JPS6157106B2 - - Google Patents
Info
- Publication number
- JPS6157106B2 JPS6157106B2 JP7709883A JP7709883A JPS6157106B2 JP S6157106 B2 JPS6157106 B2 JP S6157106B2 JP 7709883 A JP7709883 A JP 7709883A JP 7709883 A JP7709883 A JP 7709883A JP S6157106 B2 JPS6157106 B2 JP S6157106B2
- Authority
- JP
- Japan
- Prior art keywords
- mold
- molten metal
- casting
- graphite spheroidizing
- sand mold
- 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
Links
- 239000002184 metal Substances 0.000 claims description 29
- 229910052751 metal Inorganic materials 0.000 claims description 29
- 238000000034 method Methods 0.000 claims description 22
- 238000005266 casting Methods 0.000 claims description 19
- 238000006243 chemical reaction Methods 0.000 claims description 18
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims description 17
- 229910002804 graphite Inorganic materials 0.000 claims description 17
- 239000010439 graphite Substances 0.000 claims description 17
- 239000004576 sand Substances 0.000 claims description 15
- 239000003795 chemical substances by application Substances 0.000 claims description 11
- 229910001141 Ductile iron Inorganic materials 0.000 claims description 5
- 238000004519 manufacturing process Methods 0.000 claims description 5
- 238000005204 segregation Methods 0.000 claims description 4
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 4
- 239000000203 mixture Substances 0.000 claims description 2
- 230000008569 process Effects 0.000 claims description 2
- 239000007787 solid Substances 0.000 claims 5
- 229910000861 Mg alloy Inorganic materials 0.000 description 16
- 239000000843 powder Substances 0.000 description 4
- 239000002245 particle Substances 0.000 description 3
- 230000009257 reactivity Effects 0.000 description 3
- 238000010301 surface-oxidation reaction Methods 0.000 description 3
- 239000011230 binding agent Substances 0.000 description 2
- 230000007547 defect Effects 0.000 description 2
- 239000010419 fine particle Substances 0.000 description 2
- 238000010438 heat treatment Methods 0.000 description 2
- 238000009434 installation Methods 0.000 description 2
- 150000001247 metal acetylides Chemical class 0.000 description 2
- 239000003607 modifier Substances 0.000 description 2
- 229910001018 Cast iron Inorganic materials 0.000 description 1
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 description 1
- 229920002472 Starch Polymers 0.000 description 1
- 229910045601 alloy Inorganic materials 0.000 description 1
- 239000000956 alloy Substances 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 229910052802 copper Inorganic materials 0.000 description 1
- 239000010949 copper Substances 0.000 description 1
- 230000003111 delayed effect Effects 0.000 description 1
- 230000006866 deterioration Effects 0.000 description 1
- 238000011038 discontinuous diafiltration by volume reduction Methods 0.000 description 1
