JPH0347943B2 - - Google Patents

Info

Publication number
JPH0347943B2
JPH0347943B2 JP59185767A JP18576784A JPH0347943B2 JP H0347943 B2 JPH0347943 B2 JP H0347943B2 JP 59185767 A JP59185767 A JP 59185767A JP 18576784 A JP18576784 A JP 18576784A JP H0347943 B2 JPH0347943 B2 JP H0347943B2
Authority
JP
Japan
Prior art keywords
weight
slurry
spherical
product
particle size
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 - Lifetime
Application number
JP59185767A
Other languages
Japanese (ja)
Other versions
JPS6163333A (en
Inventor
Taketoki Hirata
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.)
NAIGAI SERAMITSUKUSU KK
Original Assignee
NAIGAI SERAMITSUKUSU KK
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 NAIGAI SERAMITSUKUSU KK filed Critical NAIGAI SERAMITSUKUSU KK
Priority to JP18576784A priority Critical patent/JPS6163333A/en
Publication of JPS6163333A publication Critical patent/JPS6163333A/en
Publication of JPH0347943B2 publication Critical patent/JPH0347943B2/ja
Granted legal-status Critical Current

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B22CASTING; POWDER METALLURGY
    • B22CFOUNDRY MOULDING
    • B22C1/00Compositions of refractory mould or core materials; Grain structures thereof; Chemical or physical features in the formation or manufacture of moulds

Landscapes

  • Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Materials Engineering (AREA)
  • Mechanical Engineering (AREA)
  • Mold Materials And Core Materials (AREA)

Description

【発明の詳細な説明】[Detailed description of the invention]

