力は
圧力側9により測定される。このような構造により溶湯
3をキャビティ5に供給する場合には保持炉1内への気
体送入量は一定であシ、したがって炉内圧の増加も#1
ぼ一定となっている。
A holding furnace 1 contains a molten metal 3, which is hermetically sealed with a lid 2. By pumping a carrier gas such as air into this holding furnace 1 and increasing the gas pressure in the furnace (hereinafter referred to as ``furnace pressure''), the molten metal is formed inside the mold 4 through 3 molten metals and 6 torches. It is configured to feed into the cavity 5 and fill it. The carrier gas is transferred to pressure reducing valve 7.
The pressure is reduced to an appropriate level and then introduced into the holding furnace 1 via a valve 8. The gas pressure inside the holding furnace 1 is also measured by the pressure side 9. When the molten metal 3 is supplied to the cavity 5 with such a structure, the amount of gas fed into the holding furnace 1 is constant, and therefore the increase in the furnace pressure is also constant.
It remains almost constant.

しかし一般には鋳型の形状や大きさによって炉内圧増加
速度を変化させることが必要である。なぜならばキャビ
ティ5での溶湯上昇速度は炉内圧が一定増加する場合に
はキャビティ5の水平断面積によって異なるためである
。断面積が大きければ溶湯上列速度は小場くなシ、必要
速度以下になると溶湯の温度低下や表面酸化をもたらし
湯じわや酸化物の巻込み等の欠陥が発生する。逆に断面
積が小さくなり必要速度以上になった場合には溶湯流が
みだれ、1局合によって溶湯の噴射(スズラッシュ)が
おきる場合がある。これらの現象が発生すると酸化物゛
、ピンホール、ブローホールおよび正金など多くの欠陥
発生の原因となる。また炉内浴湯が多い状態では搬入気
体の容積が小芒くな9、気体送入開始時の圧力は急激に
上昇しゃすい。
However, it is generally necessary to change the rate of increase in furnace pressure depending on the shape and size of the mold. This is because the rising speed of the molten metal in the cavity 5 varies depending on the horizontal cross-sectional area of the cavity 5 when the furnace pressure increases to a certain degree. If the cross-sectional area is large, the top speed of the molten metal will be low; if the speed is lower than the required speed, the temperature of the molten metal will drop and surface oxidation will occur, causing defects such as wrinkles and oxide entrainment. On the other hand, if the cross-sectional area becomes smaller and the speed exceeds the required speed, the flow of the molten metal may stagnate, and a jet of molten metal (tin rush) may occur due to one phase. When these phenomena occur, many defects such as oxides, pinholes, blowholes, and specie are generated. In addition, when there is a large amount of hot water in the furnace, the volume of the gas to be brought in is small9, and the pressure at the start of gas feeding is likely to rise rapidly.

このため溶湯3がスプラッシュし、前述のような欠陥を
もたらす。いずれの場合にも鋳物の品質、信頼性および
経済性において問題がある。したがって低圧鋳造法ン用
いて鋳物を製造する場合には溶湯速度と炉内圧とヲ調整
することは優れた鋳物を得る上で重要な課題であるう特
に数十kg以上の大きな鋳物乞鋳造する場合にはその重
要性はいっそう増す。
As a result, the molten metal 3 splashes, causing the defects described above. In either case, there are problems with the quality, reliability, and economy of the casting. Therefore, when manufacturing castings using the low-pressure casting method, adjusting the molten metal speed and furnace pressure is an important issue in obtaining excellent castings, especially when casting large castings weighing several tens of kg or more. Its importance becomes even more important.

〔背景技術の問題点〕[Problems with background technology]

従来、簡単な鋳物形状の場合には作業者が炉内圧を調整
していた。
Conventionally, when casting a simple shape, an operator had to adjust the furnace pressure.

第1図に示すように減圧弁7から供給婆れる例えば約1
.41(g/crdの搬送気体を弁8を用いて圧力計9
を見ながら作業者自身が調整する。しかしこのような調
整法では作業が複雑になることやIAJ婚精度が悪いこ
となどから簡単な形状の鋳物以外には適用できないとい
う欠点があった。
As shown in FIG. 1, for example, about 1
.. 41 (g/crd) of the carrier gas is transferred to the pressure gauge 9 using the valve 8.
The operator makes the adjustments himself while looking at the However, this adjustment method has the disadvantage that it cannot be applied to castings other than simple shapes because the work is complicated and the IAJ accuracy is poor.

