JP2000042706A - Premelting flux for centrifugal casting - Google Patents

Premelting flux for centrifugal casting

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Publication number
JP2000042706A
JP2000042706A JP10217793A JP21779398A JP2000042706A JP 2000042706 A JP2000042706 A JP 2000042706A JP 10217793 A JP10217793 A JP 10217793A JP 21779398 A JP21779398 A JP 21779398A JP 2000042706 A JP2000042706 A JP 2000042706A
Authority
JP
Japan
Prior art keywords
flux
casting
powder
molten metal
centrifugal casting
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
JP10217793A
Other languages
Japanese (ja)
Other versions
JP3748716B2 (en
Inventor
Minoru Ozaki
実 尾崎
Tomonori Kimura
友紀 木村
Masahiro Inui
正弘 乾
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.)
Kubota Corp
Original Assignee
Kubota Corp
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Filing date
Publication date
Application filed by Kubota Corp filed Critical Kubota Corp
Priority to JP21779398A priority Critical patent/JP3748716B2/en
Publication of JP2000042706A publication Critical patent/JP2000042706A/en
Application granted granted Critical
Publication of JP3748716B2 publication Critical patent/JP3748716B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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Abstract

PROBLEM TO BE SOLVED: To improve a molten slag-formation and feeder head and heat insulation effect of flux used for a centrifugal casting. SOLUTION: This flux is composed of powder obtd. by heating and melting the powder mixture containing each compound of silica, alumina, calcium carbonate, magnesium carbonate and calcium fluoride and executing the pulverizing treatment of this cooled solidified material. Desirably, this flux has the composition (by wt.%) composed of 25-30% SiO2, 2.5-3.5% Al2O3, 35-45% CaO, 4.5-5.5% MgO, 8-15% CaF2, 2-9% LiO2 and the balance FeO and MnO and 1.2-1.5 basicity [(CaO)/(SiO2+Al2O3)]. The grain size of this flux is adjusted to 20-200 mesh and the transportation property is secured without damaging good feeder head and heat insulation effect and the automation of charging the powder into the molten metal is easily achieved.

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明の属する技術分野】本発明は、遠心鋳造における
鋳型内の溶融金属の表面を被覆保護するフラックスの改
良に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an improved flux for coating and protecting the surface of a molten metal in a mold in centrifugal casting.

【0002】[0002]

【従来の技術】遠心鋳造において、鋳型内に注入された
溶融金属(溶湯)は、遠心力の作用で鋳型の内周面に沿
って層状に押し付けられ、その状態を保持したまま冷却
凝固して中空円筒状鋳造体(管体)を形成する。その鋳
造品質の改善・安定化を目的としてフラックスが使用さ
れている。鋳型内の溶湯に投与されたフラックスは、溶
湯の保有熱により溶融滓化して溶湯表面を被覆し、大気
の接触を遮断して溶湯の酸化を防止すると共に、溶湯に
対する押湯保温および清浄化(非金属介在物の吸収除
去)等の作用をなし、鋳造品質を高めることを可能にす
る。上記遠心鋳造用フラックスとして、珪砂(Si
2 ),アルミナ(Al2 3),炭酸カルシウム(C
aCO3 ),炭酸マグネシウム(MgCO3 ),弗化カ
ルシウム(CaF2 )、その他の化合物の粉末を、設定
塩基度に基づく配合量比で混合した粉末混合物(粒度:
約100 〜300 メッシュ)が使用されている。
2. Description of the Related Art In centrifugal casting, molten metal (molten metal) injected into a mold is pressed in layers along the inner peripheral surface of the mold by the action of centrifugal force, and cooled and solidified while maintaining that state. A hollow cylindrical casting (tube) is formed. Flux is used for the purpose of improving and stabilizing the casting quality. The flux applied to the molten metal in the mold becomes molten slag due to the retained heat of the molten metal, coats the surface of the molten metal, shuts off contact with the atmosphere to prevent oxidation of the molten metal, and keeps and cleans the hot water for the molten metal. (E.g., absorption and removal of non-metallic inclusions), thereby improving casting quality. Silica sand (Si
O 2 ), alumina (Al 2 O 3 ), calcium carbonate (C
ACO 3), magnesium carbonate (MgCO 3), calcium fluoride (CaF 2), a powder of other compounds, the powder mixture were mixed in the amounts ratio based on the setting basicity (particle size:
About 100-300 mesh) is used.

