JPH08103848A - Adjusting method of kneading molding sand and device therefor - Google Patents

Adjusting method of kneading molding sand and device therefor

Info

Publication number
JPH08103848A
JPH08103848A JP26114794A JP26114794A JPH08103848A JP H08103848 A JPH08103848 A JP H08103848A JP 26114794 A JP26114794 A JP 26114794A JP 26114794 A JP26114794 A JP 26114794A JP H08103848 A JPH08103848 A JP H08103848A
Authority
JP
Japan
Prior art keywords
sand
water
bentonite
temperature
kneading
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.)
Granted
Application number
JP26114794A
Other languages
Japanese (ja)
Other versions
JP2982629B2 (en
Inventor
Takashi Suginaka
隆司 杉中
Risaburo Kimura
利三郎 木村
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 JP6261147A priority Critical patent/JP2982629B2/en
Priority to US08/529,758 priority patent/US5816312A/en
Priority to KR1019950032012A priority patent/KR100362782B1/en
Priority to DE19536803A priority patent/DE19536803B4/en
Publication of JPH08103848A publication Critical patent/JPH08103848A/en
Application granted granted Critical
Publication of JP2982629B2 publication Critical patent/JP2982629B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Landscapes

  • Molds, Cores, And Manufacturing Methods Thereof (AREA)

Abstract

PURPOSE: To reduce the cost for molding a green sand mold by adjusting the combining ratio of water to bentonite based on the water content and the temp. of high temp. sand. CONSTITUTION: High temp. recovered sand is sent from a hopper 2 and new sand is sent from a hopper 4 to a sand weigher 6. The water content in the recovered sand in the hopper 2 is measured with a water content sensor 13. The bentonite is transferred from a hopper 7 to a bentonite weigher 9 with a signal of an arithmetic controller 14, and its quantity is measured with a load cell 16. When the bentonite quantity reaches the calculated quantity, a screw conveyor 8 is stopped and the bentonite in the weigher 9 is supplied to a vacuum kneading vessel 1 through a pressure feeding tank 10 and the sand weigher 6. The water is supplied to the vacuum kneading vessel 1 from a water weigher 11 with a signal of the arithmetic controller 14. In such a way, the combining ratio of the water is adjusted and also, the combining ratio of the bentonite is adjusted. By this method, while keeping the strength of the green sand mold molded after vacuum-kneading, the consumption of the bentonite can be restrained.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明は、真空混練槽を利用した
鋳物砂の混練調整方法及び混練調整装置に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a kneading adjusting method and a kneading adjusting device for molding sand using a vacuum kneading tank.

【0002】[0002]

【従来の技術】生型造形ラインは、混練、造形、鋳込
み、型ばらし、続いて必要に応じ新砂を加えての再度混
練という一連の循環系をなしており、高温の回収砂を再
利用するため混練後の鋳物砂の温度が上がりやすく、こ
れを防止するため、従来はサンドクーラーにより回収砂
を40℃程度に冷却したうえで混練に供していた。
2. Description of the Related Art A green molding line has a circulation system of kneading, molding, pouring, separating, and then kneading again by adding new sand if necessary, and reusing high temperature recovered sand. Therefore, the temperature of the foundry sand after kneading tends to rise, and in order to prevent this, conventionally, the recovered sand was cooled to about 40 ° C. before being subjected to kneading.

【0003】一方、最近では生型造形ラインの砂処理設
備として真空混練槽が一部で導入され、40〜70℃の
高温砂でも該混練槽内で一気に40℃以下の設定温度に
冷却できるようになった。これは、真空混練槽内に高温
砂と、ベントナイト、及び水(混練後の鋳物砂を所定の
水分値に保つための水と、高温砂を冷却するための水)
を入れ、混練槽内を減圧しつつ混練するというもので、
混練槽内を減圧することで水の沸点が下がり、添加した
水の一部(冷却水)が蒸発し、砂はこのとき発生する気
化潜熱によって設定温度まで冷却される。
On the other hand, recently, a vacuum kneading tank has been partially introduced as sand processing equipment for a green molding line so that even high temperature sand of 40 to 70 ° C. can be cooled to a set temperature of 40 ° C. or less at once in the kneading tank. Became. This is high temperature sand, bentonite, and water in the vacuum kneading tank (water for keeping the casting sand after kneading at a predetermined water content, and water for cooling the high temperature sand).
And kneading while reducing the pressure in the kneading tank.
By reducing the pressure in the kneading tank, the boiling point of water is lowered, part of the added water (cooling water) evaporates, and the sand is cooled to the set temperature by the latent heat of vaporization generated at this time.