この問題を解決するための一方法として自動的に炉内圧
ケ制御する方法が用いられている。第2図はその一例を
示した調整機構の構成図である。
One way to solve this problem is to automatically control the pressure inside the furnace. FIG. 2 is a configuration diagram of an adjustment mechanism showing an example thereof.

減圧源10ケ駆動装置たとえばツ゛−づzモータ11を
用いて作動させる。作動量は比較器12からの出力によ
り決まり、その出力針は比較器12ヘフイードノマツク
嘔れた炉内圧と設定値記憶出力装置13から出力される
設定圧との差によって定まる。このよう女(幾構を用い
れは自動的に炉内圧をコントロールすることができ、鋳
物形状に適した溶湯速度を得ることが可能である。しか
しこのような方法でもやはり炉内圧と設定圧との間には
差が生ずる。
The 10 reduced pressure sources are actuated using a driving device, such as a ZZ motor 11. The operating amount is determined by the output from the comparator 12, and its output needle is determined by the difference between the furnace internal pressure output by the comparator 12 and the set pressure output from the set value storage output device 13. By using a number of mechanisms like this, it is possible to automatically control the furnace pressure and obtain a molten metal speed suitable for the casting shape. However, even with this method, the relationship between the furnace pressure and the set pressure is There is a difference between them.

第3図は第2図の機構を用いて炉内圧を制御し。In Fig. 3, the furnace internal pressure is controlled using the mechanism shown in Fig. 2.

た場合の設定圧と炉内圧の制御状態乞時間を横軸にとっ
て示した特性図である。設定圧を実線で、実際の炉内圧
を破線で示しである。設定圧と炉内圧の実測値との差は
搬送気体の送入開始時や、気体送入量を急激にム1シ少
嘔せた時におこる。このような時には、炉内圧は設定値
よりも大きくなり、気体送入が停止ちれた状態で設定圧
が上昇するのを待つ。設定圧が炉内圧に達すると、気体
送入を再び開始するが、今まで閉状態であった弁が突然
間となるため、急激な気体流入がおこシ、再び炉内圧が
設定圧よりも犬となる。炉内圧と設定圧との差は除々に
減少するが、以上説明したような現象Y数回繰シ返すこ
とになる。この現象は操作される弁の応答速度や弁部品
の寸法公差、弁の閉じた状態から開いた状態への移行等
によって左右される。このような状態で溶湯3をキャビ
ティ5に充填した場合には、溶湯3は階段状にキャビテ
ィ5内を上昇する。したがって前述したように酸化物や
湯じわなどの欠陥発生の原因となるためH物の品質を損
ねていた。
It is a characteristic diagram showing the set pressure and the control state time of the furnace internal pressure on the horizontal axis. The set pressure is shown by a solid line, and the actual pressure inside the furnace is shown by a broken line. A difference between the set pressure and the measured value of the furnace internal pressure occurs at the start of feeding the carrier gas or when the amount of gas fed suddenly decreases. In such a case, the furnace internal pressure becomes higher than the set value, and the furnace waits for the set pressure to rise with the gas supply stopped. When the set pressure reaches the furnace pressure, gas supply starts again, but the valve that had been closed suddenly closes, causing a sudden inflow of gas, causing the furnace pressure to drop below the set pressure again. becomes. Although the difference between the furnace internal pressure and the set pressure gradually decreases, the phenomenon described above will be repeated several times. This phenomenon is influenced by the response speed of the operated valve, the dimensional tolerances of the valve parts, the transition from the closed state to the open state of the valve, etc. When the cavity 5 is filled with the molten metal 3 in such a state, the molten metal 3 rises in the cavity 5 in a stepwise manner. Therefore, as described above, this causes defects such as oxides and hot water wrinkles, which impairs the quality of the H product.