【0003】[0003]

【発明が解決しようとする課題】フラックスの溶湯被覆
効果をよりよく発揮させるには、投与されたフラックス
が速やかに溶解し良好な流動状態のもとに溶湯表面を一
様に被覆することが必要である。しかし、従来のフラッ
クスは、溶融速度は十分でなく、投与して完全に溶融滓
化するまでに、約100秒前後の時間(溶湯表面温度:
約1500〜1600℃)を要する。フラックス粉末として10
0〜300メッシュの微細粒度に調整されたものが使用
されているが、微細化だけでは溶融速度を十分に高める
ことはできない。200メッシュを越えるような微細粉
末では、粒子同士が凝集して溶湯表面に浮遊し易く、却
って溶融滓化の遅延を招く原因ともなる。また、そのよ
うな微細粉末は、粉体輸送性が悪く、フラックス投与作
業の自動化が困難である。本発明は、遠心鋳造に関する
上記問題を解消するための改良されたフラックスを提供
するものである。
In order to make the flux more effective in covering the molten metal, it is necessary to dissolve the applied flux quickly and uniformly coat the surface of the molten metal in a good fluidized state. It is. However, the conventional flux does not have a sufficiently high melting rate, and takes about 100 seconds (the surface temperature of the molten metal:
About 1500-1600 ° C). 10 as flux powder
Fine particles having a fine particle size of 0 to 300 mesh are used, but the melting rate cannot be sufficiently increased only by making the particles finer. In the case of a fine powder having a size exceeding 200 mesh, the particles tend to aggregate and float on the surface of the molten metal. Further, such fine powder has poor powder transportability, and it is difficult to automate the flux administration operation. The present invention provides an improved flux for overcoming the above problems associated with centrifugal casting.

【0004】[0004]

【課題を解決するための手段】本発明の遠心鋳造用フラ
ックスは、設定塩基度に基づいて配合された、シリカ,
アルミナ,炭酸カルシウム,炭酸マグネシウム,弗化カ
ルシウムの各化合物を含む粉末混合物を加熱溶融し、そ
の冷却固化物を粉砕処理することにより得られる粉体で
ある。
The flux for centrifugal casting according to the present invention is prepared by mixing silica,
A powder obtained by heating and melting a powder mixture containing each compound of alumina, calcium carbonate, magnesium carbonate, and calcium fluoride, and pulverizing the cooled solidified product.

【0005】従来の遠心鋳造用フラックスが、原料粉末
(シリカ,アルミナ,炭酸カルシウム,炭酸マグネシウ
ム,CaF2 等の化合物粉末)の単なる混合物であるの
に対し、本発明のフラックスは、その粉末混合物を加熱
溶融する工程を経由して製造され、本明細書ではこれを
プリメルト・フラックスと称している。原料粉末の混合
物中に存在する炭酸カルシウム(CaCO3 ),炭酸マ
グネシウム(MgCO3 )等の炭酸塩は、加熱溶融工程
で、下記の熱分解反応を生起してCO2 を分離する。従
って、本発明のプリメルト・フラックスには、CaCO
3 ,MgCO3 等の炭酸塩は存在しない。 CaCO3 →CaO+CO2 ↑ MgCO3 →MgO+CO2
[0005] The conventional flux for centrifugal casting is a raw material powder.
(Silica, alumina, calcium carbonate, magnesium carbonate
Mu, CaFTwoIs a simple mixture of compound powders
In contrast, the flux of the present invention heats the powder mixture.
Manufactured via a melting process, which is referred to herein as
It is called pre-melt flux. Mixing of raw material powder
Calcium carbonate (CaCO)Three) 、 Carbonated
Gnesium (MgCOThree), Etc. are heated and melted
Then, the following thermal decomposition reaction occurs to generate COTwoIs separated. Subordinate
Therefore, the premelt flux of the present invention contains CaCO
Three, MgCOThreeAre not present. CaCOThree→ CaO + COTwo↑ MgCOThree→ MgO + COTwo