[産業上の利用分野] 本発明は鋳鉄、鋳鋼、アルミニウム、銅合金等
の鋳造用に使われる鋳物砂を工業的に合成し製造
する方法に関するものである。 [従来の技術とその問題点] 従来、鋳物砂としては天然に産するジルコンサ
ンド(ZrO2・SiO2、融点約1780℃)、クロマイト
(Cr2O3・FeO、融点約2000℃)と珪砂(SiO2
融点約1750℃)等の粒子径が0.05〜1.5mm程度の
ものが用いられていた。しかしながらこれらは天
然産品であるために化学組成、物理的特性等の品
質のバラツキや必要粒度品の不足等の避けられな
い問題がある。そこで天然原料を塊状にしたもの
をロータリーキルン等で焼いてその後これを必要
粒度に粉砕したものもあつたが、その場合不必要
な微粒が多く発生するために歩留が悪い欠点があ
るほか、粒子が角状或いは針状の形態になるため
に流動性が悪く鋳物砂としての使用時に充填が不
均一になり易く、また鋳肌が荒れ易くなる等の欠
点があつた。 [問題点を解決するための手段] そこで本発明は安定した品質の鋳物砂を工業的
に合成製造する方法を提供しようとするものであ
る。その目的を達成するため本発明は、製品の主
成分としてAl2O3が20〜70重量%、SiO2が80〜30
重量%になるように泥漿を配合し、該泥奨に解こ
う剤を添加してスプレードライヤーにより熱風中
に吹出し、粒子径が0.05〜2.0mmの球状粒を乾燥
造粒し、その後これをロータリーキルンにて焼結
してなることを特徴とした球状鋳物砂の製造方法
である。 以下本発明についてさらに詳しく説明すると、
まづ原料としては粘土鉱物(耐火粘土、クレー、
カオリン)、珪砂、バン土ケツ岩、ボーキサイト、
シリマナイト鉱物(アンダリユーサイト、カイア
ナイト、シリマナイト)、水酸化アルミニウム、
〓焼アルミナ等を用い、これらを相互に組み合
せ、鋳物砂として充分使用可能な化学組成
(Al2O3;20〜70重量%、SiO2;70〜30重量%、
その他の不純物(Fe2O3、TiO2、K2O、Na2O、
CaO、MaO等)が5重量%以下となるよう配合
する。例えば融点については、Al2O3;30重量
%、SiO2;68重量%、その他;2重量%では、
約1700℃でAl2O3;70重量%、SiO2;29重量%、
その他;1重量%では約1850℃である。配合が決
定されたものは泥漿状態に混合される。この時、
泥漿に解こう剤(苛性ソーダ、リン酸ソーダ、珪
酸ソーダ、タンニン酸ソーダ、アルミン酸ソーダ
等のソーダ化合物、水酸化リチウム、くえん酸リ
チウム等のリチウム化合物、水酸化カリウム、炭
酸カリウム等のカリウム化合物、蓚酸アンモン、
硫酸シアン化アンモン等のアンモニア化合物、ポ
リビニールアミン、ジエチルアミン等のアミン系
化合物)を0.01〜5重量%の範囲で添加すること
により泥漿の粘性を変化させ製品粒径を制御す
る。このようにして調整した泥しようをスプレー
ドライヤーにより熱風中に吹出し、0.05〜2.0mm
の球状に造粒乾燥させる。一般にスプレードライ
ヤーは、第1図に示したようにダクト4から350
〜450℃の熱風を室1に送り、該室1にノズル2
から泥漿を加圧状態で噴霧することにより表面張
力で球状となつた粒子を乾燥させ、球状の造粒乾
燥品として排出口3より取り出すものである。な
お5は排風ダクトである。その後造粒乾燥品をロ
ータリーキルンで焼成し、この球状で粒子径が
0.05〜2.0mmの焼結粒子を球状鋳物砂とする。こ
の焼結粒子は必要に応じてフルイ分け、目的の粒
度品として用いられる。 [実施例] 原料に粘土と水酸化アルミニウムを用いた。そ
の化学組成を表1に示す。
[Industrial Application Field] The present invention relates to a method for industrially synthesizing and manufacturing foundry sand used for casting cast iron, cast steel, aluminum, copper alloys, etc. [Conventional technology and its problems] Conventionally, naturally occurring zircon sand (ZrO 2・SiO 2 , melting point approximately 1780°C), chromite (Cr 2 O 3・FeO, melting point approximately 2000°C) and silica sand have been used as foundry sand. ( SiO2 ,
(melting point: approximately 1750°C) and particle diameters of approximately 0.05 to 1.5 mm were used. However, since these are natural products, there are unavoidable problems such as variations in quality such as chemical composition and physical properties, and shortages of necessary particle sizes. Therefore, there was a method in which a lump of natural raw materials was baked in a rotary kiln or the like and then pulverized to the required particle size, but in this case, many unnecessary fine particles were generated, resulting in a poor yield, and Because of its angular or acicular shape, it has poor fluidity and tends to be filled unevenly when used as foundry sand, and the casting surface tends to become rough. [Means for Solving the Problems] Therefore, the present invention aims to provide a method for industrially synthesizing foundry sand of stable quality. In order to achieve that purpose, the present invention uses 20 to 70% by weight of Al 2 O 3 and 80 to 30% by weight of SiO 2 as the main components of the product.
A peptizer is added to the slurry, and the slurry is blown into hot air using a spray dryer to dry and granulate spherical particles with a particle size of 0.05 to 2.0 mm, which are then placed in a rotary kiln. This is a method for producing spherical foundry sand characterized by sintering it in a process. The present invention will be explained in more detail below.
First, raw materials include clay minerals (fireclay, clay,
kaolin), silica sand, slagstone, bauxite,
Sillimanite minerals (andalyusite, kyanite, sillimanite), aluminum hydroxide,
= By using calcined alumina, etc., and combining them with each other, a chemical composition that can be used sufficiently as foundry sand ( Al2O3 : 20-70% by weight , SiO2 : 70-30% by weight,
Other impurities (Fe 2 O 3 , TiO 2 , K 2 O, Na 2 O,
(CaO, MaO, etc.) is blended so that it is 5% by weight or less. For example, regarding the melting point, Al2O3 : 30% by weight, SiO2 : 68% by weight, others: 2% by weight,
Al 2 O 3 ; 70% by weight, SiO 2 ; 29% by weight, at approximately 1700°C.
Others: At 1% by weight, the temperature is about 1850°C. Once the formulation has been determined, it is mixed into a slurry. At this time,
Add peptizers to the slurry (soda compounds such as caustic soda, sodium phosphate, sodium silicate, sodium tannate, and sodium aluminate; lithium compounds such as lithium hydroxide and lithium citrate; potassium compounds such as potassium hydroxide and potassium carbonate; ammonium oxalate,
By adding an ammonia compound such as ammonium sulfate cyanide, or an amine compound such as polyvinylamine or diethylamine in a range of 0.01 to 5% by weight, the viscosity of the slurry is changed and the particle size of the product is controlled. The slurry prepared in this way was blown out into hot air using a spray dryer, and the thickness was 0.05 to 2.0 mm.
Granulate and dry into spherical shapes. Generally, the spray dryer has duct 4 to 350 as shown in Figure 1.
~450℃ hot air is sent to chamber 1, and nozzle 2 is installed in chamber 1.
The slurry is sprayed under pressure from the slurry to dry the particles, which have become spherical due to surface tension, and are taken out from the discharge port 3 as spherical dried granulated products. Note that 5 is an exhaust duct. After that, the dried granulated product is fired in a rotary kiln, and the spherical particle size is reduced.
The sintered particles of 0.05 to 2.0 mm are used as spherical foundry sand. The sintered particles are sieved as necessary and used as a product with the desired particle size. [Example] Clay and aluminum hydroxide were used as raw materials. Its chemical composition is shown in Table 1.