〔発明の目的〕 この発明の目的は、炉内圧と設定圧との差が瞬時に解消
される低圧鋳造炉の制御装置を提供するにある。
[Object of the Invention] An object of the present invention is to provide a control device for a low-pressure casting furnace that instantly eliminates the difference between the furnace internal pressure and the set pressure.

〔発明の概要〕[Summary of the invention]

この発明では上記目的ヶ達成するために、密閉保持炉内
の溶湯面を搬入気体によシ押圧することにより前記浴湯
を鋳型内キャビティに充填する機構をそなえた低圧鋳造
装置において、前記保持炉内に湯面押圧用の気体を導入
する炉内気体送入装置と、前記保持炉内の気体圧力の検
出手段と、あらかじめ設定された前記保持炉内の気体圧
力値と前記検出手段の出力値との偏差に基づいて、その
偏差を)q11!消するよう前記炉内気体送入装置から
の専入気体bit絹欠制御1−る流Nil %Q節弁と
、前記検出手段の出力値が前記設定逼れた気体圧力値7
超えた時前記保持炉内の気体を炉外に排出し前記検出手
段の出力値と前記設定烙れた気体圧力値とが等しくなっ
た1侍に排出を停止するように前記保持炉に数句ジノら
7+、た排出装置と、前記保持炉内の気体圧力値を設定
し、かつ前記排出装置に対する動作指令信号を送出する
演算装置とを具備したこと乞特徴とする。
In order to achieve the above object, the present invention provides a low-pressure casting apparatus equipped with a mechanism for filling a cavity in a mold with bath water by pressing the surface of the molten metal in the closed holding furnace with gas. an in-furnace gas supply device that introduces gas for pressing the molten metal surface into the furnace; a gas pressure detection means in the holding furnace; and a preset gas pressure value in the holding furnace and an output value of the detection means. Based on the deviation from )q11! Dedicated gas bit shortage control 1 - flow Nil %Q control valve from the in-furnace gas supply device to extinguish the gas pressure value 7 at which the output value of the detection means is within the set value.
When the temperature exceeds the temperature, a few words are placed in the holding furnace so that the gas in the holding furnace is discharged to the outside of the furnace and the discharge is stopped when the output value of the detection means and the set gas pressure value become equal. Gino et al. 7+ is characterized in that it includes a discharge device, and an arithmetic device that sets a gas pressure value in the holding furnace and sends an operation command signal to the discharge device.

〔発明の実施例〕[Embodiments of the invention]

以下この発明ケ実施例に基づいて詳細に説明する。 The present invention will be described in detail below based on embodiments.

第4図はこの発明の一実施例を示した概略構成図である
。なお以下の図面においては第1図に示したと同一部分
には同一符号ケ伺してその説明を省略する。
FIG. 4 is a schematic diagram showing an embodiment of the present invention. In the following drawings, the same parts as shown in FIG. 1 are designated by the same reference numerals, and their explanations will be omitted.

保持炉1内に導入される搬送気体の流量はサーボモータ
15によって駆動される可変形流量調整弁14によりお
こなわれる。嘔らに保持炉lには炉内の気体を排出する
ための開閉弁16が取付けられている。開閉弁16は後
述する演算装置からの動作指令信号によって動作する電
磁弁17により弁の開閉をおこなうように構成されてい
る。
The flow rate of the carrier gas introduced into the holding furnace 1 is controlled by a variable flow rate regulating valve 14 driven by a servo motor 15. Additionally, the holding furnace l is equipped with an on-off valve 16 for discharging gas within the furnace. The on-off valve 16 is configured to be opened and closed by an electromagnetic valve 17 operated by an operation command signal from an arithmetic unit, which will be described later.

第5図は制御装置の構成を示したブロック図である。炉
内圧乞設定したシ開閉弁16に対する動作指令信号を送
出するための演算装置としてマイクロコンピュータ18
が使用される。マイクロコンピュータ18はキャビティ
5や保持炉1の状態および溶@3の温度等により定゛ま
る最適の炉内圧を設定値として格納しており、これt時
々刻々出力する。
FIG. 5 is a block diagram showing the configuration of the control device. A microcomputer 18 is used as an arithmetic device to send an operation command signal to the on-off valve 16 that has set the furnace pressure.
is used. The microcomputer 18 stores the optimal furnace internal pressure, which is determined by the conditions of the cavity 5 and the holding furnace 1, the temperature of the melt 3, etc., as a set value, and outputs this value every moment.