【0006】炭酸塩(CaCO3 ,MgCO3 等)を含
む従来のフラックスは、溶湯に投与されて溶湯の保有熱
で、炭酸塩の分解反応(吸熱反応)を生じる。このた
め、溶融滓化が遅延し、しかも生成するCO2 ガスは溶
湯に対する酸素供給源となる。これと異なって、本発明
のフラックスは、そのような熱分解反応はなく、溶融滓
化に要する時間が短縮され、かつCO2 ガスによる溶湯
の酸化汚染の懸念も解消される。
A conventional flux containing a carbonate (CaCO 3 , MgCO 3, etc.) is applied to the molten metal and causes a decomposition reaction (endothermic reaction) of the carbonate by the retained heat of the molten metal. Therefore, the formation of molten slag is delayed, and the generated CO 2 gas serves as an oxygen supply source for the molten metal. On the other hand, the flux of the present invention does not have such a thermal decomposition reaction, shortens the time required for forming the molten slag, and eliminates the concern of oxidative contamination of the molten metal by CO 2 gas.

【0007】また、従来のフラックス(複数種の化合物
粉末の混合物)では、各化合物粉末の融点(SiO 2 : 約
2230℃, Al2 O 3 : 約2020℃, CaO:約2572℃,CaF:約13
60℃)や比重(SiO 2 : 約2.3, Al 2 O 3 : 約3.99, Ca
O:約3.4, CaF: 約3.2 )等の相違を付随し、この成分間
の物性の差異は、フラックスの迅速・均一な溶融滓化を
妨げる要因となる。本発明のプリメルト・フラックス
は、複数種の化合物が融合一体化されている効果として
そのような不具合が解消される。プリメルト工程を経由
して得られる本発明フラックスの溶融滓化性の改善効果
は顕著であり、従来のフラックス(溶融滓化時間:約1
00秒)に比し、わずか数秒(4〜6秒)(いずれも溶
湯温度:1500 〜1600℃)で溶融滓化を達成することがで
き、溶湯への投与後、速やかに溶湯表面を一様に被覆保
護する。
In the conventional flux (mixture of plural kinds of compound powders), the melting point (SiO 2 : about
2230 ℃, Al 2 O 3 : about 2020 ℃, CaO: about 2572 ℃, CaF: about 13
60 ° C) and specific gravity (SiO 2 : about 2.3, Al 2 O 3 : about 3.99, Ca
O: about 3.4, CaF: about 3.2), etc., and the difference in physical properties between the components is a factor that hinders rapid and uniform melting of the flux. The premelt flux of the present invention eliminates such inconveniences as a result of the fusion and integration of a plurality of types of compounds. The effect of the flux of the present invention obtained via the pre-melt process to improve the slag forming property is remarkable, and the conventional flux (the slag forming time: about 1
00 seconds), the molten slag can be achieved in only a few seconds (4 to 6 seconds) (all at a temperature of the melt of 1500 to 1600 ° C.). Protect the coating.

