JPH0445262B2 - - Google Patents
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- Publication number
- JPH0445262B2 JPH0445262B2 JP59281746A JP28174684A JPH0445262B2 JP H0445262 B2 JPH0445262 B2 JP H0445262B2 JP 59281746 A JP59281746 A JP 59281746A JP 28174684 A JP28174684 A JP 28174684A JP H0445262 B2 JPH0445262 B2 JP H0445262B2
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- Prior art keywords
- pressure
- hot water
- water storage
- storage chamber
- molten metal
- Prior art date
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- Expired - Lifetime
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Description
【発明の詳細な説明】
産業上の利用分野
この発明は溶湯等を気体圧により注湯する加圧
式注湯炉に関する。DETAILED DESCRIPTION OF THE INVENTION Field of Industrial Application This invention relates to a pressurized pouring furnace for pouring molten metal or the like using gas pressure.
従来技術
加圧式注湯炉は、たとえば第2図に示すよう
に、圧力調整装置3から給気弁4を経て注湯炉1
の貯湯室2に、例えば、空気あるいは不活性ガス
等の気体を所定の圧力(以下にベース圧Pとい
う)で押込み、貯湯室2内の溶湯の湯面レベルを
押し下げて注湯室5の湯面レベルを所定の注湯待
機レベル(以下にプリレベルという)まで上昇さ
せる。Prior Art A pressurized pouring furnace, for example, as shown in FIG.
For example, a gas such as air or an inert gas is forced into the hot water storage chamber 2 at a predetermined pressure (hereinafter referred to as base pressure P), and the level of the molten metal in the hot water storage chamber 2 is lowered to lower the hot water level in the pouring chamber 5. The surface level is raised to a predetermined pouring standby level (hereinafter referred to as pre-level).
鋳型7に注湯するときには、第3図に示すよう
に、圧力調整装置3から上記貯湯室2に、上記ベ
ース圧Pに追加気圧(以下にシヨツト圧ΔPとい
う)を加圧して、貯湯室2内の湯面レベルを押下
げるとともに注湯室5における溶湯の湯面レベル
を所定の注湯レベルまで押上げ、注湯口8から鋳
型7に定量の注湯を行なう。 When pouring hot water into the mold 7, as shown in FIG. 3, an additional pressure (hereinafter referred to as shot pressure ΔP) is applied to the base pressure P from the pressure regulator 3 to the hot water storage chamber 2. At the same time, the level of the molten metal in the pouring chamber 5 is raised to a predetermined pouring level, and a fixed amount of molten metal is poured into the mold 7 from the pouring port 8.
上述した動作を、第3図に示すように繰り返す
ことにより、多数の鋳型7に自動的に注湯を行な
うようになつている。 By repeating the above-described operations as shown in FIG. 3, a large number of molds 7 are automatically poured.
しかしながら、上述した従来の加圧式注湯炉に
おいては、貯湯室2に供給する空気圧は、注湯炉
1の重量をロードセル等で測定することによつ
て、貯湯室2内の溶湯重量を表わす信号を得て、
この溶湯重量の信号だけによつて、所要の空気圧
となるように制御していた。 However, in the above-mentioned conventional pressurized pouring furnace, the air pressure supplied to the hot water storage chamber 2 is determined by measuring the weight of the hot water pouring furnace 1 with a load cell or the like, and then generating a signal representing the weight of the molten metal in the hot water storage chamber 2. obtained,
The required air pressure was controlled solely by the signal of the weight of the molten metal.
しかしながら、この従来方式では加圧制御に遅
れを生じる一方、ノイズ等による誤動作によつて
正確な圧力制御が困難であるという問題があつ
た。 However, this conventional method has problems in that there is a delay in pressurization control and that accurate pressure control is difficult due to malfunctions caused by noise and the like.
