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JPS6033549B2 - Mold release agent treatment method - Google Patents
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JPS6033549B2 - Mold release agent treatment method - Google Patents

Mold release agent treatment method

Info

Publication number
JPS6033549B2
JPS6033549B2 JP55137899A JP13789980A JPS6033549B2 JP S6033549 B2 JPS6033549 B2 JP S6033549B2 JP 55137899 A JP55137899 A JP 55137899A JP 13789980 A JP13789980 A JP 13789980A JP S6033549 B2 JPS6033549 B2 JP S6033549B2
Authority
JP
Japan
Prior art keywords
solution
tank
mold
release agent
concentration
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
Application number
JP55137899A
Other languages
Japanese (ja)
Other versions
JPS5762836A (en
Inventor
勝美 石田
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.)
TOKYO RIKA Manufacturing
Original Assignee
TOKYO RIKA Manufacturing
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 TOKYO RIKA Manufacturing filed Critical TOKYO RIKA Manufacturing
Priority to JP55137899A priority Critical patent/JPS6033549B2/en
Publication of JPS5762836A publication Critical patent/JPS5762836A/en
Publication of JPS6033549B2 publication Critical patent/JPS6033549B2/en
Expired legal-status Critical Current

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  • Application Of Or Painting With Fluid Materials (AREA)
  • Casting Devices For Molds (AREA)
  • Coating Apparatus (AREA)

Description

【発明の詳細な説明】 本発明は離型剤処理方法に係り、金属鋳造、ダィキャス
ト鋳造などの鋳造において金型の型面に噴射して製品の
滋型性をよくする離型剤を回収して再使用できるように
したものに関する。
[Detailed Description of the Invention] The present invention relates to a mold release agent treatment method, which recovers a mold release agent that is sprayed onto the mold surface of a mold in metal casting, die casting, etc. to improve the moldability of the product. Concerning things that can be reused.

従釆、ダィキャスト鋳造などの鋳造に際しては、金型に
離型剤の溶液を噴射して塗着することが行われているが
、この場合、余分な溶液は金型から流出するとともに、
工場廃液として排出されている頃向が大である。
When casting, such as mold casting or die casting, a mold release agent solution is sprayed onto the mold to apply it, but in this case, the excess solution flows out from the mold and
Most of the waste is discharged as factory waste.

しかし、このような処理の仕方によると、離型剤の溶液
によって環境を汚染し公害問題が生じるとともに、不経
済であるなどの問題を有している。
However, this method of treatment has problems such as the release agent solution contaminates the environment, causing pollution problems, and is uneconomical.

本発明はこのように点に鑑みなされたもので、金型に噴
射した離型剤の溶液を回収するとともに、これを金型に
噴射できる所定の濃度に設定して再使用を可能にし、こ
れにより、公害問題の発生を未然に防止するとともに離
型剤を経済的に使用できるようにしたことを目的とする
のである。
The present invention was made in view of the above points, and it is possible to recover the solution of the mold release agent sprayed onto the mold, set it to a predetermined concentration that allows it to be sprayed onto the mold, and make it possible to reuse it. The purpose is to prevent the occurrence of pollution problems and to make it possible to use mold release agents economically.

本発明の方法は、金型に噴射した離型剤溶液を回収して
分離槽内に導入し、この分離槽内において溶液から油な
どの不純物を分離除去するとともに、この溶液をざらフ
ィル夕にかけて炉過したのちこれを貯留槽内に導入し、
この貯留槽内の溶液の濃度を測定して希釈溶液または原
液を加えて溶液を所定の濃度に設定するとともに、この
溶液を上記金型に噴射するようにしたものである。つぎ
に、本発明の一実施例を添附図面を参照して説明する。
図において、1は鋳造部で、この鋳造部1には固定金型
2と可動金型3からなる金型4が設けられ、上記可動金
型3は、シリンダ、ポンプ、配管などからなる金型可動
機構5によって上記固定金型2に対して進退され、それ
ぞれの型面6,7によって型合せ時にキャビティを構成
するようになつている。
In the method of the present invention, a mold release agent solution injected onto a mold is collected and introduced into a separation tank, and impurities such as oil are separated and removed from the solution in this separation tank, and the solution is passed through a coarse filter. After passing through the furnace, it is introduced into a storage tank,
The concentration of the solution in this storage tank is measured, a diluted solution or a stock solution is added to set the solution to a predetermined concentration, and this solution is injected into the mold. Next, one embodiment of the present invention will be described with reference to the accompanying drawings.
In the figure, 1 is a casting section, and this casting section 1 is provided with a die 4 consisting of a fixed die 2 and a movable die 3. The movable die 3 is a die consisting of a cylinder, a pump, piping, etc. It is moved forward and backward relative to the fixed mold 2 by a movable mechanism 5, and the respective mold surfaces 6 and 7 form a cavity during mold matching.