【0008】[0008]

【発明の実施の形態】本発明のプリメルト・フラックス
は、従来のフラックスと同じように、シリカ,アルミ
ナ,炭酸カルシウム,炭酸マグネシウム,弗化カルシウ
ム,その他の化合物(酸化鉄,酸化マンガン等)から適
宜選択される化合物粉末を原料として製造される。これ
らの化合物を設定塩基度に基づいて、適当な量比で配合
して原料粉末混合物とする。なお、炭酸カルシウム等の
炭酸塩は、事前に焙焼処理(約700〜800℃)に付
し、熱分解反応によりCaO,MgO等の粉末に変換し
たうえで、他の化合物粉末と配合するようにしてもよ
い。
BEST MODE FOR CARRYING OUT THE INVENTION The premelt flux of the present invention is prepared from silica, alumina, calcium carbonate, magnesium carbonate, calcium fluoride, and other compounds (iron oxide, manganese oxide, etc.) as in the conventional flux. It is manufactured using the selected compound powder as a raw material. These compounds are blended at an appropriate ratio based on the set basicity to obtain a raw material powder mixture. Note that carbonates such as calcium carbonate are subjected to a roasting process (about 700 to 800 ° C.) in advance, converted into powders such as CaO and MgO by a thermal decomposition reaction, and then mixed with other compound powders. It may be.

【0009】原料粉末混合物は電気炉等の加熱装置で加
熱溶融される。処理温度は、1200〜1300℃であ
り、設定温度域で適当時間(例えば,0.5 〜1 Hr)加熱
保持することにより、溶融処理を達成する。生成した溶
融物の冷却は、炉中冷却または大気中放冷としてよい。
その冷却固化物を、ボールミル、その他の粉砕手段によ
り適宜の粒度に粉砕し分級して目的とするプリメルト・
フラックスを得る。
The raw material powder mixture is heated and melted by a heating device such as an electric furnace. The processing temperature is from 1200 to 1300 ° C., and the melt processing is achieved by heating and maintaining for an appropriate time (for example, 0.5 to 1 Hr) in a set temperature range. Cooling of the resulting melt may be furnace cooling or air cooling.
The cooled solidified product is pulverized to an appropriate particle size by a ball mill or other pulverizing means and classified to obtain a desired pre-melt.
Get flux.

【0010】本発明のプリメルト・フラックスの好まし
い成分組成として、下記のものが挙げられる。構成成分
の量比はすべて重量基準である。 SiO2 :25〜30%,Al2 3 :2.5〜3.5
%,CaO:35〜45%,MgO:4.5〜5.5
%,CaF2 :8〜15%,Li2 O:2〜9%,残
部:FeO及びMnO、塩基度=CaO/(SiO2
Al2 3 ):1.2〜1.5。
The preferred components of the premelt flux of the present invention include the following. All component ratios are by weight. SiO 2: 25~30%, Al 2 O 3: 2.5~3.5
%, CaO: 35 to 45%, MgO: 4.5 to 5.5
%, CaF 2 : 8 to 15%, Li 2 O: 2 to 9%, balance: FeO and MnO, basicity = CaO / (SiO 2 +
Al 2 O 3): 1.2~1.5.

【0011】CaOおよびSiO2 はフラックスの基本
成分である。SiO2 は溶融フラックスの均質性を高
め、CaOは、SiO2 のネットワークを切断してフラ
ックスの流動性を高める作用を有する。Al2 3 は、
フラックスのガラス化を助長して溶湯との濡れ性を高
め、MgOは溶湯表面に対するフラックスの冶金的濡れ
性を良好にする。また、CaF2 はフラックスの低融点
化すると共に、流動性,非金属介在物の吸収除去効果を
高める。Li2 Oもフラックスの粘性を下げ、流動性を
良好化する。更に、塩基度が1.2〜1.5の範囲に調
節されていることにより、フラックスの低融点が確保さ
れ、フラックスの流動性、溶湯浄化作用を良好に保持す
ることができ、また鋳造終了後においては、鋳造物の表
面に残留したフラックス固化物の剥離が容易化される。
FeO,MnO等は、フラックス固化物の剥離性を高め
る効果を有する。
[0011] CaO and SiO 2 are basic components of the flux. SiO 2 enhances the homogeneity of the molten flux, and CaO has the effect of cutting the SiO 2 network to increase the fluidity of the flux. Al 2 O 3 is
MgO enhances the wettability with the molten metal by promoting vitrification of the flux, and MgO improves the metallurgical wettability of the flux on the surface of the molten metal. CaF 2 lowers the melting point of the flux and enhances the fluidity and the effect of absorbing and removing nonmetallic inclusions. Li 2 O also lowers the viscosity of the flux and improves the fluidity. Furthermore, by adjusting the basicity to the range of 1.2 to 1.5, a low melting point of the flux is ensured, and the fluidity of the flux and the action of purifying the molten metal can be maintained well. Later, the peeling of the solidified flux remaining on the surface of the casting is facilitated.
FeO, MnO, and the like have an effect of improving the releasability of the solidified flux.