発明の目的
この発明は上述の問題を解決し、応答性が早く
かつ正確に所要気体圧を制御できる加圧式注湯炉
を提供することを目的とするものである。OBJECTS OF THE INVENTION It is an object of the present invention to solve the above-mentioned problems and provide a pressurized pouring furnace that can quickly respond and accurately control the required gas pressure.
発明の構成
この発明の加圧式注湯炉は、溶湯を貯留する貯
湯室と、上記貯湯室と連通する注湯室と、上記貯
湯室に加圧系統を介して加圧気体を供給する加圧
気体供給手段とを備え、上記加圧気体供給手段か
ら上記貯湯室に溶湯の貯湯量に見合つたベース圧
を印加した後、シヨツト圧を加圧することにより
上記注湯室の注湯口から所定量の溶湯を注出する
加圧式注湯炉において、
上記貯湯室内の圧力を検出する圧力検出手段
と、
上記加圧気体供給手段から上記貯湯室へ加圧気
体を供給する加圧系統に備わる弁開度調整可能な
加圧調整弁と、
上記貯湯室内の気体を貯湯室の外部へ放出する
減圧系統に備わる弁開度調整可能な減圧調整弁
と、
上記貯湯室内の貯湯重量を検出する貯湯重量検
出手段と、
上記貯湯重量検出手段によつて検出された貯湯
重量に応じて上記ベース圧及び上記シヨツト圧を
演算し上記貯湯室内の圧力設定値としての制御信
号を送出する制御装置と、
上記制御信号の示す上記圧力設定値と上記圧力
検出手段から供給される上記貯湯室の圧力検出値
との偏差がゼロの状態のときには、上記貯湯室内
への加圧と減圧とが平衡するように、上記加圧調
整弁及び上記減圧調整弁に対して相関した弁開度
となるようなコントロール信号を発生し、上記偏
差が平衡状態から貯湯室内の圧力が上昇する方向
へ変化したときには、上記加圧調整弁の弁開度が
減少し上記減圧調整弁の弁開度が増加するように
コントロール信号を発生し、上記偏差が平衡状態
から貯湯室内の圧力が下降する方向へ変化したと
きには、上記加圧調整弁の弁開度が増加し上記減
圧調整弁の弁開度が減少するようにコントロール
信号を発生する圧力調整手段とを備えている。Composition of the Invention The pressurized pouring furnace of the present invention includes a hot water storage chamber for storing molten metal, a pouring chamber communicating with the hot water storage chamber, and a pressurized metal pouring furnace for supplying pressurized gas to the hot water storage chamber via a pressurization system. After applying a base pressure commensurate with the amount of stored molten metal from the pressurized gas supply means to the storage chamber, a predetermined amount of molten metal is poured from the pouring port of the pouring chamber by increasing shot pressure. In a pressurized pouring furnace that pours out molten metal, a pressure detection means for detecting the pressure in the hot water storage chamber, and a valve opening degree provided in a pressurization system that supplies pressurized gas from the pressurized gas supply means to the hot water storage chamber. an adjustable pressure regulating valve; a pressure reducing regulating valve having an adjustable valve opening in a pressure reducing system that discharges the gas in the hot water storage chamber to the outside of the hot water storage chamber; and a hot water storage weight detection means for detecting the weight of hot water stored in the hot water storage chamber. and a control device that calculates the base pressure and the shot pressure according to the stored hot water weight detected by the hot water storage weight detection means and sends out a control signal as a pressure setting value in the hot water storage chamber; When the deviation between the pressure set value shown and the pressure detection value of the hot water storage chamber supplied from the pressure detection means is zero, the pressurization is performed so that pressurization and depressurization in the hot water storage chamber are in balance. A control signal is generated for the regulating valve and the pressure reducing regulating valve so that the valve opening degrees are correlated to each other, and when the deviation changes from an equilibrium state to a direction in which the pressure in the hot water storage chamber increases, the pressure regulating valve is controlled. A control signal is generated so that the valve opening degree decreases and the valve opening degree of the pressure reduction regulating valve increases, and when the deviation changes from the equilibrium state to a direction in which the pressure in the hot water storage chamber decreases, the pressure reduction regulating valve increases. and pressure regulating means for generating a control signal such that the valve opening increases and the valve opening of the pressure reduction regulating valve decreases.