また上記鋳造部1において、上記金型4および金型可動
機構5の下部に回収槽8が設けられている。
Further, in the casting section 1, a recovery tank 8 is provided below the mold 4 and the mold movable mechanism 5.

つぎに、上記回収糟8の底部に凹部9が形成され、この
凹部9に運通路10の一様部が運遠されているとともに
、この運通路10の池端部に分離糟としての第1の分離
槽11が蓮通されている。
Next, a recess 9 is formed at the bottom of the collection waste 8, and a uniform portion of a transport path 10 is conveyed through the recess 9, and a first recess serving as a separation waste is formed at the end of the transport path 10. The separation tank 11 is filled with water.

この第1の分離槽11内には、所定の間隔をおいて流れ
方向に高さを少しずつ低くした複数の仕切壁12,13
が底板14上に立設され、この各仕切壁12,13の一
側部にそれぞれ下端を関口した案内板15,16によっ
て排出路17,18が形成され、この各排出路17,1
8の上端部にオーバフロー用の排出口部17a,18a
が流れ方向に折曲して形成されている。また上記各仕切
壁12,13間の上端に、すなわち、上記各排出口部1
7a,18aの位置とほぼ同一高さ位置に油などの浮遊
する不純物を排出する排出路20,21,22が形成さ
れ、この各排出路20,21,22は導通路23,24
,25を介して廃気処理糟26に蓮速されている。また
上記第1の分離槽11の排出路11を有する部分にポン
プ27が設けられ、このポンプ27に接続した導管28
を介して第1の分離槽11に分離槽としての第2の分離
槽29が運速されている。この第2の分離槽29内には
、所定の間隔をおいて複数の仕切盛30,31が底板3
2上に立設され、この各仕切壁30,31の一側部に下
端を閉口したそれぞれ案内板33,34によって排出路
35,36が形成され、この各排出路35,36の上端
部にオーバフロー用の排出口部35a,36aが形成さ
れている。また上記各仕切壁30,31間の上部にすな
わち、上記各排出口部35a,36aの位置とほぼ同一
高さ位置に油などの浮遊する不純物19を排出する排出
路37,38が形成され、この各排出路37,38は運
通路39を介して上記第1の分離槽11の最初の分離部
に帰還され再処理されるようになっている。つぎに、上
記第2の分離槽29の流れ方向の側壁の外側上部に支枠
40が突設され、この支枠40にたとえばスポンジなど
からなる複数のフィル夕41が上下に重積して着脱自在
に取付けられている。
Inside this first separation tank 11, there are a plurality of partition walls 12, 13 whose heights are gradually lowered in the flow direction at predetermined intervals.
are erected on the bottom plate 14, and discharge passages 17, 18 are formed by guide plates 15, 16 whose lower ends are connected to one side of each of the partition walls 12, 13, respectively.
Overflow outlet portions 17a and 18a are provided at the upper end of 8.
is bent in the flow direction. Moreover, at the upper end between each of the partition walls 12 and 13, that is, each of the discharge ports 1
Discharge passages 20, 21, 22 for discharging floating impurities such as oil are formed at positions approximately at the same height as positions 7a, 18a, and these discharge passages 20, 21, 22 are connected to conductive passages 23, 24.
, 25 to an exhaust gas treatment tank 26. Further, a pump 27 is provided in a portion of the first separation tank 11 having the discharge path 11, and a conduit 28 connected to the pump 27 is provided.
A second separation tank 29 serving as a separation tank is conveyed to the first separation tank 11 via the first separation tank 11 . Inside this second separation tank 29, a plurality of partition plates 30, 31 are arranged at predetermined intervals on the bottom plate 3.
Discharge passages 35 and 36 are formed by guide plates 33 and 34, respectively, which are installed upright on the partition walls 30 and 31 and whose lower ends are closed at one side of each of the partition walls 30 and 31. Exhaust ports 35a and 36a for overflow are formed. In addition, discharge passages 37 and 38 for discharging floating impurities 19 such as oil are formed at the upper part between the partition walls 30 and 31, that is, at substantially the same height as the positions of the discharge ports 35a and 36a, These discharge passages 37 and 38 are returned to the first separation section of the first separation tank 11 via a transportation passage 39 for reprocessing. Next, a supporting frame 40 is protruded from the upper outer side wall of the second separation tank 29 in the flow direction, and a plurality of filters 41 made of, for example, sponge are stacked vertically on this supporting frame 40 and can be attached and removed. Can be installed freely.