【0012】本発明のプリメルト・フラックスの粉体粒
度は、従来のフラックス(粒度:100 〜300 メッシュ)
に比し、20〜200メッシュの比較的粗粒の粒度構成
とすることができ、このような比較的粗い粒度であって
も、良好な溶融滓化性が確保される。しかも、その粒度
構成においては、従来の微細粉末と異なって良好な粉体
流動性を有するので、フラックスの投与操作の自動化が
可能になる。例えば、図1のように、回転駆動ローラ
(1)に水平載置した鋳型(2)の鋳込み口から溶湯ホ
ッパー(3)を介して鋳型内に溶湯(M)を鋳込む一
方、他端の鋳込み口に配置したフラックス投与ホッパー
(4)により鋳型内の溶湯(M)にフラックス(F)を
投与する。フラックス(F)は良好な粉体輸送性を有す
るので、自重によりホッパー内を降下し自動的に鋳型内
溶湯に供給され、供給量はバルブ(電磁弁等)(5)に
より任意に調節される。フラックスの溶湯に対する投与
のタイミングや投与量等は従来の遠心鋳造の常法に従っ
て設定すればよい。
The powder particle size of the premelt flux of the present invention is the same as that of a conventional flux (particle size: 100 to 300 mesh).
, A relatively coarse particle size configuration of 20 to 200 mesh can be obtained, and even with such a relatively coarse particle size, good meltability can be ensured. In addition, in the particle size configuration, unlike the conventional fine powder, the powder has a good powder fluidity, so that the flux administration operation can be automated. For example, as shown in FIG. 1, the molten metal (M) is cast into the casting mold through the casting hopper (3) from the casting opening of the casting mold (2) horizontally mounted on the rotary drive roller (1), while the other end is formed. The flux (F) is administered to the molten metal (M) in the mold by the flux administration hopper (4) arranged at the casting port. Since the flux (F) has good powder transportability, it falls down in the hopper by its own weight and is automatically supplied to the molten metal in the mold, and the supply amount is optionally adjusted by a valve (such as a solenoid valve) (5). . The timing of the administration of the flux to the molten metal, the dosage, and the like may be set according to a conventional method of conventional centrifugal casting.

【0013】本発明のプリメルト・フラックスは、鋳造
物の冷却凝固に伴って固化した後の剥離性も良好であ
る。すなわち、鋳造物の表面に生成するフラックス固化
物は鋳造物の降温過程で漸次剥落していくので、鋳造物
の内面に対する付着残留は殆どなく、付着残留している
場合でも、ウエス等で軽く拭うことにより容易に除去す
ることができる。また、従来のフラックスを使用した鋳
造物の内面は、仕上げ加工に約2mm前後の研削代を必要
とするが、本発明のフラックスを使用して得られる鋳造
物の内面鋳肌は極めて平滑美麗であるので、機械加工の
必要は殆どなく、それを必要とする場合でも、研削代は
ごく微量である。
The pre-melt flux of the present invention has good releasability after solidification accompanying cooling and solidification of a casting. That is, since the solidified flux generated on the surface of the casting gradually peels off during the cooling process of the casting, there is almost no adhesion residue on the inner surface of the casting, and even if the adhesion remains, gently wipe it with a rag or the like. Thus, it can be easily removed. The inner surface of the casting using the conventional flux requires a grinding allowance of about 2 mm for finishing, but the inner casting surface of the casting obtained using the flux of the present invention is extremely smooth and beautiful. Therefore, there is almost no need for machining, and even when it is necessary, the grinding allowance is very small.