上記の構成において、設定圧と検出圧の偏差零
の時は、加圧および減圧調節弁ともたとえば約20
%の開度となり、流入気体量と排出気体量がバラ
ンスして炉内圧は一定となるように制御される。
今、制御信号が上昇して(−)偏差が発生した場
合、コントロール信号は0.6〜1.0Kg/cm2に増加す
る。これによつて、加圧調節弁は20〜100%開度
となつて炉内への流入気体量を増大し、加圧す
る。また、同時に減圧調節弁は20〜0%開度とな
つて炉内からの排出気体量を減少(停止)させ
る。(+)偏差の場合は、逆の動作を同様に行な
う。この制御により気体送給応答速度を早くし、
またノイズによつてロードセルの信号にエラーが
生じても正確な制御を行なうことができる。 In the above configuration, when the deviation between the set pressure and the detected pressure is zero, both the pressurization and pressure reduction control valves are approximately 20
% opening, and the inflow gas amount and exhaust gas amount are balanced and the furnace pressure is controlled to be constant.
Now, if the control signal increases and a (-) deviation occurs, the control signal will increase to 0.6-1.0Kg/ cm2 . As a result, the pressure control valve opens 20 to 100%, increasing the amount of gas flowing into the furnace and pressurizing it. At the same time, the pressure reducing control valve becomes 20% to 0% open to reduce (stop) the amount of gas discharged from the furnace. In the case of a (+) deviation, perform the opposite operation in the same manner. This control speeds up the gas supply response speed,
Further, even if an error occurs in the signal of the load cell due to noise, accurate control can be performed.
実施例
第1図において、注湯炉1の貯湯室2の室内圧
を検出するように圧力検出器10が設けられ、圧
力検出器10で検出された炉内圧力を示す空気圧
を用いた信号は注湯炉の設置現場に設けた空気式
の圧力調節計11に印加される。Embodiment In FIG. 1, a pressure detector 10 is provided to detect the indoor pressure of a hot water storage chamber 2 of a pouring furnace 1, and a signal using air pressure indicating the pressure inside the furnace detected by the pressure detector 10 is as follows. The pressure is applied to a pneumatic pressure regulator 11 installed at the pouring furnace installation site.
一方、注湯炉1の重量はロードセル12で検出
され、その信号は制御装置20に印加され、この
制御装置20内でA/D変換器21によりデイジ
タル信号に変換されて、CPU22に印加される。
CPU22は、この重量信号から、貯湯室2内の
残留貯湯重量を演算して、残留貯湯量に対応する
プリレベルPならびにシヨツト圧ΔPを演算する。
非注湯時にはこのプリレベルPがD/A変換器2
3によりアナログ信号に変換され、さらに電空変
換器12にて空気圧信号に変換されて、この空気
圧信号が設定圧信号として圧力調節計11に印加
される。 On the other hand, the weight of the pouring furnace 1 is detected by the load cell 12, and the signal is applied to the control device 20. Within this control device 20, it is converted into a digital signal by the A/D converter 21, and the signal is applied to the CPU 22. .
The CPU 22 calculates the weight of the remaining hot water stored in the hot water storage chamber 2 from this weight signal, and calculates the pre-level P and shot pressure ΔP corresponding to the remaining hot water storage amount.
During non-pouring, this pre-level P is the D/A converter 2.
3 into an analog signal, and further converted into an air pressure signal by an electro-pneumatic converter 12, and this air pressure signal is applied to the pressure regulator 11 as a set pressure signal.