- 239000000428 dust Substances 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 239000003292 glue Substances 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- 239000011261 inert gas Substances 0.000 description 1
- 238000002347 injection Methods 0.000 description 1
- 239000007924 injection Substances 0.000 description 1
- 238000007689 inspection Methods 0.000 description 1
- 235000000396 iron Nutrition 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 230000007246 mechanism Effects 0.000 description 1
- 239000000155 melt Substances 0.000 description 1
- 230000002093 peripheral effect Effects 0.000 description 1
- 235000019353 potassium silicate Nutrition 0.000 description 1
- 238000010791 quenching Methods 0.000 description 1
- 230000000171 quenching effect Effects 0.000 description 1
- 238000010992 reflux Methods 0.000 description 1
- 239000011347 resin Substances 0.000 description 1
- 229920005989 resin Polymers 0.000 description 1
- 230000004044 response Effects 0.000 description 1
- 238000009991 scouring Methods 0.000 description 1
- NTHWMYGWWRZVTN-UHFFFAOYSA-N sodium silicate Chemical compound [Na+].[Na+].[O-][Si]([O-])=O NTHWMYGWWRZVTN-UHFFFAOYSA-N 0.000 description 1
- 229910000679 solder Inorganic materials 0.000 description 1
- 238000007711 solidification Methods 0.000 description 1
- 230000008023 solidification Effects 0.000 description 1
- 235000019698 starch Nutrition 0.000 description 1
- 239000008107 starch Substances 0.000 description 1
- 238000003860 storage Methods 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B22—CASTING; POWDER METALLURGY
- B22D—CASTING OF METALS; CASTING OF OTHER SUBSTANCES BY THE SAME PROCESSES OR DEVICES
- B22D1/00—Treatment of fused masses in the ladle or the supply runners before casting
- B22D1/007—Treatment of the fused masses in the supply runners
Landscapes
- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- Refinement Of Pig-Iron, Manufacture Of Cast Iron, And Steel Manufacture Other Than In Revolving Furnaces (AREA)
Description
【発明の詳細な説明】
ダクタイル鋳鉄の製造に於いて、極めて激しく
反応し燃焼し易いMgを合金化し、取鍋にて球状
化処理してMgの歩留りを高めたり、又密閉され
た高圧容器内でMgを添加することによつてMgの
歩留りを高め節約するなどの数多くの方法が知ら
れており枚挙に暇がない程であるが、その内で
も、最近、インモールド法と称する型内球状化方
法が種々研究されるようになつてきた。
この型内球状化法は、特公昭46―16260に示さ
れるように特別に設けた反応室と垢こしの機能を
備えた鋳造方案よりなつており(図1参照)、こ
こに粒粉状に破砕した球状化剤を置くことによ
り、成分調整をされたダクタイル鋳鉄の元湯を注
入することによつて型内で球状化剤と接触せしめ
てダクタイル鋳物を製造する方法が知られている
が、この先行技術は、特公昭57―21004にも示さ
れるように比重の軽いMg合金の溶湯流による流
されの現象が起るために、反応室の体積を充分大
きく取るとか、発生する流された粒子や酸化物の
除去のための垢こし方法を充分に大きく取る必要
があつたために鋳造方案歩留りが取鍋にてMg処
理された溶湯を注入してつくるダクタイル鋳物に
比べ悪いという欠点があつた。
しかし、この型内で球状化処理をするという方
法は、取鍋でMg処理された溶湯を鋳込む方法に
比べ数々の優れた特徴を持つ。それは、Mgが時
間と共に消失するという、所謂、フエデング―現
象を全く考慮しなくてもよいという点であり、黒
鉛粒数の多い炭化物のない鋳物をつくり得るとい
う点であり、高価なMg合金の歩留りが高いとい
う点であつた。
しかし、この初めて開発された先行技術は、前
述のようにMg合金として3m/m以下程度の微
粒子を用いるため浮され、流され易いという欠点
があり、更には、このように表面面積率の大きい
微粒子を用いるために通常用いられる生砂型造型
ラインと称される、水分を2〜6%含有する砂型
ラインでの使用に当つては微粒子状Mg合金を設
置してから注湯する迄の時間的な制約もあつた。
何故なら、これらの砂型は繰返し用いられるた
めある程度の熱を有しており造型された生砂型内
は水蒸気があり、あらかじめ挿入されている表面
面積率の大きい活性なMg微粒子を酸化させる恐
れがあるために一昼夜も放置するようなことは推
奨されなかつた。
即ち、微粒子状のMg合金を用いることによる
浮遊して流されたものによつて起因するノロかみ
欠陥や部分的にMgやSiの偏析によつて起る欠
陥、粒子状のための見掛け体積の増大による反応