この上下に配置した各フィル夕41は下方に至るにつれ
次第に細いメッシュのものが採用されている。しかして
、フィル夕41としては、ポーラス耐火物、ポーラス金
属板、スポンジ、炉紙などを用いる。つぎに、上記フィ
ル夕41の下部に位置して貯留槽としての貯留調整槽4
2が設けられている。
Each of the filters 41 disposed above and below has a mesh that becomes gradually thinner toward the bottom. As the filter 41, porous refractories, porous metal plates, sponges, furnace paper, etc. are used. Next, a storage adjustment tank 4 is located below the filter 41 and serves as a storage tank.
2 is provided.

この貯留調整槽42内には、溶液の濃度を側定する測定
装置が設けられ、この測定装置43に接続された濃度計
44にリレー45が接続され、このリレー45に上記貯
留調整槽42に原液または希釈溶液を供V給する原液供
V給装置としてのポンプ46が導線47を介して接続さ
れ、このポンプ46は原液槽48内に設けられていると
ともに、このポンプ46に接続された導管49の吐出口
50が上記貯留調整槽42に臨ませて閉口されている。
また上記貯留調整槽42内にポンプ51が設けられ、こ
のポンプ51に導管52を介して溶液槽53が接続され
ている。この溶液槽53内には離型剤の原液槽54と希
釈液槽55が設けられ、この希釈液槽55に希釈液を導
入する導管56が接続されているとともに、この導管5
6の途中にバルブ57および導管58を介して上記原液
槽54が運速されている。そして、上記原液槽54の原
液は、上記希釈液槽55内において所定の倍率で自動的
に希釈化されて磯型剤の溶液aとして溶液槽53に後続
された吐出管59およびその吐出管59の先端部に取付
けられたノズル60から上記金型4に噴射されるように
なっている。このように構成されたものにおいて、溶液
槽53においてアルミニュム及び亜鉛ダイカスト用の水
溶性のェマルジョンタィプの雛型剤の原液が希釈水によ
って所定の濃度に希釈化され、この溶液aは図示しない
駆動手段の駆動によって吐出管59で圧送されるととも
に、その先端部のノズル60から、金型4すなわち、固
定金型2と可動金型3の型面6,7に噴射され、この型
面6,7に溶液aからなる雛型被膜bが形成される。
A measuring device for determining the concentration of the solution is provided in this storage adjustment tank 42 , and a relay 45 is connected to a concentration meter 44 connected to this measuring device 43 . A pump 46 serving as a stock solution supply device for supplying stock solution or diluted solution is connected via a conductor 47, and this pump 46 is provided in a stock solution tank 48 and a conduit connected to this pump 46. 49 discharge ports 50 are closed facing the storage adjustment tank 42.
Further, a pump 51 is provided within the storage adjustment tank 42, and a solution tank 53 is connected to this pump 51 via a conduit 52. A release agent stock solution tank 54 and a diluted solution tank 55 are provided in this solution tank 53, and a conduit 56 for introducing a diluted solution is connected to this diluted solution tank 55.
6, the stock solution tank 54 is transported through a valve 57 and a conduit 58. The undiluted solution in the undiluted solution tank 54 is automatically diluted at a predetermined ratio in the diluted solution tank 55, and the discharge pipe 59 is connected to the solution tank 53 as a solution a of the rock molding agent. The liquid is sprayed into the mold 4 from a nozzle 60 attached to the tip of the metal mold 4. In this structure, a stock solution of a water-soluble emulsion type template agent for aluminum and zinc die casting is diluted to a predetermined concentration with dilution water in the solution tank 53, and this solution a Driven by the means, the liquid is pumped through the discharge pipe 59, and is injected from the nozzle 60 at the tip onto the mold surfaces 6, 7 of the mold 4, that is, the fixed mold 2 and the movable mold 3. A template film b made of solution a is formed on 7.