圧力調節計11は圧力検出器10からの検出圧
力信号と電空変換器12からの設定圧信号との差
にもとずいて、加圧調節弁13と減圧調節弁14
の開度に対応する圧力を有するコントロール信号
を出力する。 The pressure regulator 11 operates a pressure control valve 13 and a pressure reduction control valve 14 based on the difference between the detected pressure signal from the pressure detector 10 and the set pressure signal from the electro-pneumatic converter 12.
outputs a control signal having a pressure corresponding to the degree of opening.
加圧調節弁13は貯湯室2へ加圧用の気体を送
る加圧系統中の調節弁16の開度を制御するもの
であり、コントロール信号0.2〜1.0Kg/cm2をポジ
シヨナーにてスプリツトレンジとし、0.5〜1.0
Kg/cm2/0〜100%弁開度の作動とする。 The pressure regulating valve 13 controls the opening degree of the regulating valve 16 in the pressurizing system that sends pressurizing gas to the hot water storage chamber 2, and a control signal of 0.2 to 1.0 kg/cm 2 is sent to the split range using a positioner. and 0.5 to 1.0
Kg/cm 2 /0 to 100% valve opening operation.
減圧調節弁14は貯湯室2と大気間の減圧系統
中の調節弁17の開度を制御するものであり、コ
ントロール信号をポジシヨナーにてスプリツトレ
ンジとし、0.2〜0.7Kg/cm2/100〜0%弁開度の
作動とする。 The pressure reduction control valve 14 controls the opening degree of the control valve 17 in the pressure reduction system between the hot water storage chamber 2 and the atmosphere, and the control signal is split in the range from 0.2 to 0.7Kg/cm 2 /100 using a positioner. Operate with 0% valve opening.
調節計11の制御方式は、第4図に示すように
検出圧力と設定圧信号の偏差がゼロのときは加圧
調節弁13、減圧調節弁14とも約20%の開度と
なり、貯湯室2への流入気体量と貯湯室2からの
排出空気量がバランスして注湯炉の炉内圧力が一
定となるように制御される。いま設定圧信号が増
加して(−)偏差が発生した場合にはコントロー
ル信号は0.6から1.0Kg/cm2に増加して加圧調節弁
13は20%開度から100%開度に変化して、貯湯
室2への流入気体量を増加して、加圧力を増す。
また同時に減圧調節弁14は20%開度から0%開
度となつて、炉内からの排出気体量を減少または
停止させる。 As shown in Fig. 4, the control method of the controller 11 is such that when the deviation between the detected pressure and the set pressure signal is zero, both the pressure control valve 13 and the pressure reduction control valve 14 are opened approximately 20%, and the hot water storage chamber 2 The amount of gas flowing into the hot water storage chamber 2 and the amount of air discharged from the hot water storage chamber 2 are balanced, and the pressure inside the pouring furnace is controlled to be constant. If the set pressure signal increases and a (-) deviation occurs, the control signal will increase from 0.6 to 1.0 Kg/cm 2 and the pressure control valve 13 will change from 20% opening to 100% opening. Then, the amount of gas flowing into the hot water storage chamber 2 is increased to increase the pressurizing force.
At the same time, the pressure reducing control valve 14 changes from 20% opening to 0% opening to reduce or stop the amount of gas discharged from the furnace.
(+)偏差の場合は上述と逆の動作を行なう。 In the case of a (+) deviation, the operation opposite to the above is performed.
上述の構成において、各調節弁13,14は炉
内容積に基づく気体流入量に対する炉内圧の上昇
率を求め、これによつて適切なCv値(流量特性
値)の調節弁を選定する。状況に応じて供給気体
圧を1〜6Kg/cm2の範囲で調整し設定する。そし
て、調節計のP(比例帯)I(積分帯)D(微分帯)
機能の各設定値を適切に調整することにより、応
答性、追従性を向上させることができる。 In the above-described configuration, each of the control valves 13 and 14 determines the rate of increase in pressure within the furnace relative to the amount of gas inflow based on the internal volume of the furnace, and based on this, a control valve with an appropriate Cv value (flow characteristic value) is selected. Adjust and set the supply gas pressure within the range of 1 to 6 kg/cm 2 depending on the situation. And P (proportional band) I (integral band) D (differential band) of the controller
By appropriately adjusting each setting value of the function, responsiveness and followability can be improved.