【表】【table】

【表】 配合割合を表2に示す。【table】 The blending ratios are shown in Table 2.

【表】 混合はボールミルを用い湿式で2時間の混合を
行なつた。泥しようの比重は1.68g/cm3、泥しよ
う中の固形分割合は66%であつた。スプレードラ
イヤーは加圧ノズル噴霧の向流式乾燥装置を用
い、泥しようを0.1〜1.0mmの球状粒子に造粒乾燥
させた。その粒度分布を表3に示した。
[Table] Mixing was carried out in a wet manner for 2 hours using a ball mill. The specific gravity of the slurry was 1.68 g/cm 3 , and the solid content in the slurry was 66%. The spray dryer was a countercurrent type drying device with pressure nozzle spraying, and the slurry was granulated and dried into spherical particles of 0.1 to 1.0 mm. The particle size distribution is shown in Table 3.

【表】 造粒乾燥品はロータリーキルンにて約1550℃の
温度で焼成した。焼成品の物理的特性(0.5〜
0.297mmの粒子径のもの)を表4に、化学分析値
を表5に示した。
[Table] The dried granulated product was fired in a rotary kiln at a temperature of approximately 1550°C. Physical properties of fired products (0.5~
Table 4 shows the particle diameter of 0.297 mm, and Table 5 shows the chemical analysis values.

【表】【table】

【表】【table】

【表】 また、第2図に焼成された製品の粒子構造の顕
微鏡写真を示したようにその外観は球状を呈して
いる。 [発明の効果] 本発明により製造された鋳物砂は粒子形が球状
で、その直径が0.05〜2.0mmに造粒したため流動
性に優れており、細部まで均一な充填が可能とな
り、鋳型製作において精密で、均一な組織を有す
る鋳型が生産可能となる、又、球状粒子形である
ことより鋳物の鋳はだが美しく仕上がる。更にロ
ータリーキルンにより各粒子は充分に焼結させら
れているため粒子強度は高くなつている。このこ
とにより、再度くり返し鋳物砂の使用が可能とな
る。更に工業的に合成して、製造するため球状と
いう一定形状を持つ品質の安定した必要粒度品の
供給が可能となるなど産業上有益なものである。
[Table] Furthermore, as shown in FIG. 2, a microscopic photograph of the particle structure of the fired product, its appearance is spherical. [Effect of the invention] The molding sand produced according to the present invention has a spherical particle shape and is granulated with a diameter of 0.05 to 2.0 mm, so it has excellent fluidity and can be filled evenly in the details, making it suitable for mold manufacturing. It is possible to produce molds with a precise and uniform structure, and the spherical particle shape allows castings to be finished beautifully. Furthermore, since each particle is sufficiently sintered by the rotary kiln, the particle strength is high. This makes it possible to use the foundry sand again. Furthermore, since it is industrially synthesized and manufactured, it is possible to supply a product with a constant spherical shape and the required particle size with stable quality, which is industrially useful.