室の増大によるものと垢とり機構の複雑化に伴う
鋳造方案歩留りの減少、生砂型内の表面酸化の可
能性及び合金破砕及び貯蔵時の取扱いの問題等が
あつた。又更に、特公昭46―16260に示されてい
るようにMg合金からなる球状化剤を粉砕してか
ら固め、又は押出し圧縮した成型物として一体化
して用いる、とも記されているが極めて活性な
Mg合金を粉末状にしたる後、樹脂、水ガラス、
でん粉による糊、有機バインダー、無機バインダ
ーによるものなどのあらゆる方法で固めても発明
者らの研究によると、表面酸化のため全く溶け
ず、これはある不活性ガスの雰囲気中で粉砕をし
ても、固める過程で表面酸化してしまい実用性は
全くない。なお、ワツクスと称される鑞で固めた
ものは見た目には溶けるが、所謂、バラケルとい
う現象であり表面より徐々に溶けるという現象で
はない。
このため球状化Mg合金を粉末にしたるのち、
何等かの方法で固めて用いる方法は一切実用化さ
れていない。
かゝる粒子状Mg合金を用いる型内ダクタイル
鋳鉄の製造方法の欠点を修正したものとして、特
公昭57―21004に示される一体化改質剤を使用
する球状化処理が出されているが(図2参照)こ
れとても次の様な完全でない点を有していた。
処理されるべき溶湯が接触する凹部に嵌め込ま
れた鋳造された球状化剤の上部は鋳型において冷
硬化されているために薄いながらも酸化皮膜を有
していることは避けられない点であり、このこと
は金型、黒鉛型、水冷銅金型その他あらゆる鋳型
にて鋳造してもその表面は必ず酸化皮膜を有して
いることは、Fe―SiやFe―Si―Ca,Fe―Si―
Mg―Ca―REなどの鋳造に於いては周知のこと
であつた。
又、この凹部に嵌合して置かれる鋳造されて冷
硬化された球状化剤の表面を処理されるべき溶湯
が流れることによつて含有されているMgと溶湯
が反応することによつて型内で球状化黒鉛鋳鉄を
得ようとするものであつたが表面酸化皮膜のため
に一瞬反応が遅れることが判明している。又更に
鋳造され、冷硬化された該球状化ブロツクは注入
された溶湯によつて予熱され本格的な反応を開始
する迄にある程度の時間的な余裕が必要なことも
判明している。
以上の2点は、この型内球状化方法を実施する
のに際して決定的な欠陥要因となつていた。
即ち、最近の自動注湯ラインや取鍋注湯に於い
ても能率向上のため、その注湯時間は従来13〜20
秒程度のものが4〜10秒程度へと短縮されてきて
いる。このことは注入された溶湯の最初に通過し
た溶湯はMgとの反応が充分に行われないことを
意味し、このために型内に於いて黒鉛が球化され
た所や、充分に球化されない所などが生じるため
に信頼性に欠け、1枠毎の検査を必要としたた
め、我国に於いては実用化されていない。
本発明はこの注入されたごく初期の溶湯に対し
ても完全に均一にMg反応が保証できるようなシ
ステムを提供するものである。
本発明に従つてその詳細を記すると(図3参
照)砂型内湯口直下凹部に嵌合され設置され鋳
造されつくられた黒鉛球状化Mg合金ブロツク
の上部は平滑なる鋳造面ではなく、必ず凹凸のあ
る常温破断面となした鋳造ブロツクを設置する
ことからなつており、更に、該鋳造ブロツクの
内部のMg濃度を外周部より外周部より意識的
に高くして反応性を高める工夫をしたものであ
る。この内部へのMgの偏析は急にMg濃度が高く
なるのではなく、徐々に外周部より高くなるよう
にしてつくられる。
このようにしなければならない理由は、次の通
りである。
Mg濃度を中芯部に於いて高くしたのは、通常
型内で用いられる黒鉛球状化用Mg合金は、6%
Mg程度が好適とされる。しかし、前述のような
理由で6%であり、且、表面が冷硬なる型に面し
て表面酸化層のあるブロツクでは瞬間的に流れる
初期溶湯を球状化さすには反応性が低すぎるので
ある。
発明者らの研究によれば、Mgは8%以上が、
初期溶湯については必要である。
しかし、鋳造ブロツクの全体のMg濃度を8%
以上としたのでは該型内に於いての反応が初期溶
湯が通過してから本格的な反応が始まつた場合、
強すぎることになり反応蒸気の型外への吹き出し
や型内での沸騰などが起りよくないので意識的に
中心部にMgを高く偏在せしめ全体としては、Mg
を高くしなくても初期溶湯のMg反応に充分の保
証を与えるというのでこの点が、特公昭57―
21004に示される均質なMgの偏析のない溶湯接触
面が冷硬化された一体改質剤を用いる方法とは根
本的に技術的思想が異なるのである。
更に、本発明の場合は常温に於いて必ず溶湯と
の接触面を破砕して全く酸化皮膜のない面を露
出させることと破砕による凹凸面を出すことに
よつても初期反応への即応性と反応面積の増大を
計つているのである。
本発明に用いるMgを中心部に偏析させたこれ
らのMg合金ブロツクは、鋳型を高周波熱源で加
熱しつゝ鋳込むとか、鋳型外周を充分に予熱せし
めた鋳型を用いることによつて容易に手に入れる
ことができる。このように、
Mgの中心濃度を高める。
溶湯接触面を常温破断面とする。
溶湯接触面に凹凸をつけ反応面積の増大を計
る。
等のことにより注入速度の極めて速い高速短時間
鋳込みの場合の型内球化の方法に於いても初期溶
湯のMg反応の確実なる保証の故に従来のように
初期溶湯のMg含有の不確実性のために、初期溶
湯をオーバーフローさせて無駄にする、所謂、は
かせ湯や型内還流させる等の鋳造方案歩留りの悪
化につながるようなことをする必要がなくなつ
た、等の鋳造方案歩留りの向上の他に、先行鋳込
部位や鋳込み最終部位などの球状化程度のバラツ
キのない鋳物の製造を確実に提供するものであ
る。なお、本法は、取鍋にてRE処理やMg処理さ
れた不完全なる球状化処理溶湯を完全に球状化処
理をするためにも用いることもできるなど、工業
的応用範囲は極めて広い方法である。
次に実施例を示す。
実施例
図4に示すような砂型で反応室の大きさ、巾、
46mm長さ、46mm深さ、1は30mm、2と3は20m/
mの反応室をつくり、これに300Kg高周波炉で
溶製したC.3.7%,Si.2.4%,Mn.0.3%,P.0.035
%,S.0.015%,からなるダクタイル元湯をそれ
ぞれ次のような方法で型内球状化処理してそれぞ
れの製品部の異物噛み込み状況と球状化状況を調
査した。なお、砂型内の鋳込みダクタイル元湯の
容量は15Kgとなつている。
1 Mg.6.5%,Ca.0.8%,RE.1.5%,Si.46%か
らなるMg合金の2m/m以下粉末を0.8%120
gを反応室に入れ、これに前述の溶湯15Kgを4
秒で鋳込んだ。
2 Mg.6.7%,Ca.0.8%,RE.1.4%,Si.45%か
らなるMg合金を、巾4.5cm×4.5cm、高さ17mm
の上下面急冷硬金型にて鋳造したものをセツト
して前述の溶湯15Kgを同じく4秒で鋳込んだ。
3 急冷して分析すれば、Mg.6.5%,Ca.0.7%,
RE.1.4%,Si.46%からなるMg合金を、巾.