また上記の構成において、シヨツト圧印加時に
は、第5図に示すように昇圧曲線の応答性と追従
性が向上する。 Further, in the above configuration, when shot pressure is applied, the responsiveness and followability of the pressure increase curve are improved as shown in FIG.
炉内圧∝流入空気量 ……
また、流入気体量=定数×供給気体圧×
時間×配管断面積 ……
であるから、今、時間と配管断面積を同じとする
と、、式から炉内圧の昇圧効果は、供給気体
圧に正比例する。 Furnace pressure ∝ inflow air amount ... Also, inflow gas amount = constant x supply gas pressure x time x piping cross-sectional area ... Therefore, if time and piping cross-sectional area are the same, the furnace pressure will increase from the formula. The effect is directly proportional to the supply gas pressure.
つまり、制御の範囲内で供給気体圧が高いほ
ど、昇圧効果は高くなり、応答性、追従性が良く
なるといえる。 In other words, it can be said that the higher the supplied gas pressure within the control range, the higher the pressure increase effect, and the better the responsiveness and followability.
従来方式は、応答性、改善のためには、配管断
面積を上げる方法しか選べなかつたが、この発明
においては溶湯重量による加圧力制御のほかに、
貯湯室2内の圧力検出によつて加圧調節弁と減圧
調節弁とを制御するようにしたので、供給気体圧
と配管断面積の両要素によつて制御できることに
なり、速応性を容易に向上できる。 In the conventional method, in order to improve responsiveness, the only option was to increase the cross-sectional area of the piping, but in this invention, in addition to controlling the pressure by the weight of the molten metal,
Since the pressure control valve and the pressure reduction control valve are controlled by detecting the pressure in the hot water storage chamber 2, it is possible to control the supply gas pressure and the cross-sectional area of the piping, which facilitates quick response. You can improve.
なおこの実施例においては、調節弁16と貯湯
室2との間に緊急しや断弁18が設けられてお
り、非常時には、制御装置30からの信号により
緊急しや断弁18を閉じて貯湯室2への気体供給
をしや断する。 In this embodiment, an emergency shutoff valve 18 is provided between the control valve 16 and the hot water storage chamber 2, and in an emergency, the emergency shutoff valve 18 is closed by a signal from the control device 30 to stop hot water storage. The gas supply to chamber 2 is cut off.
一方、調節弁17と並列に非常用排出弁19が
設けられており、非常時には、制御装置30から
の信号により、この非常用排出弁19を閉じて、
貯湯室2内の気体を排出する。 On the other hand, an emergency discharge valve 19 is provided in parallel with the control valve 17, and in an emergency, this emergency discharge valve 19 is closed by a signal from the control device 30.
The gas in the hot water storage chamber 2 is discharged.
なお、制御装置30からの非常用の信号は
CPU22にも印加されている。 In addition, the emergency signal from the control device 30 is
It is also applied to the CPU 22.
制御装置30からの非常停止信号がCPU22
に入ることにより、制御出力を零とする。制御信
号が零になると、圧力調節計11の外部設定値が
零となり、加圧調整弁13を全閉、減圧調整弁1
4を全開とするコントロール信号0.2Kg/cm2を出
力する。 The emergency stop signal from the control device 30 is sent to the CPU 22.
By entering, the control output is made zero. When the control signal becomes zero, the external setting value of the pressure regulator 11 becomes zero, the pressurization regulating valve 13 is fully closed, and the pressure reducing regulating valve 1 is closed completely.