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

第1図は本発明にて使用されるスプレードライ
ヤーの概略を示した縦断面図、第2図は製品の粒
子構造を示した顕微鏡写真である。
FIG. 1 is a longitudinal sectional view schematically showing the spray dryer used in the present invention, and FIG. 2 is a microscopic photograph showing the particle structure of the product.

Claims (1)

【特許請求の範囲】[Claims] 1 製品の主成分としてAl2O3が20〜70重量%、
SiO2が80〜30重量%になるように泥奨を配合し、
該泥奨に解こう剤を添加してスプレードライヤー
により熱風中に吹出し、粒子径が0.05〜2.0mmの
球状粒に造粒し、その後これをロータリーキルン
にて焼結してなることを特徴とした球状鋳物砂の
製造方法。
1 20-70% by weight of Al 2 O 3 as the main component of the product,
Add mud so that SiO 2 is 80 to 30% by weight,
A peptizer was added to the slurry, which was then blown into hot air using a spray dryer to granulate it into spherical particles with a particle size of 0.05 to 2.0 mm, which was then sintered in a rotary kiln. Method for producing spherical foundry sand.
JP18576784A 1984-09-05 1984-09-05 Production of molding material for casting Granted JPS6163333A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP18576784A JPS6163333A (en) 1984-09-05 1984-09-05 Production of molding material for casting

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP18576784A JPS6163333A (en) 1984-09-05 1984-09-05 Production of molding material for casting

Publications (2)

Publication Number Publication Date
JPS6163333A JPS6163333A (en) 1986-04-01
JPH0347943B2 true JPH0347943B2 (en) 1991-07-22

Family

ID=16176520

Family Applications (1)

Application Number Title Priority Date Filing Date
JP18576784A Granted JPS6163333A (en) 1984-09-05 1984-09-05 Production of molding material for casting

Country Status (1)

Country Link
JP (1) JPS6163333A (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2004052572A1 (en) * 2002-12-09 2004-06-24 Kao Corporation Spherical casting sand
JP2006150451A (en) * 2004-11-02 2006-06-15 Kao Corp Ceramic particles
WO2014128981A1 (en) 2013-02-19 2014-08-28 伊藤忠セラテック株式会社 Method for modifying refractory molding particles and refractory molding particles obtained thereby and process for producing mold
US11236904B2 (en) 2018-01-19 2022-02-01 Itochu Ceratech Corporation Bed medium for fluidized bed

Families Citing this family (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP5297731B2 (en) 2007-09-12 2013-09-25 花王株式会社 Recycled casting sand manufacturing method
JP5075902B2 (en) * 2009-10-05 2012-11-21 キンセイマテック株式会社 Mold sand and its manufacturing method
CN102179482B (en) * 2011-01-24 2014-05-28 江苏兴盛重工有限公司 Mould paint spraying device
JP6892284B2 (en) 2017-02-28 2021-06-23 ダイハツ工業株式会社 Sand mold manufacturing method and casting sand
JP6880302B1 (en) 2019-11-22 2021-06-02 キンセイマテック株式会社 Kit for casting sand and sand molds

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS4967822A (en) * 1972-11-02 1974-07-01

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS4967822A (en) * 1972-11-02 1974-07-01

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2004052572A1 (en) * 2002-12-09 2004-06-24 Kao Corporation Spherical casting sand
JP2006150451A (en) * 2004-11-02 2006-06-15 Kao Corp Ceramic particles
JP4603463B2 (en) * 2004-11-02 2010-12-22 花王株式会社 Spherical casting sand
WO2014128981A1 (en) 2013-02-19 2014-08-28 伊藤忠セラテック株式会社 Method for modifying refractory molding particles and refractory molding particles obtained thereby and process for producing mold
US10456829B2 (en) 2013-02-19 2019-10-29 Itochu Ceratech Corporation Method for modifying refractory molding particles and refractory molding particles obtained thereby and process for producing mold
US11236904B2 (en) 2018-01-19 2022-02-01 Itochu Ceratech Corporation Bed medium for fluidized bed

Also Published As

Publication number Publication date
JPS6163333A (en) 1986-04-01

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