つぎに、上記型面6,7に噴射された余分な溶液aは金
型4から回収槽8内に回収されるとともに、この回収槽
8内に金型4の冷却水、金型可動機構5の作動油、チッ
プおよび潤滑油などの不純物cが回収される。
Next, the excess solution a sprayed onto the mold surfaces 6 and 7 is collected from the mold 4 into a collection tank 8, and cooling water for the mold 4 and mold movable mechanism 5 are collected in the collection tank 8. Impurities c such as hydraulic oil, chips and lubricating oil are recovered.

そして、この回収槽8内に回収された不純物cを含む溶
液aは、運通路1川こよって第1の分離糟11の最初の
分離部内に導入されるとともに、各排出路17,18か
ら順次オーバフローされつつ最後の分離部に流入される
。この際、第1の分離槽11内には各排出路17,18
に近接して各分離部毎にオーバフローする高さで排出路
20,21,22が形成されているので、順次流入する
溶液aに浮遊する油などの不純物cは、順次排出路20
,21,22内にオーバフローされて溶液aから分離除
去されるとともに、これが導通路23,24,25を介
して廃棄処理槽26内に捕捉処理される。そして、ポン
プ27の駆動により、第1の分離槽11内において不純
物cが分離された溶液aは、導管28を介して第2の分
離槽29の最初の分離部内に導入されるとともに、各排
出路35,36から順次オーバフロ−されつつ最後の分
離部に流入される。
The solution a containing impurities c collected in the collection tank 8 is introduced into the first separation section of the first separation tank 11 through one transportation path, and is sequentially introduced from each discharge path 17, 18. It is overflowed and flows into the final separation section. At this time, each discharge path 17, 18 is provided in the first separation tank 11.
Since the discharge passages 20, 21, and 22 are formed at a height such that they overflow in each separation section, impurities c such as oil floating in the solution a that sequentially flows into the discharge passage 20.
, 21, 22 and is separated and removed from solution a, and is captured and treated in a waste treatment tank 26 via conduction paths 23, 24, 25. Then, by driving the pump 27, the solution a from which impurities c have been separated in the first separation tank 11 is introduced into the first separation section of the second separation tank 29 via the conduit 28, and each discharge The water is sequentially overflowed from channels 35 and 36 and flows into the final separating section.

この際、順次流入する溶液aに浮遊する油などの不純物
cは、順次排出路37,38内にオーバフローされて溶
液aからさらに分離除去されるとともに、これが蓮通路
39を介して上記第1の分離槽11内に帰戻しされ順次
廃棄処理槽26内に捕捉処理される。ついで、溶液aは
、第2の分離槽29からオーバフローされてフィル夕4
1上に流入され、このフィル夕41によってさらに炉週
され、塵挨、油、粕士、カーボンなどが除去されて貯留
調整槽42内に導入される。
At this time, impurities c such as oil floating in the solution a that sequentially flows in are sequentially overflowed into the discharge passages 37 and 38 and are further separated and removed from the solution a. The waste is returned to the separation tank 11 and sequentially captured and processed in the waste treatment tank 26. Next, the solution a overflows from the second separation tank 29 and enters the filter tank 4.
1 and further filtered by this filter 41 to remove dust, oil, lees, carbon, etc., and then introduced into the storage adjustment tank 42.