Outputs a control signal of 0.2Kg/cm 2 with 4 fully open.
加圧調節弁13および減圧調節弁14のポジシ
ヨナー出力信号を信号しや断電磁弁でカツトし、
強制的に加圧調節弁13を全閉、減圧調節弁14
を全開する。加圧気体配管ラインに設けた緊急し
や断弁18を制御盤からの非常停止信号により全
閉し、流入気体回路をしや断する。排気ライン上
の大口径の非常用排出電磁弁19を、制御盤から
の非常停止信号により全開し、炉内圧を急速に減
圧する。 The positioner output signals of the pressure control valve 13 and the pressure reduction control valve 14 are cut by a signal cut-off solenoid valve,
Forcibly closes the pressure control valve 13 fully and reduces the pressure control valve 14.
fully open. The emergency shutoff valve 18 provided in the pressurized gas piping line is fully closed by an emergency stop signal from the control panel, and the inflow gas circuit is cut off. The large-diameter emergency discharge solenoid valve 19 on the exhaust line is fully opened in response to an emergency stop signal from the control panel, and the pressure inside the furnace is rapidly reduced.
発明の効果
以上のように、この発明によれば、加圧式注湯
炉において、加圧調節弁と減圧調節弁とを設け
て、炉内の検出気体圧と設定気体圧との差に応じ
て加圧調節弁と減圧調節弁とを制御することによ
り注湯炉の加圧力を制御するようにしたから、従
来の装置に比して、貯湯室内圧力の制御応答速度
を早くできるとともに、正確な圧力制御が可能と
なる。Effects of the Invention As described above, according to the present invention, in a pressurized pouring furnace, a pressure control valve and a pressure reduction control valve are provided to adjust the pressure according to the difference between the detected gas pressure and the set gas pressure in the furnace. Since the pressurizing force of the pouring furnace is controlled by controlling the pressure regulating valve and the pressure reducing regulating valve, it is possible to control the pressure in the hot water storage chamber faster and more accurately than with conventional devices. Pressure control becomes possible.
第1図はこの発明の一実施例を示す系統図、第
2図と第3図は加圧式注湯炉の動作原理を示す断
面図、第4図と第5図は第1図の装置の動作を示
す特性曲線である。
1……加圧式注湯炉、2……貯湯室、10……
圧力検出器、11……圧力調節計、13……加圧
調節弁、14……減圧調節弁。
Fig. 1 is a system diagram showing an embodiment of the present invention, Figs. 2 and 3 are sectional views showing the operating principle of a pressurized pouring furnace, and Figs. 4 and 5 are diagrams of the apparatus shown in Fig. 1. This is a characteristic curve showing the operation. 1... Pressurized pouring furnace, 2... Hot water storage room, 10...
Pressure detector, 11...pressure regulator, 13...pressure control valve, 14...pressure reduction control valve.