4.5cm×4.5cm、高さ.17mmの黒鉛鋳型に鋳込む
に際して該黒鉛鋳型の外側に巻いた高周波加熱
装置で加熱しながら凝固させ、中芯部の成分が
Mg.8.9%,Ca.0.9%,RE.1.4%,Si.45%,外
周部の成分がMg.5.6%,Ca.0.6%,RE.1.4%,
Si.46%からなる凝固後上部を常温破断してつ
くつたブロツクをセツトして前述の溶湯15Kgを
同じく4秒で鋳込んだ。
結果は、図4に示すNo.1〜No.11までの部位を
顕微鏡にて球状化率と未溶解物及び酸化物の捲
き込み状況を調査した表1のとおりであつた。
【表】[Detailed Description of the Invention] In the production of ductile cast iron, Mg, which reacts extremely violently and is easily combustible, is alloyed and spheroidized in a ladle to increase the yield of Mg, or in a sealed high-pressure container. There are many known methods for increasing the yield and saving Mg by adding Mg, and there is too much time to list them. Various methods have been studied. This in-mold spheroidization method consists of a casting method equipped with a specially prepared reaction chamber and straining function, as shown in Japanese Patent Publication No. 46-16260 (see Figure 1), in which granular powder is formed. There is a known method for manufacturing ductile castings by placing a crushed spheroidizing agent into contact with the spheroidizing agent in a mold by injecting a base water of ductile cast iron whose composition has been adjusted. In this prior art, as shown in Japanese Patent Publication No. 57-21004, the phenomenon of flowing away due to the flow of molten Mg alloy with light specific gravity occurs, so the volume of the reaction chamber is made sufficiently large, and the flowing out that occurs occurs. Because it was necessary to use a sufficiently large scouring method to remove particles and oxides, the casting method had a disadvantage in that the yield was lower than that of ductile casting, which is made by pouring Mg-treated molten metal in a ladle. . However, this method of spheroidizing in a mold has many advantages over the method of casting Mg-treated molten metal in a ladle. This means that there is no need to take into account the so-called "fedeng" phenomenon, in which Mg disappears over time, and that it is possible to create castings with a large number of graphite grains and no carbides, and it is possible to make cast irons with a large number of graphite grains without carbides. The point was that the yield was high. However, as mentioned above, this first developed prior art technology uses fine particles of about 3 m/m or less as the Mg alloy, so it has the disadvantage of being easily floated and washed away. When using a sand mold line containing 2 to 6% moisture, which is commonly used to use fine particles and is called a green sand mold making line, the time required from installing the fine particulate Mg alloy to pouring the mold is There were also some restrictions. This is because these sand molds are used repeatedly, so they have a certain amount of heat, and there is water vapor inside the molded green sand mold, which may oxidize the active Mg particles with a large surface area ratio that have been inserted in advance. Therefore, it was not recommended to leave it for a day or night. In other words, by using fine particulate