【0014】[0014]

【実施例】(1)供試フラックスの製造 シリカ,アルミナ,炭酸カルシウム,炭酸マグネシウ
ム,弗化カルシウム,酸化鉄,酸化マンガンの各粉末を
混合する。混合粉末を電気炉に装入して加熱溶融(1300
℃×0.5Hr)する。溶融物を大気中で自然放冷した後、固
化物を粉砕処理(ボールミル)し、分級して供試フラッ
クスA,Bを得る。比較例として従来材に相当する供試
フラックスa,b(原料粉末の混合物,プリメルト工程
なし)を別途用意した。フラックスA,B(プリメル
ト)の粒径は 20 〜200 メッシュ、フラックスa,b
(原料粉末混合体)の粒径は 100〜300 メッシュであ
る。表1に各供試フラックスの組成を示す。フラックス
a,b(いずれも混合粉末)の組成は、溶湯への投与
(炭酸塩熱分解)後の値に換算して示している。
EXAMPLES (1) Production of Test Flux Powders of silica, alumina, calcium carbonate, magnesium carbonate, calcium fluoride, iron oxide and manganese oxide are mixed. The mixed powder is charged into an electric furnace and heated and melted (1300
° C x 0.5Hr). After the melt is allowed to cool naturally in the air, the solid is pulverized (ball mill) and classified to obtain test fluxes A and B. As comparative examples, test fluxes a and b (mixture of raw material powders, without a pre-melt step) corresponding to conventional materials were separately prepared. The particle size of fluxes A and B (Premelt) is 20-200 mesh, fluxes a and b
The particle size of the (raw material powder mixture) is 100 to 300 mesh. Table 1 shows the composition of each test flux. The compositions of fluxes a and b (both mixed powders) are shown in terms of values after administration to molten metal (carbonate pyrolysis).

【0015】(2)鋳造試験 鋳鋼材種:ステンレス鋳鋼(JIS G 5121 SCS 1相当材) 溶湯鋳込み温度:1640℃ 鋳造管サイズ:内径 750, 長さ 5000,肉厚 110(mm) フラックス投与量:20 kg 鋳型内溶湯に対するフラックスの投与は、遠心鋳造鋳型
の側部に配置したホッパーを介して行った。
(2) Casting test Cast steel material: stainless cast steel (JIS G 5121 SCS 1 equivalent material) Molten casting temperature: 1640 ° C Cast pipe size: inner diameter 750, length 5000, wall thickness 110 (mm) Flux dose: The flux was applied to the molten metal in the 20 kg mold via a hopper arranged on the side of the centrifugal casting mold.

【0016】各供試フラックスについて、溶融滓化時
間,鋳造後のフラックス固化物の剥離性、鋳造管の内面
の鋳肌性状(平滑性)および内面の機械研削代を比較評
価し、表2に示す結果を得た。溶融滓化時間は鋳造開始
直後のフラックスで被覆された溶湯表面を放射温度計で
測温して判定した。鋳造後の剥離性は、常温まで冷却降
温した鋳造管の内面に観察されるフラックス固化物の付
着残存量とその付着の強弱により評価し、管内面の鋳肌
性状は平滑度合いを肉眼観察に基づいて評価した(○…
良好,△…やや悪い,×…劣る)。
For each of the test fluxes, the melt slag time, the releasability of the solidified flux after casting, the casting surface properties (smoothness) of the inner surface of the casting tube, and the mechanical grinding allowance of the inner surface were compared and evaluated. The results shown were obtained. The molten slag time was determined by measuring the temperature of the molten metal surface coated with the flux immediately after the start of casting with a radiation thermometer. The peelability after casting was evaluated based on the amount of residual flux solidification observed on the inner surface of the cast tube cooled to room temperature and the strength of the adhesion. (...
Good, Δ: somewhat poor, ×: poor).