【0004】[0004]

【発明が解決しようとする課題】ところで、混練後の鋳
物砂に含まれる水は砂粒表面に付着した付着水とベント
ナイトの結晶層に浸透した吸着水に分けられ、結晶層に
浸透した水は蒸発しにくく鋳物砂の保水性を向上させ
る。真空混練槽で混練した鋳物砂の場合、通常の大気圧
混練の場合と比較して保水性がよく、しかも高温砂にな
るほど混練後の鋳物砂の保水性が向上する。これは、高
温砂になるほど冷却水量が多く、真空混練槽内での水蒸
気の発生量が増え、ベントナイトの結晶層に浸透しやす
くなるためであると考えられる。
By the way, the water contained in the foundry sand after kneading is divided into the adhered water adhering to the surface of the sand grains and the adsorbed water penetrating into the bentonite crystal layer, and the water permeating into the crystal layer evaporates. It is difficult to do and improves the water retention of the foundry sand. In the case of the molding sand kneaded in the vacuum kneading tank, the water retention is better than in the case of ordinary atmospheric pressure kneading, and the higher the temperature of the sand is, the more the water retention of the molding sand after kneading is improved. It is considered that this is because as the temperature of the sand becomes higher, the amount of cooling water increases, the amount of water vapor generated in the vacuum kneading tank increases, and the water easily penetrates into the bentonite crystal layer.

【0005】そして、ベントナイトの結晶層に浸透した
吸着水はベントナイトを活性化して生型強度(抗圧力)
の立ち上がりを速くすると同時に、生型強度を高める作
用をなす。図2は、25℃の回収砂と65℃の回収砂に
同じ配合率でベントナイトを添加し、真空混練槽で混練
後造形した生型の抗圧力と水分量の関係を示すグラフで
あり、65℃の高温砂を使用した生型の方が抗圧力が高
くなっている。なお、同図には比較のため大気圧下で混
練後造形した生型の抗圧力も記載した。
The adsorbed water that has penetrated into the bentonite crystal layer activates the bentonite to produce the green strength (coercive force).
It has the effect of increasing the strength of green mold while at the same time increasing the rising speed of. FIG. 2 is a graph showing the relationship between the coercive pressure and the water content of the green mold, which was produced by adding bentonite to the recovered sand of 25 ° C. and the recovered sand of 65 ° C. at the same mixing ratio and kneading in a vacuum kneading tank. The raw pressure using high temperature sand at ℃ has higher coercive force. For comparison, the figure also shows the coercive pressure of the green mold molded after kneading under atmospheric pressure.

【0006】上記真空混練槽を利用するときも、これま
では大気中で混練するときと同様に、温度に関わりなく
砂に対するベントナイトの配合率が一定に保たれるよう
に調整していたが、高温の砂を使用したものほど生型強
度が向上することに着目すれば、生型強度が所定以上の
値に保たれる限り粘結材としてのベントナイトの配合率
を減少させることもできるはずである。本発明は上記知
見に基づいてなされたもので、生型の強度(抗圧力)を
維持しつつ、砂の温度に基づいてベントナイトの配合率
の調整を行うことで、ベントナイトの使用量を抑制し生
型造型コストの低減を図ることを目的とする。
Even when the above-mentioned vacuum kneading tank is used, the mixing ratio of bentonite to sand has been adjusted to be constant regardless of temperature, as in the case of kneading in the air. If attention is paid to the fact that the green mold strength is improved with the use of high-temperature sand, it should be possible to reduce the blending ratio of bentonite as a binder as long as the green mold strength is maintained at a predetermined value or more. is there. The present invention has been made based on the above findings, while maintaining the strength of the green mold (coercive pressure), by adjusting the blending ratio of bentonite based on the temperature of the sand, to suppress the amount of bentonite used The purpose is to reduce the cost of green molding.