Mg alloys, there are slosh defects caused by suspended particles, defects partially caused by segregation of Mg and Si, and apparent volume reduction due to particulates. There were problems such as a decrease in the casting method yield due to the increase in the reaction chamber and the complexity of the dust removal mechanism, the possibility of surface oxidation in the green sand mold, and problems with alloy crushing and handling during storage. Furthermore, as shown in Japanese Patent Publication No. 46-16260, it is stated that a spheroidizing agent made of Mg alloy is crushed and then solidified, or it is extruded and compressed and used as an integrated molded product, but it is extremely active.
After turning Mg alloy into powder, it is processed into resin, water glass,
According to the research of the inventors, even if it is hardened by various methods such as starch glue, organic binder, inorganic binder, etc., it does not dissolve at all due to surface oxidation, and this is because even if it is crushed in an inert gas atmosphere. The surface oxidizes during the hardening process, making it completely impractical. Note that wax, which is hardened with solder, may appear to melt, but this is a so-called phenomenon called "barakel" and does not mean that it gradually melts from the surface. For this reason, after turning the spheroidized Mg alloy into powder,
No method of solidifying it in any way has been put to practical use. In order to correct the drawbacks of the manufacturing method of in-mold ductile cast iron using such a particulate Mg alloy, a spheroidizing treatment using an integrated modifier as shown in Japanese Patent Publication No. 57-21004 has been proposed ( (See Figure 2) This had the following imperfections. It is inevitable that the upper part of the cast spheroidizing agent fitted into the recess with which the molten metal to be treated comes into contact has a thin oxide film because it is cold hardened in the mold. This means that even when cast using a metal mold, graphite mold, water-cooled copper mold, or any other type of mold, the surface always has an oxide film.
This was well known in the casting of Mg-Ca-RE. In addition, when the molten metal to be treated flows over the surface of the cast and cold-hardened spheroidizing agent that is placed in the recess, the molten metal reacts with the Mg contained in the mold. The aim was to obtain spheroidized graphite cast iron within the reactor, but it was discovered that the reaction was momentarily delayed due to the surface oxide film. Furthermore, it has been found that a certain amount of time is required before the cast, cold-hardened spheroidized block is preheated by the injected molten metal and a full-scale reaction begins. The above two points were decisive flaws when implementing this in-mold spheroidization method. In other words, due to improved efficiency in recent automatic pouring lines and ladle pouring, the pouring time has traditionally been 13 to 20 minutes.