そして、この貯留調整槽42内において溶液aは測定装
置43によってその濃度が測定されるとともに、この測
定濃度が濃度計44で表示される一方で、溶液aが所定
の濃度に満たない場合にはリレー45が励磁されるとと
もに、ポンプ46が駆動され、このポンプ46によって
原液槽48内の雛型剤の原液または希釈液が導管49を
介して上記貯留調整槽42内に自動的に供給され、溶液
aの濃度が上記溶液槽53の溶液aの濃度と等しい所定
濃度に達するまで供給される。
In this storage adjustment tank 42, the concentration of solution a is measured by a measuring device 43, and this measured concentration is displayed on a concentration meter 44. However, if the concentration of solution a is less than a predetermined concentration, When the relay 45 is excited, the pump 46 is driven, and the pump 46 automatically supplies the stock solution or diluted solution of the model agent in the stock solution tank 48 into the storage adjustment tank 42 through the conduit 49, The solution a is supplied until the concentration reaches a predetermined concentration equal to the concentration of the solution a in the solution tank 53.

そうして溶液aが所定の濃度に達すると、これが測定装
置43によって測定され濃度計44に表示されるととも
に、リレー45が非励磁となりポンプ46の動作が停止
される。
When the solution a reaches a predetermined concentration, it is measured by the measuring device 43 and displayed on the concentration meter 44, and the relay 45 is de-energized and the operation of the pump 46 is stopped.

つぎに、貯留調整槽42内に設けたポンプ51が駆動さ
れると、調整設定された溶液aは導管52を介して溶液
槽53内に帰戻しされて再使用に供される。
Next, when the pump 51 provided in the storage adjustment tank 42 is driven, the adjusted solution a is returned to the solution tank 53 via the conduit 52 and is reused.

上記の場合、雛型剤の溶液の濃度は鋳造品などによって
自由に設定することができる。
In the above case, the concentration of the template agent solution can be freely set depending on the casting product.

またフィル夕41は着脱自在に取付けられているので、
掃除が容易であり、耐火物、ポ−ラス金属板の場合には
焼き、フポンジ、炉紙など場合は焼却路で焼却するよう
にするとよい。
Also, since the filter 41 is removably attached,
Cleaning is easy, and if the material is made of refractories or porous metal plates, it is best to burn it, or if it is made of foam or paper, it is best to incinerate it in an incineration path.

本発明によれば、金型に噴射した離型剤の溶液を回収し
て分離槽内において溶液から作動油などの不純物を除去
して浄化するとともに、この溶液の濃度を金型に噴射す
る溶液の濃度と同等に設定して金型に噴射することによ
り、雛型剤は循環されつつ金型に附着する必要量ずつ消
費され全体として無駄なく有効に消費することができる
ので経済的である。
According to the present invention, a solution of a mold release agent injected onto a mold is recovered and purified by removing impurities such as hydraulic oil from the solution in a separation tank, and the concentration of this solution is changed to a solution injected into a mold. By injecting the template agent into the mold at a concentration equivalent to that of the template agent, the template agent is circulated and consumed in the necessary amount that adheres to the mold, and can be consumed effectively as a whole without waste, which is economical.

また金型に噴射したのちこれを工場廃液として直ちに排
出されないので環境を汚染するなど公害問題が生じるこ
とがなく、かつまた後処理が容易であり、したがって生
産性に寄与すること極めて大である。また金型に噴射し
た溶液は、回収して分離槽およびフィル夕に順次かける
ことにより、溶液に混在する油などの不純物は順次分離
除去され、したがって溶液を確実に浄化することができ
る。
Furthermore, since it is not immediately discharged as factory waste after being injected into the mold, it does not cause pollution problems such as contaminating the environment, and post-treatment is easy, so it greatly contributes to productivity. Furthermore, by collecting the solution injected into the mold and sequentially applying it to a separation tank and a filter, impurities such as oil mixed in the solution are successively separated and removed, and therefore the solution can be reliably purified.

また浄化した溶液が所定の濃度に満たない場合にはこれ
に原液または希釈液を自動的に供総合して所定の濃度に
設定することにより、溶液の濃度管理が確実で適正な濃
度の溶液として十分再使用に供することができる。
In addition, if the purified solution does not reach a predetermined concentration, the stock solution or diluted solution is automatically added to it and the concentration is set to the predetermined concentration, ensuring reliable solution concentration control and ensuring that the solution has an appropriate concentration. It can be fully reused.