【0007】[0007]

【課題を解決するための手段】本発明に関わる鋳物砂の
混練調整方法は、真空混練槽内に高温砂及びベントナイ
トを投入し、水を添加して混練するもので、上記高温砂
の含水率及び温度に基づき添加する水の配合率を調整す
るとともに、高温砂の温度に基づきベントナイトの配合
率を調整することを特徴とする。より具体的には、添加
する水が混練後の鋳物砂の水分値を一定にするための添
加水と、高温砂の温度を低下させるための冷却水からな
り、冷却水の配合率が高温砂の温度に基づき調整される
ことを特徴とする。
The method for adjusting the kneading of foundry sand according to the present invention is one in which high temperature sand and bentonite are put into a vacuum kneading tank, and water is added and kneading. And adjusting the mixing ratio of water to be added based on the temperature, and adjusting the mixing ratio of bentonite based on the temperature of the high-temperature sand. More specifically, the water to be added consists of added water for keeping the moisture value of the foundry sand after kneading constant and cooling water for lowering the temperature of the high temperature sand, and the mixing ratio of the cooling water is high temperature sand. It is characterized in that it is adjusted based on the temperature.

【0008】また、本発明に関わる鋳物砂の混練調整装
置は、真空混練槽と、該真空混練槽に対し高温砂、ベン
トナイト、及び水を供給する各供給装置と、高温砂の含
水量を測定する含水量測定手段と、高温砂の温度を測定
する温度測定手段と、上記含水量測定手段と温度測定手
段の信号を受けて所定の配合率で水を供給するように上
記水供給装置を制御するとともに、温度測定手段の信号
を受けて所定の配合率でベントナイトを供給するように
該ベントナイト供給装置を制御する制御手段を備えるこ
とを特徴とする。
Further, a kneading adjusting device for foundry sand according to the present invention is a vacuum kneading tank, each supplying device for supplying high temperature sand, bentonite, and water to the vacuum kneading tank, and measuring the water content of the high temperature sand. Water content measuring means, temperature measuring means for measuring the temperature of high-temperature sand, and controlling the water supply device so as to receive water from the water content measuring means and the temperature measuring means and supply water at a predetermined mixing ratio. In addition, it is characterized by comprising control means for receiving the signal from the temperature measuring means and controlling the bentonite supply device so as to supply bentonite at a predetermined mixing ratio.

【0009】[0009]

【作用】先に述べたように、真空混練槽内で混練する場
合、砂の温度が高いほど同じ生型強度を得るためのベン
トナイト配合率は少なくて済む。そこで、本発明では、
例えば所定の生型強度を得ることができるベントナイト
配合率と砂の温度の関係を予め求めておき、真空混練槽
に投入された砂の温度をその都度測定し、その温度に対
応する配合率でベントナイトを投入する。
As described above, when kneading in a vacuum kneading tank, the higher the temperature of the sand, the smaller the blending ratio of bentonite for obtaining the same green strength. Therefore, in the present invention,
For example, the relationship between the blending ratio of bentonite that can obtain a predetermined green strength and the temperature of sand is obtained in advance, and the temperature of the sand put into the vacuum kneading tank is measured each time, and the mixing ratio corresponding to that temperature is obtained. Add bentonite.

【0010】[0010]

【実施例】以下、本発明の実施例を図1を参照して説明
する。図1に示すものは生型造形ラインにおける鋳物砂
の混練調整装置であり、真空混練槽1と、回収砂ホッパ
2、振動フィーダ3、新砂ホッパ4、スクリューコンベ
ア5、及び回収砂及び新砂を計量する砂計量器6等から
なる砂供給装置と、ベントナイトホッパ7、スクリュー
コンベア8、ベントナイト計量器9及び圧送タンク10
等からなるベントナイト供給装置と、水計量器11と、
真空混練槽1に設置された温度センサ12、回収砂ホッ
パ2に設置された含水量センサ13と、温度センサ12
及び含水量センサ13からの信号等に基づき上記各供給
装置を制御する演算コントローラ14から構成される。
なお、Mは各装置の駆動モータを示す。
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENT An embodiment of the present invention will be described below with reference to FIG. 1 shows a kneading adjustment device for foundry sand in a green molding line, which measures a vacuum kneading tank 1, a recovered sand hopper 2, a vibration feeder 3, a new sand hopper 4, a screw conveyor 5, and recovered sand and new sand. Sand supply device including a sand measuring device 6 and the like, a bentonite hopper 7, a screw conveyor 8, a bentonite measuring device 9, and a pressure feeding tank 10.
A bentonite supply device including a water meter 11 and the like,
Temperature sensor 12 installed in the vacuum kneading tank 1, water content sensor 13 installed in the recovered sand hopper 2, and temperature sensor 12
And an arithmetic controller 14 that controls each of the above-mentioned supply devices based on signals from the water content sensor 13.
In addition, M shows the drive motor of each apparatus.