このマイクロコンピュータ18の出力は一般にディジタ
ル信号として出力されるので、これビD/A変換器19
によりアナログ信号に変換して比較器2Jに入力する。
Since the output of this microcomputer 18 is generally output as a digital signal, it is
The signal is converted into an analog signal and input to the comparator 2J.

一方、保持炉1内の気体による炉内圧は圧力計9により
検出逼れ、圧力変換器2tJを介してアナログ的な市1
気量に変換されて比較器2Jに入力逼れる。
On the other hand, the pressure inside the holding furnace 1 due to the gas is detected by the pressure gauge 9, and the pressure inside the holding furnace 1 is detected by the pressure transducer 2tJ.
It is converted into air volume and input to the comparator 2J.

比較器2】はD/A変換器19と圧力変換器側との入力
域の差夕羽出してその偏差it火丈−日?モータ15を
介して可変形流量調整弁14に出力するととによりその
偏差M:ヲなくすように可変形流量調整弁14の弁を調
節する。保持炉l内の炉内圧はA/D 変換器22によ
ってディジタル信号に変換されてマイクロごンビュータ
18にフィードバックされる。一方マイクロコンピュー
タ18からは開閉弁16ン駆動する%i1磁弁磁子17
作指令信号が接点出力器23ヲ介して出力される。
Comparator 2] shows the difference in the input range between the D/A converter 19 and the pressure transducer side, and calculates the deviation it fire height - days? By outputting the signal to the variable flow rate regulating valve 14 via the motor 15, the valve of the variable flow rate regulating valve 14 is adjusted so as to eliminate the deviation M:. The internal pressure in the holding furnace 1 is converted into a digital signal by the A/D converter 22 and fed back to the microcomputer 18. On the other hand, from the microcomputer 18, the %i1 magnetic valve magnet 17 which drives the on-off valve 16
An operation command signal is outputted via the contact output device 23.

このように構成烙れた制御装置の動作について次に説明
する。
The operation of the thus configured control device will now be described.

人力圧6kg/iの乾燥気体(たとえば乾燥空気)は減
圧弁7によl> 1.4kgA−rIに減圧されて可変
形流量1iIAl整弁14に達している。ここでマイク
ロコンピュータ18から、経過時間に適応した設定圧が
D/A変換器19y!l−介して比較器21に出力され
る。比較器21は圧力言19からの電気量との偏差火水
め、この偏差をサーボモータ15に出力することによシ
可変形流量調整弁14が作動する。炉内圧はA/D 変
換器22ヲ介してマイクロコンピユー月8にフィートノ
々ツクされるように構成されているので、前述した偏差
が解消することで経過時間に適応した炉内圧の調整がお
こなわれることになる。
Dry gas (for example, dry air) with a manual pressure of 6 kg/i is reduced in pressure by the pressure reducing valve 7 to 1>1.4 kgA-rI and reaches the variable flow rate 1iIA1 regulating valve 14. Here, the microcomputer 18 transmits the set pressure adapted to the elapsed time to the D/A converter 19y! It is output to the comparator 21 via l-. The comparator 21 measures the deviation from the electrical quantity from the pressure gauge 19, and by outputting this deviation to the servo motor 15, the variable flow rate regulating valve 14 is operated. Since the furnace internal pressure is configured to be foot-checked to the microcomputer 8 via the A/D converter 22, the above-mentioned deviation is eliminated and the furnace internal pressure is adjusted in accordance with the elapsed time. It will be.