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

図は本発明の離型剤方法を実施する装置の一実施例を示
す説明図である。 4・・・金型、11,29・・・分離槽、26・・・廃
棄処理槽、41…フィル夕、42・・・貯留調整槽、4
3・・・測定菱贋、46…原液供給装置としてのポンプ
、a・・・離型剤の溶液。
The figure is an explanatory view showing one embodiment of an apparatus for carrying out the mold release agent method of the present invention. 4... Mold, 11, 29... Separation tank, 26... Waste treatment tank, 41... Filter tank, 42... Storage adjustment tank, 4
3...Measurement counterfeit, 46...Pump as stock solution supply device, a... Solution of mold release agent.

Claims (1)

【特許請求の範囲】[Claims] 1 金型に噴射した離型剤溶液を回収して分離槽内に導
入し、この分離槽内おいて溶液から油などの不純物を分
離除去するとともに、この溶液をさらフイルタにかけて
濾過したのちこれを貯留槽内に導入し、この貯留槽内の
溶液の濃度を測定して希釈溶液または原液を加えて溶液
を所定の濃度に設定するとともに、この溶液を上記金型
に噴射するようにしたことを特徴とする離型剤処理方法
1 The mold release agent solution injected into the mold is collected and introduced into a separation tank, and impurities such as oil are separated and removed from the solution in this separation tank, and the solution is further filtered through a filter. The solution is introduced into a storage tank, the concentration of the solution in this storage tank is measured, and a diluted solution or stock solution is added to set the solution to a predetermined concentration, and this solution is injected into the mold. Characteristic mold release agent treatment method.
JP55137899A 1980-10-02 1980-10-02 Mold release agent treatment method Expired JPS6033549B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP55137899A JPS6033549B2 (en) 1980-10-02 1980-10-02 Mold release agent treatment method

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP55137899A JPS6033549B2 (en) 1980-10-02 1980-10-02 Mold release agent treatment method

Related Child Applications (1)

Application Number Title Priority Date Filing Date
JP4987385A Division JPS60221148A (en) 1985-03-13 1985-03-13 Device for controlling concentration of mold releasing agent

Publications (2)

Publication Number Publication Date
JPS5762836A JPS5762836A (en) 1982-04-16
JPS6033549B2 true JPS6033549B2 (en) 1985-08-03

Family

ID=15209273

Family Applications (1)

Application Number Title Priority Date Filing Date
JP55137899A Expired JPS6033549B2 (en) 1980-10-02 1980-10-02 Mold release agent treatment method

Country Status (1)

Country Link
JP (1) JPS6033549B2 (en)

Families Citing this family (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS59206138A (en) * 1983-05-07 1984-11-21 Toshiba Mach Co Ltd Automatic concentration adjuster for mold coating material
JPS60221148A (en) * 1985-03-13 1985-11-05 Tokyo Rika Kogyosho:Kk Device for controlling concentration of mold releasing agent
JP2007175752A (en) * 2005-12-28 2007-07-12 Hanshin Tec Kk Apparatus for regenerating release agent
JP2009028751A (en) * 2007-07-26 2009-02-12 Daito Kogyo Kk Release agent regeneration system
JP5698638B2 (en) * 2011-09-27 2015-04-08 富士フイルム株式会社 Liquid applicator and ink jet recording apparatus
CN114890573B (en) * 2022-04-25 2023-10-24 维苏威铸造科技(江苏)有限公司 Environment-friendly recycling process for casting coating cleaning waste

Family Cites Families (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5932228B2 (en) * 1974-02-15 1984-08-07 ハナノシヨウジ カブシキガイシヤ How to spray mold release agent
JPS5112950U (en) * 1974-07-16 1976-01-30
JPS52120162A (en) * 1976-03-30 1977-10-08 Kuraray Co Method of producing fibrous highhprotein food
JPS5516199A (en) * 1978-07-13 1980-02-04 Fagersta Ab Metal product with sounddattenuating element

Also Published As

Publication number Publication date
JPS5762836A (en) 1982-04-16

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