【0011】一方、添加される水のうち冷却水の配合率
は砂の比熱に比例し、供給される砂の温度が真空混練槽
の設定温度(混練後の砂の温度、例えば40℃)と同一
のときゼロで、砂の温度がそれより高くなるほど高い配
合率となるように設定され、ベントナイトの配合率は、
供給される砂の温度が設定温度と同一のとき最大値をと
り、砂の温度がそれより高くなるほど低い配合率となる
ように設定され、いずれも上記演算コントローラ14に
予め入力されている。なお、供給される砂の温度が設定
温度未満のときは、冷却水の配合率はゼロ、ベントナイ
トの配合率は上記設定温度における配合率に設定され
る。
On the other hand, the mixing ratio of the cooling water in the added water is proportional to the specific heat of the sand, and the temperature of the supplied sand is equal to the set temperature of the vacuum kneading tank (the temperature of the sand after kneading, eg 40 ° C.). It is set to zero at the same time, and the higher the sand temperature, the higher the mixing ratio, and the mixing ratio of bentonite is
When the temperature of the supplied sand is the same as the set temperature, it takes a maximum value, and the higher the sand temperature is, the lower the mixing ratio is set, and both are preliminarily input to the arithmetic controller 14. When the temperature of the supplied sand is lower than the preset temperature, the blending ratio of the cooling water is set to zero and the blending ratio of bentonite is set to the blending ratio at the preset temperature.

【0012】この鋳物砂の混練調整装置の作動について
順に説明すると、まず演算コントローラ14の信号で、
高温の回収砂が回収砂ホッパ2から振動フィーダ3を経
て砂計量器6に送られ、必要に応じて新砂が新砂ホッパ
4からスクリューコンベア5を経て砂計量器6に送ら
れ、ここでロードセル15により重量を測定され、その
測定信号は計量のあいだ演算コントローラ14に入力さ
れる。それが予定重量に達したとき、演算コントローラ
14は振動フィーダ3及びスクリューコンベア5の作動
をストップする信号を出す。なお、回収砂の含水量が回
収砂ホッパ2内の含水量センサ13により測定され、そ
の測定信号が演算コントローラ14に入力される。
The operation of this kneading adjusting device for foundry sand will be described in order. First, with the signal from the arithmetic controller 14,
The high temperature recovered sand is sent from the recovered sand hopper 2 to the sand meter 6 via the vibration feeder 3 and, if necessary, the new sand is sent from the new sand hopper 4 to the sand meter 6 via the screw conveyor 5, where the load cell 15 The weight is measured by and the measurement signal is input to the arithmetic controller 14 during weighing. When it reaches the predetermined weight, the arithmetic controller 14 gives a signal to stop the operation of the vibrating feeder 3 and the screw conveyor 5. The water content of the recovered sand is measured by the water content sensor 13 in the recovered sand hopper 2, and the measurement signal is input to the arithmetic controller 14.

【0013】続いて、砂計量器6内の砂は真空混練槽1
に供給され、真空混練槽1内で大気圧下で予備混練され
る。このときの砂の温度が温度センサ12で測定され、
その測定信号は演算コントローラ14に入力される。演
算コントローラ14では、回収砂の含水量の測定値から
混練後の鋳物砂を所定の水分値に保つために必要な水の
配合率が演算され、温度の測定値から冷却水の配合率と
ベントナイトの配合率が求められ、砂の重量に応じて実
際に必要とされる水の総量及びベントナイトの量が演算
される。
Subsequently, the sand in the sand meter 6 is vacuum kneading tank 1
And is pre-kneaded in the vacuum kneading tank 1 under atmospheric pressure. The temperature of the sand at this time is measured by the temperature sensor 12,
The measurement signal is input to the arithmetic controller 14. The operation controller 14 calculates the mixing ratio of water required to keep the molding sand after kneading at a predetermined moisture value from the measured value of the water content of the recovered sand, and from the measured value of the temperature, the mixing ratio of the cooling water and the bentonite. Is calculated, and the total amount of water and the amount of bentonite actually required are calculated according to the weight of sand.