Claims (1)
通する注湯室5と、上記貯湯室に加圧系統を介し
て加圧気体を供給する加圧気体供給手段とを備
え、上記加圧気体供給手段から上記貯湯室に溶湯
の貯湯量に見合つたベース圧を印加した後、シヨ
ツト圧を加圧することにより上記注湯室の注湯口
8から所定量の溶湯を注出する加圧式注湯炉にお
いて、 上記貯湯室内の圧力を検出する圧力検出手段1
0と、 上記加圧気体供給手段から上記貯湯室へ加圧気
体を供給する加圧系統に備わる弁開度調整可能な
加圧調整弁13,16と、 上記貯湯室内の気体を貯湯室の外部へ放出する
減圧系統に備わる弁開度調整可能な減圧調整弁1
4,17と、 上記貯湯室内の貯湯重量を検出する貯湯重量検
出手段12と、 上記貯湯重量検出手段によつて検出された貯湯
重量に応じて上記ベース圧及び上記シヨツト圧を
演算し上記貯湯室内の圧力設定値としての制御信
号を送出する制御装置20と、 上記制御信号の示す上記圧力設定値と上記圧力
検出手段から供給される上記貯湯室の圧力検出値
との偏差がゼロの状態のときには、上記貯湯室内
への加圧と減圧とが平衡するように、上記加圧調
整弁及び上記減圧調整弁に対して相関した弁開度
となるようなコントロール信号を発生し、上記偏
差が平衡状態から貯湯室内の圧力が上昇する方向
へ変化したときには、上記加圧調整弁の弁開度が
減少し上記減圧調整弁の弁開度が増加するように
コントロール信号を発生し、上記偏差が平衡状態
から貯湯室内の圧力が下降する方向へ変化したと
きには、上記加圧調整弁の弁開度が増加し上記減
圧調整弁の弁開度が減少するようにコントロール
信号を発生する圧力調整手段11と、 を備えたことを特徴とする加圧式貯湯炉。[Scope of Claims] 1. A hot water storage chamber 2 for storing molten metal, a pouring chamber 5 communicating with the hot water storage chamber, and pressurized gas supply means for supplying pressurized gas to the hot water storage chamber via a pressurization system. After applying a base pressure corresponding to the amount of molten metal stored in the molten metal from the pressurized gas supply means to the molten metal storage chamber, a predetermined amount of molten metal is poured from the pouring port 8 of the molten metal pouring chamber by increasing shot pressure. Pressure detection means 1 for detecting the pressure inside the hot water storage chamber in the pressurized pouring furnace
0, pressurization adjustment valves 13 and 16 that are provided in a pressurization system that supplies pressurized gas from the pressurized gas supply means to the hot water storage chamber, and whose opening degree can be adjusted; Pressure reduction regulating valve 1 with adjustable valve opening included in the pressure reduction system that releases to
4, 17; stored hot water weight detection means 12 for detecting the weight of hot water stored in the hot water storage chamber; when the deviation between the pressure setting value indicated by the control signal and the pressure detection value of the hot water storage chamber supplied from the pressure detection means is zero; , so that the pressurization and depressurization in the hot water storage chamber are balanced, a control signal is generated for the pressurization adjustment valve and the pressure reduction adjustment valve so that the valve opening degrees are correlated, and the deviation is in an equilibrium state. When the pressure in the hot water storage chamber changes in the direction of increasing from pressure regulating means 11 that generates a control signal so that when the pressure in the hot water storage chamber changes in a direction in which the pressure in the hot water storage chamber decreases, the opening degree of the pressure regulating valve increases and the opening degree of the pressure reducing regulating valve decreases; A pressurized hot water storage furnace characterized by being equipped with.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP28174684A JPS61150765A (en) | 1984-12-25 | 1984-12-25 | Pressure type pouring furnace |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP28174684A JPS61150765A (en) | 1984-12-25 | 1984-12-25 | Pressure type pouring furnace |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS61150765A JPS61150765A (en) | 1986-07-09 |
| JPH0445262B2 true JPH0445262B2 (en) | 1992-07-24 |
Family
ID=17643403
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP28174684A Granted JPS61150765A (en) | 1984-12-25 | 1984-12-25 | Pressure type pouring furnace |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS61150765A (en) |
Families Citing this family (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2643651B2 (en) * | 1991-04-18 | 1997-08-20 | 日立金属株式会社 | Automatic hot water distribution device |
| JP2020163399A (en) * | 2019-03-28 | 2020-10-08 | 宇部興産機械株式会社 | Casting equipment |
Family Cites Families (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| NZ195142A (en) * | 1979-10-15 | 1984-09-28 | Commw Scient Ind Res Org | Monitoring integrity of longitudinal steel members in conveyor belts and cables |
-
1984
- 1984-12-25 JP JP28174684A patent/JPS61150765A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS61150765A (en) | 1986-07-09 |
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