しかし可変形流量調整弁14の遅!1等のため、炉内圧
が設定圧を超えるような場合には本装置は次のように作
動する。炉内圧はA/D 変換器22暑介してマイクロ
コンピュータ18に入力略れ、常に設定圧との比較がな
されているため、炉内圧が設定圧以上の値となった場合
には接点出力器23’aj介して電磁弁17へ動作指令
信号が送出烙れ、開閉弁16が開いて炉内気体が排出さ
れる。したがって瞬時に炉内圧は減少して設定圧に近づ
く。このような開閉弁16の動作がおこ−なわれている
場合も、炉内圧は可変形流量調整弁14によって制御さ
れている、そして炉内圧が設定圧に達した時点で開閉弁
16目、閉じ、炉内気体の排出は停止する。
However, the variable flow rate regulating valve 14 is slow! 1, so if the pressure inside the furnace exceeds the set pressure, this device operates as follows. The furnace internal pressure is input to the microcomputer 18 via the A/D converter 22 and is constantly compared with the set pressure, so if the furnace internal pressure exceeds the set pressure, the contact output device 23 An operation command signal is sent to the solenoid valve 17 through the solenoid valve 17, and the on-off valve 16 is opened and the gas in the furnace is discharged. Therefore, the furnace pressure instantly decreases and approaches the set pressure. Even when the on-off valve 16 is operated in this way, the furnace internal pressure is controlled by the variable flow rate adjustment valve 14, and when the furnace internal pressure reaches the set pressure, the on-off valve 16 closes. , the exhaust of gas inside the furnace will stop.

従来の制御装置ではこのような排出装置を有しないため
炉内圧と設定圧との調整は可変形流縫調整弁14ン用い
ておこなう11かはなかったつしたがって両者が一致す
るのに長時間を有する場合があった。しか[7この発明
では排出装置を設けたので炉内圧と設定圧との間に差ケ
生じてもこの差は瞬時に解消されるように動作する。
Conventional control devices do not have such a discharge device, so adjustment of the furnace internal pressure and set pressure is done using a variable flow adjustment valve (14).Therefore, it takes a long time for the two to match. There was a case. However, since the present invention is provided with a discharge device, even if a difference occurs between the furnace internal pressure and the set pressure, it operates so that this difference is instantly eliminated.

〔発明の効果〕〔Effect of the invention〕

以上実施例に基づいて詳細に説明したように、この発明
では搬入気体の流kWM整機構に加えて炉内に導入され
た気体を炉外に排出するための排出装置ビ設けて両者を
演n、装置からの指令に基づいて制御するように構成し
たので、炉内圧が設定圧にきわめて急速に調整できると
いう利点がある。
As described above in detail based on the embodiments, in this invention, in addition to the KWM regulating mechanism for the flow of the gas introduced into the furnace, a discharge device for discharging the gas introduced into the furnace outside the furnace is provided, so that both can be controlled. Since the furnace is configured to be controlled based on commands from the device, there is an advantage that the pressure inside the furnace can be adjusted to the set pressure extremely quickly.

し7たかってこの装麿ヲ用いると欠陥のきわめて少ない
品質の優れた妃1造製品を安定して供給することができ
るという優れた効果がある。
However, the use of this method has the excellent effect of stably supplying high-quality products with very few defects.

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

第1図は従来の装置の構成ビ示した図、第2図は従来の
炉内11三制御機横の一例ケ示した図、第3図は第2図
に示し7た装置による炉内圧の制御状態を示す特性図、
第4図および第5図はこの発明の一実施例〉示したもσ
)で、第4図はその概略構成図、第5図はブロック図で
ある。 l・・・保持炉、3・・・溶湯、4・・・鋳型、5・・
・キャビティ、9・・・圧力計、12・・・比較器、1
4・・・可変形流域調整弁、16・・・開閉弁、17・
・・電磁弁、18・・・マイクロコンピュータ、n・・
・接点出力器。 出願人代理人  猪  股     清第3因 第4図
Fig. 1 is a diagram showing the configuration of a conventional device, Fig. 2 is an example of a conventional in-furnace controller 11, and Fig. 3 is a diagram showing an example of the side of the conventional furnace internal pressure controller. Characteristic diagram showing control status,
FIGS. 4 and 5 show an embodiment of the present invention.
), FIG. 4 is a schematic configuration diagram thereof, and FIG. 5 is a block diagram thereof. l... Holding furnace, 3... Molten metal, 4... Mold, 5...
・Cavity, 9...Pressure gauge, 12...Comparator, 1
4... Variable flow area regulating valve, 16... Opening/closing valve, 17.
...Solenoid valve, 18...Microcomputer, n...
・Contact output device. Applicant's agent Kiyoshi Inomata Cause 3 Figure 4