【0014】次に、演算コントローラ14の信号で、ベ
ントナイトがベントナイトホッパ7からスクリューコン
ベア8を経てベントナイト計量器9に送られ、ここでベ
ントナイトの量がロードセル16により測定され、その
測定信号は計量のあいだ演算コントローラに入力され
る。ベントナイト量が前記演算値に達したとき、演算コ
ントローラ14はスクリューコンベア8をストップする
信号を出す。続いて、ベントナイト計量器9内のベント
ナイトは圧送タンク10に移され、空気圧送により砂計
量器6を経て真空混練槽1に供給される。また、同時に
演算コントローラ14の信号で、水計量器11から水が
真空混練槽1に供給される。
Next, the bentonite is sent from the bentonite hopper 7 through the screw conveyor 8 to the bentonite meter 9 by a signal from the arithmetic controller 14, where the amount of bentonite is measured by the load cell 16, and the measured signal is measured. In the meantime, it is input to the arithmetic controller. When the bentonite amount reaches the calculated value, the calculation controller 14 outputs a signal to stop the screw conveyor 8. Then, the bentonite in the bentonite meter 9 is transferred to the pressure feed tank 10 and is supplied to the vacuum kneading tank 1 via the sand meter 6 by air pressure feed. At the same time, water is supplied from the water meter 11 to the vacuum kneading tank 1 by a signal from the arithmetic controller 14.

【0015】真空混練槽1に砂、ベントナイト及び水が
供給された後、真空混練槽1内を減圧し真空混練に移
り、所定時間混練した後、大気圧に戻し、鋳物砂を造型
機に送る。なお、上記実施例では、砂の温度とベントナ
イトの配合率の関係を設定し、砂の温度測定値からベン
トナイトの配合率を直接求めるようにしたが、砂の温度
が高く冷却水の配合率が高くなるとベントナイトの配合
率を低く設定できるという関係にあることから、冷却水
の配合率とベントナイトの配合率の関係を設定しこれを
演算コントローラに入力しておき、温度の測定値から冷
却水の配合率を求め、冷却水の配合率からベントナイト
の配合率を求めるようにしてもよい。
After the sand, bentonite and water are supplied to the vacuum kneading tank 1, the pressure in the vacuum kneading tank 1 is reduced to vacuum kneading, and after kneading for a predetermined time, the pressure is returned to atmospheric pressure and the molding sand is sent to the molding machine. . In the above example, the relationship between the sand temperature and the blending ratio of bentonite was set, and the blending ratio of bentonite was directly obtained from the measured temperature of sand. Since the ratio of bentonite can be set lower when it becomes higher, the relationship between the ratio of cooling water and the ratio of bentonite is set, and this is input to the arithmetic controller. The blending ratio may be determined, and the blending ratio of bentonite may be determined from the blending ratio of cooling water.

【0016】[0016]

【発明の効果】本発明によれば、真空混練後造形される
生型の強度を維持しつつ、ベントナイトの使用量を抑制
し生型造型コストの低減を図ることができる。
According to the present invention, it is possible to suppress the amount of bentonite used and reduce the cost of molding a green mold while maintaining the strength of the green mold molded after vacuum kneading.

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

【図1】実施例の鋳物砂混練調整装置の説明図である。FIG. 1 is an explanatory view of a molding sand kneading adjusting device of an embodiment.

【図2】真空混連後造型した生型の抗圧力と水分量の関
係を示す図である。
FIG. 2 is a diagram showing a relationship between a coercive pressure and a water content of a green mold produced after vacuum mixing.