Time periods of about seconds have been shortened to about 4 to 10 seconds. This means that the first molten metal that passes through the injected metal does not react sufficiently with Mg, and as a result, in the mold, graphite may be spheroidized or not fully spheroidized. It has not been put into practical use in Japan because it is unreliable as there are places where it is not inspected, and it requires inspection for each frame. The present invention provides a system that can guarantee a completely uniform Mg reaction even in the very early stage of injected molten metal. To describe the details according to the present invention (see Fig. 3), the upper part of the graphite spheroidized Mg alloy block that is fitted into the recess directly below the sprue in the sand mold and cast is not a smooth casting surface, but always has an uneven surface. It consists of installing a cast block with a certain room-temperature fracture surface, and is also designed to increase reactivity by intentionally increasing the Mg concentration inside the cast block from the outer periphery. be. This segregation of Mg into the interior does not result in a sudden increase in the Mg concentration, but rather in such a way that it gradually becomes higher than in the outer periphery. The reason why this must be done is as follows. The Mg concentration in the central core was increased by 6% in the Mg alloy for graphite spheroidization used in normal molds.
It is said that Mg level is suitable. However, for the reasons mentioned above, the reactivity is 6%, and in a block with a surface oxidation layer facing the cold and hard mold, the reactivity is too low to make the instantaneous flowing initial molten metal into spheres. be. According to the inventors' research, more than 8% of Mg is
It is necessary for the initial molten metal. However, the overall Mg concentration of the cast block was reduced to 8%.
Based on the above, if the reaction in the mold starts after the initial molten metal has passed, then
If the strength is too strong, the reaction vapor may blow out of the mold or boil inside the mold, which is not good, so we consciously made Mg highly unevenly distributed in the center.
This point is said to provide sufficient guarantee for the Mg reaction in the initial molten metal without increasing the temperature.
The technical idea is fundamentally different from the method shown in 21004, which uses an integral modifier in which the molten metal contact surface is cold-hardened and has no homogeneous Mg segregation. Furthermore, in the case of the present invention, the surface in contact with the molten metal is always crushed at room temperature to expose a surface with no oxide film, and by creating an uneven surface by crushing, the rapid response to the initial reaction can be improved. The aim is to increase the reaction area. These Mg alloy blocks, in which Mg is segregated in the center, used in the present invention can be easily produced by heating the mold with a high-frequency heat source or by using a mold whose outer periphery is sufficiently preheated. can be put in. In this way, increasing the central concentration of Mg. The molten metal contact surface is a room-temperature fracture surface. The molten metal contact surface is made uneven to increase the reaction area. Due to the above reasons, even in the case of high-speed, short-time casting where the injection speed is extremely high, there is no uncertainty in the Mg content of the initial molten metal because the Mg reaction in the initial molten metal is guaranteed. Therefore, it is no longer necessary to overflow and waste the initial molten metal, so-called pouring, refluxing in the mold, etc., which can lead to deterioration of the casting method yield, and improve the casting method yield. In addition, it is possible to reliably produce a casting without variation in the degree of spheroidization in the preliminary casting region and the final casting region. This method can also be used to completely spheroidize molten metal that has undergone RE treatment or Mg treatment in a ladle, so it has an extremely wide range of industrial applications. be. Next, examples will be shown. Example: Using a sand mold as shown in Figure 4, the size and width of the reaction chamber,
46mm length, 46mm depth, 1 is 30mm, 2 and 3 are 20m/
A reaction chamber of m was made, and C.3.7%, Si.2.4%, Mn.0.3%, P.0.035 were melted in a 300Kg high-frequency furnace.
% and S.0.015% were each treated to form spheroids in the mold using the following method, and the state of foreign matter entrapment and spheroidization in each product part was investigated. The capacity of the cast ductile source water in the sand mold is 15 kg. 1 Mg alloy powder consisting of Mg.6.5%, Ca.0.8%, RE.1.5%, Si.46% less than 2m/m at 0.8%120
Put 4 g of the molten metal into the reaction chamber, and add 15 kg of the above-mentioned molten metal to it.
Cast in seconds. 2 Mg alloy consisting of Mg.6.7%, Ca.0.8%, RE.1.4%, Si.45%, width 4.5cm x 4.5cm, height 17mm
The above-mentioned molten metal (15 kg) was cast in the same 4 seconds by setting the cast material in the upper and lower quenching hard molds. 3 If analyzed after rapid cooling, Mg.6.5%, Ca.0.7%,
Width: Mg alloy consisting of RE.1.4% and Si.46%.
4.5cm x 4.5cm, height. When casting into a 17 mm graphite mold, the components in the core are solidified while being heated by a high-frequency heating device wrapped around the outside of the graphite mold.