Claims (1)

【特許請求の範囲】[Claims] 密閉保持炉内の溶湯面を搬入気体により押圧することに
よシ前記溶湯を鋳型内キャビティに充填する機0!/を
そなえた低圧鋳造装置において、前記保持炉内に湯面押
圧用の気体を導入する炉内気体送入装置と、前記保持炉
内の気体圧力の検出手段と、あらかじめ設定烙れた前記
保持炉内の気体圧力値と前記検出手段の出力値との偏差
に基づいて、その偏差な解消するようnIJ記炉内炉内
気体送入装置の導入気体流域を制御する流量調節弁と、
前記検出手段の出力値が前記設定された気体圧力値を超
えた時前記保持炉内の気体ケ炉外に排出し前記検出手段
の出力値とg+I記設定された気体圧力(11’4とが
等しくなった時に排出を停止するように前記保持炉に取
+Jけられた排出装置と、前記保持炉内の気体圧力値乞
設定し、かつ前記排出装置に対する動作指令信号を送出
する演算装置とt具備したことケ特徴とする低圧鋳造制
御装置。
A machine for filling the cavity in the mold with the molten metal by pressing the surface of the molten metal in the closed holding furnace with the introduced gas! / A low-pressure casting apparatus equipped with: an in-furnace gas supply device for introducing gas for pressing the molten metal level into the holding furnace; a means for detecting the gas pressure in the holding furnace; a flow rate regulating valve that controls an inlet gas flow area of an in-furnace gas supply device in an nIJ recording furnace to eliminate the deviation based on a deviation between a gas pressure value in the furnace and an output value of the detection means;
When the output value of the detection means exceeds the set gas pressure value, the gas in the holding furnace is discharged to the outside of the furnace, and the output value of the detection means and the set gas pressure (g+I) are a discharge device attached to the holding furnace so as to stop discharge when the pressure becomes equal; a calculation device that sets the gas pressure value in the holding furnace and sends an operation command signal to the discharge device; A low-pressure casting control device with the following features.
JP18427882A 1982-10-20 1982-10-20 Control device for low pressure casting Pending JPS5973169A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP18427882A JPS5973169A (en) 1982-10-20 1982-10-20 Control device for low pressure casting

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP18427882A JPS5973169A (en) 1982-10-20 1982-10-20 Control device for low pressure casting

Publications (1)

Publication Number Publication Date
JPS5973169A true JPS5973169A (en) 1984-04-25

Family

ID=16150512

Family Applications (1)

Application Number Title Priority Date Filing Date
JP18427882A Pending JPS5973169A (en) 1982-10-20 1982-10-20 Control device for low pressure casting

Country Status (1)

Country Link
JP (1) JPS5973169A (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS61253158A (en) * 1985-05-04 1986-11-11 Sintokogio Ltd Low-pressure casting device
US4741381A (en) * 1986-01-22 1988-05-03 Sintokogio Ltd. Method of and apparatus for automatically controlling pressure in holding furnace incorporated in low pressure die-casting system
JPS63273561A (en) * 1987-05-02 1988-11-10 Isuzu Seisakusho:Kk Method and apparatus for controlling pressure
US5913358A (en) * 1993-11-11 1999-06-22 Hi-Tec Metals Ltd. Casting apparatus and method

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS61253158A (en) * 1985-05-04 1986-11-11 Sintokogio Ltd Low-pressure casting device
JPH0416260B2 (en) * 1985-05-04 1992-03-23 Sintokogio Ltd
US4741381A (en) * 1986-01-22 1988-05-03 Sintokogio Ltd. Method of and apparatus for automatically controlling pressure in holding furnace incorporated in low pressure die-casting system
JPS63273561A (en) * 1987-05-02 1988-11-10 Isuzu Seisakusho:Kk Method and apparatus for controlling pressure
JP2528313B2 (en) * 1987-05-02 1996-08-28 株式会社 五十鈴製作所 Pressure control device
US5913358A (en) * 1993-11-11 1999-06-22 Hi-Tec Metals Ltd. Casting apparatus and method

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