Claims (3)

【特許請求の範囲】[Claims] 【請求項1】 真空混練槽内に高温砂及びベントナイト
を投入し、水を添加して混練する鋳物砂の混練調整方法
において、上記高温砂の含水量及び温度に基づき添加す
る水の配合率を調整するとともに、高温砂の温度に基づ
きベントナイトの配合率を調整することを特徴とする鋳
物砂の混練調整方法。
1. A method for kneading a molding sand in which high temperature sand and bentonite are put into a vacuum kneading tank and kneaded by adding water, wherein the mixing ratio of water to be added is based on the water content and temperature of the high temperature sand. A method for adjusting the kneading of foundry sand, which comprises adjusting the blending ratio of bentonite based on the temperature of high-temperature sand.
【請求項2】 添加する水が、混練後の鋳物砂の水分値
を一定にするための添加水と、高温砂の温度を低下させ
るための冷却水からなり、冷却水の配合率が高温砂の温
度に基づき調整されることを特徴とする請求項1に記載
された鋳物砂の混練調整方法。
2. The added water comprises added water for keeping the moisture value of the foundry sand after kneading constant and cooling water for lowering the temperature of the high temperature sand, and the mixing ratio of the cooling water is high temperature sand. It adjusts based on the temperature of the said, The kneading | mixing adjustment method of the molding sand of Claim 1 characterized by the above-mentioned.
【請求項3】 真空混練槽と、該真空混練槽に対し高温
砂、ベントナイト、及び水を供給する各供給装置と、高
温砂の含水量を測定する含水量測定手段と、高温砂の温
度を測定する温度測定手段と、上記含水量測定手段と温
度測定手段の信号を受けて所定の配合率で水を供給する
ように上記水供給装置を制御するとともに、温度測定手
段の信号を受けて所定の配合率でベントナイトを供給す
るように該ベントナイト供給装置を制御する制御手段を
備えることを特徴とする鋳物砂の混練調整装置。
3. A vacuum kneading tank, supply devices for supplying high temperature sand, bentonite, and water to the vacuum kneading tank, water content measuring means for measuring the water content of the high temperature sand, and temperature of the high temperature sand. The water supply device is controlled so as to supply water at a predetermined mixing ratio by receiving signals from the temperature measuring means for measuring, the water content measuring means and the temperature measuring means, and at the same time receiving signals from the temperature measuring means. A kneading adjustment device for foundry sand, comprising control means for controlling the bentonite supply device so as to supply bentonite at a mixing ratio of.
JP6261147A 1994-09-30 1994-09-30 Method and apparatus for adjusting kneading of foundry sand Expired - Fee Related JP2982629B2 (en)

Priority Applications (4)

Application Number Priority Date Filing Date Title
JP6261147A JP2982629B2 (en) 1994-09-30 1994-09-30 Method and apparatus for adjusting kneading of foundry sand
US08/529,758 US5816312A (en) 1994-09-30 1995-09-18 Method of and apparatus for reclaiming foundry sand
KR1019950032012A KR100362782B1 (en) 1994-09-30 1995-09-27 Recycling method and apparatus for casting sand
DE19536803A DE19536803B4 (en) 1994-09-30 1995-10-02 Process and device for the treatment of foundry sand

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP6261147A JP2982629B2 (en) 1994-09-30 1994-09-30 Method and apparatus for adjusting kneading of foundry sand

Publications (2)

Publication Number Publication Date
JPH08103848A true JPH08103848A (en) 1996-04-23
JP2982629B2 JP2982629B2 (en) 1999-11-29

Family

ID=17357762

Family Applications (1)

Application Number Title Priority Date Filing Date
JP6261147A Expired - Fee Related JP2982629B2 (en) 1994-09-30 1994-09-30 Method and apparatus for adjusting kneading of foundry sand

Country Status (1)

Country Link
JP (1) JP2982629B2 (en)

Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH08300098A (en) * 1995-04-04 1996-11-19 Mas Fab Gustav Eirich Method and apparatus for cooling of casting sand
JPH1080745A (en) * 1996-09-06 1998-03-31 Sintokogio Ltd Binder feeder for molding sand
JPH10146644A (en) * 1996-11-15 1998-06-02 Sintokogio Ltd C/b value control system of kneaded sand
JPH10249482A (en) * 1997-03-10 1998-09-22 Mazda Motor Corp Method for regenerating molding sand
JP2003535700A (en) * 2000-06-23 2003-12-02 マシネンファブリク グスタフ アイリッヒ Method and apparatus for compounding sand foundry
JP2010528873A (en) * 2007-06-11 2010-08-26 マシーネンファブリーク・グスタフ・アイリッヒ・ゲゼルシャフト・ミット・ベシュレンクテル・ハフツング・ウント・コムパニー・コマンディットゲゼルシャフト Method for processing molding sand
CN107377870A (en) * 2017-08-14 2017-11-24 湖北亚钢金属制造有限公司 A kind of sand mixer for casting
WO2018100804A1 (en) * 2016-11-29 2018-06-07 新東工業株式会社 Casting sand binder supply apparatus and binder supply method