Mg.8.9%, Ca.0.9%, RE.1.4%, Si.45%, outer peripheral components are Mg.5.6%, Ca.0.6%, RE.1.4%,
A block made by breaking the upper part at room temperature after solidification consisting of 46% Si was set, and 15 kg of the aforementioned molten metal was poured in the same 4 seconds. The results are as shown in Table 1, in which the spheroidization rate and the state of entrainment of undissolved matter and oxides were investigated using a microscope for the parts No. 1 to No. 11 shown in FIG. 【table】
第1図及び第2図は、先行技術にて用いる生砂
型内に於ける型内黒鉛球状化処理Mg合金の設置
状況を表わす湯口系の縦断面図。第3図は、本発
明にて用いる生砂型内に於ける型内黒鉛球状化処
理Mg合金の設置状況を表わす湯口系の縦断面
図。第4図は、本発明方法と比較のため、第1
図,第2図に示される先行技術と同じ湯口系にて
試験をした生砂型装置の中心断面立面図である。
FIGS. 1 and 2 are longitudinal sectional views of a sprue system showing the installation status of graphite spheroidized Mg alloy in a green sand mold used in the prior art. FIG. 3 is a longitudinal sectional view of the sprue system showing the installation status of the graphite nodularized Mg alloy in the green sand mold used in the present invention. Figure 4 shows the first method for comparison with the method of the present invention.
FIG. 2 is a central cross-sectional elevational view of a green sand mold device tested using the same sprue system as the prior art shown in FIGS.
Claims (1)
理を行う工程に使用する固型黒鉛球状化剤に於い
て、 砂型内に置かれる溶湯と接触する鋳造固型黒
鉛球状化剤の上部面の表面を鋳造面とせず、鋳
造後の常温破断面となすこと。 砂型内に置かれる溶湯と接触する鋳造固型黒
鉛球状化剤の上部面の表面を深い凹凸面となす
こと。 砂型内に置かれる溶湯と接触する鋳造固型黒
鉛球状化剤のMg濃度を外周部を低く、中芯部
のMg濃度が高いように偏析させること。 以上の〜のようにして鋳造されてつくつた
常温破断面露出で反応面に深い凹凸のある中芯部
にMgを高く偏析せしめた固型黒鉛球状化剤を砂
型内所定位置に置き、成分調整されたダクタイル
元湯を注入して型内にてダクタイル鋳鉄をつくる
方法。[Scope of Claims] 1. In the solid graphite spheroidizing agent used in the process of in-mold graphite spheroidizing treatment during the production of ductile cast iron, casting solid graphite spheroidizing agent that comes into contact with molten metal placed in a sand mold. The upper surface of the agent should not be the casting surface, but should be the room-temperature fracture surface after casting. The upper surface of the cast solid graphite spheroidizing agent that comes into contact with the molten metal placed in the sand mold is formed into a deeply uneven surface. To segregate the Mg concentration of the cast solid graphite spheroidizing agent that comes into contact with the molten metal placed in the sand mold so that the Mg concentration is low at the outer periphery and high at the central core. A solid graphite spheroidizing agent with a high segregation of Mg is placed in the sand mold at a predetermined position in the center core where the reaction surface has deep irregularities due to the room-temperature fracture surface exposed and the reaction surface is exposed as described in ~ above, and the composition is adjusted. A method of making ductile cast iron in a mold by injecting the ductile base water.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP7709883A JPS59202139A (en) | 1983-04-30 | 1983-04-30 | Treatment of cast iron |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP7709883A JPS59202139A (en) | 1983-04-30 | 1983-04-30 | Treatment of cast iron |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS59202139A JPS59202139A (en) | 1984-11-15 |
| JPS6157106B2 true JPS6157106B2 (en) | 1986-12-05 |
Family
ID=13624306
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP7709883A Granted JPS59202139A (en) | 1983-04-30 | 1983-04-30 | Treatment of cast iron |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS59202139A (en) |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH0591549U (en) * | 1991-04-26 | 1993-12-14 | 昌一 柴田 | Water catcher |
-
1983
- 1983-04-30 JP JP7709883A patent/JPS59202139A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS59202139A (en) | 1984-11-15 |
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