【0017】[0017]

【表1】 [Table 1]

【0018】[0018]

【表2】 [Table 2]

【0019】表2に示したように、発明例のフラックス
A,Bは比較例のフラックスa,bに比し、極く短時間
で溶融滓化している。また、フラックスA,Bは、鋳造
後のフラックス固化物の付着残留が殆どなく、比較例の
フラックスa,bに比し良好な剥離性を有している。更
に、比較例のフラックスa,bを使用した鋳造管の内面
は粗い鋳肌を呈し、仕上げ加工に1.5 〜2mm の研削代を
必要としているのに対し、発明例のフラックスA,Bを
使用した鋳造管は、機械加工を必要としない平滑美麗な
鋳肌を有している。これはフラックスの卓抜した押湯保
温効果を示すものであり、比較例との差異は歴然であ
る。
As shown in Table 2, the fluxes A and B of the invention example were molten in a very short time compared to the fluxes a and b of the comparative example. Further, the fluxes A and B have little adhesion of the solidified flux after casting, and have better releasability than the fluxes a and b of the comparative example. Further, the inner surface of the cast pipe using the fluxes a and b of the comparative example has a rough casting surface and requires a grinding allowance of 1.5 to 2 mm for finishing, whereas the fluxes A and B of the inventive example were used. The casting tube has a smooth and beautiful casting surface that does not require machining. This shows the excellent heating effect of the hot water by the flux, and the difference from the comparative example is obvious.

【0020】[0020]

【発明の効果】本発明の遠心鋳造用フラックスは、迅速
に溶融滓化してすぐれた押湯保温効果を奏し、鋳造後の
剥離性も良好である。本発明フラックスの改良された押
湯保温効果により、鋳造管内面は著しく平滑美麗な鋳肌
となり、仕上げ研削代を大幅に低減することができ、機
械加工コストの節減,製品歩留りの向上等の効果が得ら
れる。この鋳造品質の改善効果は、原料粉末混合物の加
熱溶融(プリメルト)に要するコスト増分の不利を充分
に補って余りあるものである。また、フラックス粉末の
粒度調整により、溶湯への投与を自動化することも可能
となり、遠心鋳造操業の効率化を可能にするものであ
る。
The flux for centrifugal casting according to the present invention is quickly melted, exhibits an excellent heat retention effect, and has good releasability after casting. Due to the improved feeder heat retention effect of the flux of the present invention, the inner surface of the casting tube has a remarkably smooth and beautiful casting surface, and the finish grinding allowance can be greatly reduced, thereby reducing machining costs and improving product yield. Is obtained. This effect of improving the casting quality sufficiently compensates for the disadvantage of the additional cost required for heating and melting (premelt) the raw material powder mixture. Further, by adjusting the particle size of the flux powder, it is possible to automate the dosing of the molten metal, thereby enabling the efficiency of the centrifugal casting operation to be improved.

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

【図1】遠心鋳造におけるフラックスの供給態様の例を
示す正面説明図である。
FIG. 1 is a front explanatory view showing an example of a supply mode of a flux in centrifugal casting.