Cited By (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH08300098A (en) * 1995-04-04 1996-11-19 Mas Fab Gustav Eirich Method and apparatus for cooling of casting sand
JPH1080745A (en) * 1996-09-06 1998-03-31 Sintokogio Ltd Binder feeder for molding sand
JPH10146644A (en) * 1996-11-15 1998-06-02 Sintokogio Ltd C/b value control system of kneaded sand
JPH10249482A (en) * 1997-03-10 1998-09-22 Mazda Motor Corp Method for regenerating molding sand
JP2003535700A (en) * 2000-06-23 2003-12-02 マシネンファブリク グスタフ アイリッヒ Method and apparatus for compounding sand foundry
JP2010528873A (en) * 2007-06-11 2010-08-26 マシーネンファブリーク・グスタフ・アイリッヒ・ゲゼルシャフト・ミット・ベシュレンクテル・ハフツング・ウント・コムパニー・コマンディットゲゼルシャフト Method for processing molding sand
WO2018100804A1 (en) * 2016-11-29 2018-06-07 新東工業株式会社 Casting sand binder supply apparatus and binder supply method
CN109982787A (en) * 2016-11-29 2019-07-05 新东工业株式会社 The bonding agent feeding device and binder supply method of molding sand
JPWO2018100804A1 (en) * 2016-11-29 2019-10-17 新東工業株式会社 Binder supply apparatus and binder supply method for foundry sand
CN107377870A (en) * 2017-08-14 2017-11-24 湖北亚钢金属制造有限公司 A kind of sand mixer for casting

Also Published As

Publication number Publication date
JP2982629B2 (en) 1999-11-29

Similar Documents

Publication Publication Date Title
RU2476289C2 (en) Method of making sand blend
JPH08103848A (en) Adjusting method of kneading molding sand and device therefor
US4852028A (en) Method and apparatus for measuring and controlling the volumetric weight of an expanded particulate material
CN108319214A (en) A kind of control method of Weightlessness balance, apparatus and system
JPS59102896A (en) Method for controlling shape of single crystal
CN107639212A (en) One kind, which is poured, wraps automatic stream inoculation device
JP2002542018A (en) Monitoring method of coal filling level of ball mill
JP4353596B2 (en) Casting sand kneading adjustment method
JPH0976044A (en) Method for reclamation of molding sand and its device
JPS62174617A (en) Weighing method for granule
JP6635192B2 (en) Kneading sand property adjustment system and property adjustment method
JP2523821B2 (en) Raw material supply device for CZ furnace
JPS56117853A (en) Method for adjusting moisture of grains and fine particles
JPH10225921A (en) Reinforcing fiber supply device
JP2002205304A (en) Method and apparatus for correcting composition of ready-mixed concrete
CN108106705A (en) A kind of controllable rubber injection mold feeding control system of preheating temperature weight
CN211888865U (en) Sand mixing and water adding system
JPS5922510Y2 (en) Automatic test equipment for reduction and powdering of sintered grains
CN114309494B (en) Casting method for dynamically controlling feeding speed of vermiculizer and nodulizer cored wire
SU1689793A1 (en) Method of coal ash analysis
JP2004154996A (en) Method and apparatus for producing ready-mixed concrete
SU1390496A1 (en) Apparatus for continuous drying of materials
JPS57140397A (en) Method and apparatus for manufacturing crystal
JPH0510179B2 (en)
SU1613249A1 (en) System for dosing molten cast iron

Legal Events

Date Code Title Description
A01 Written decision to grant a patent or to grant a registration (utility model)

Free format text: JAPANESE INTERMEDIATE CODE: A01

Effective date: 19990906

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20080924

Year of fee payment: 9

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20090924

Year of fee payment: 10

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20100924

Year of fee payment: 11

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20110924

Year of fee payment: 12

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20120924

Year of fee payment: 13

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20120924

Year of fee payment: 13

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20130924

Year of fee payment: 14

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

LAPS Cancellation because of no payment of annual fees