【符号の説明】[Explanation of symbols]

1:回転駆動ローラ 2:鋳型 3:溶湯鋳込みホッパー 4:フラックス投与ホッパー 5:バルブ F:フラックス M:溶湯 1: Rotary drive roller 2: Mold 3: Melt casting hopper 4: Flux dosing hopper 5: Valve F: Flux M: Molten metal

Claims (3)

【特許請求の範囲】[Claims] 【請求項1】 設定塩基度に基づいて配合された、シリ
カ,アルミナ,炭酸カルシウム,炭酸マグネシウム,弗
化カルシウムの各化合物を含む粉末混合物を加熱溶融
し、その冷却固化物を粉砕処理して得られた粉末からな
る遠心鋳造用プリメルト・フラックス。
1. A powder mixture containing each compound of silica, alumina, calcium carbonate, magnesium carbonate and calcium fluoride, which is blended based on a set basicity, is heated and melted, and a cooled solidified product is obtained by pulverizing. Premelt flux for centrifugal casting made of powder.
【請求項2】 重量%で,SiO2 :25〜30%,A
2 3 :2.5〜3.5%,CaO:35〜45%,
MgO:4.5〜5.5%,CaF2 :8〜15%,L
2 O:2〜9%,残部はFeO及びMnOからなり、
塩基度〔(CaO)/(SiO2 +Al2 3 )〕:
1.2〜1.5である請求項1に記載の遠心鋳造用プリ
メルト・フラックス。
2. SiO 2 : 25 to 30% by weight, A
l 2 O 3: 2.5~3.5%, CaO: 35~45%,
MgO: 4.5~5.5%, CaF 2: 8~15%, L
i 2 O: 2 to 9%, the balance being FeO and MnO;
Basicity [(CaO) / (SiO 2 + Al 2 O 3 )]:
The pre-melt flux for centrifugal casting according to claim 1, wherein the flux is 1.2 to 1.5.
【請求項3】 20〜200メッシュの粒度を有する請
求項1または請求項2に記載の遠心鋳造用プリメルト・
フラックス。
3. The premelt for centrifugal casting according to claim 1, which has a particle size of 20 to 200 mesh.
flux.
JP21779398A 1998-07-31 1998-07-31 Premelt flux for centrifugal casting Expired - Lifetime JP3748716B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP21779398A JP3748716B2 (en) 1998-07-31 1998-07-31 Premelt flux for centrifugal casting

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP21779398A JP3748716B2 (en) 1998-07-31 1998-07-31 Premelt flux for centrifugal casting

Publications (2)

Publication Number Publication Date
JP2000042706A true JP2000042706A (en) 2000-02-15
JP3748716B2 JP3748716B2 (en) 2006-02-22

Family

ID=16709826

Family Applications (1)

Application Number Title Priority Date Filing Date
JP21779398A Expired - Lifetime JP3748716B2 (en) 1998-07-31 1998-07-31 Premelt flux for centrifugal casting

Country Status (1)

Country Link
JP (1) JP3748716B2 (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100524432B1 (en) * 2002-09-28 2005-10-27 스톨베르그 앤드 삼일 주식회사 Premelted manganese slag composition for production of mold flux and mold flux manufactured therefrom
JP2010023043A (en) * 2008-07-15 2010-02-04 Jfe Steel Corp Flux for centrifugal casting
JP2010023044A (en) * 2008-07-15 2010-02-04 Jfe Steel Corp Flux for centrifugal casting
WO2018048162A1 (en) * 2016-09-12 2018-03-15 주식회사 포스코 Blocking material and method for producing alloy steel using same

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100524432B1 (en) * 2002-09-28 2005-10-27 스톨베르그 앤드 삼일 주식회사 Premelted manganese slag composition for production of mold flux and mold flux manufactured therefrom
JP2010023043A (en) * 2008-07-15 2010-02-04 Jfe Steel Corp Flux for centrifugal casting
JP2010023044A (en) * 2008-07-15 2010-02-04 Jfe Steel Corp Flux for centrifugal casting
WO2018048162A1 (en) * 2016-09-12 2018-03-15 주식회사 포스코 Blocking material and method for producing alloy steel using same
CN109804091A (en) * 2016-09-12 2019-05-24 株式会社Posco Barrier material and for use its manufacture steel alloy method

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