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JPS6258809B2 - - Google Patents
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JPS6258809B2 - - Google Patents

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Publication number
JPS6258809B2
JPS6258809B2 JP15935183A JP15935183A JPS6258809B2 JP S6258809 B2 JPS6258809 B2 JP S6258809B2 JP 15935183 A JP15935183 A JP 15935183A JP 15935183 A JP15935183 A JP 15935183A JP S6258809 B2 JPS6258809 B2 JP S6258809B2
Authority
JP
Japan
Prior art keywords
resin
sand
coated
resol type
thermosetting
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
JP15935183A
Other languages
Japanese (ja)
Other versions
JPS6049829A (en
Inventor
Masae Kuroda
Takeshi Sumi
Yukio Yoshimura
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.)
Resonac Corp
Original Assignee
Hitachi Chemical Co Ltd
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 Hitachi Chemical Co Ltd filed Critical Hitachi Chemical Co Ltd
Priority to JP15935183A priority Critical patent/JPS6049829A/en
Publication of JPS6049829A publication Critical patent/JPS6049829A/en
Publication of JPS6258809B2 publication Critical patent/JPS6258809B2/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
    • B22C1/16Compositions of refractory mould or core materials; Grain structures thereof; Chemical or physical features in the formation or manufacture of moulds characterised by the use of binding agents; Mixtures of binding agents
    • B22C1/20Compositions of refractory mould or core materials; Grain structures thereof; Chemical or physical features in the formation or manufacture of moulds characterised by the use of binding agents; Mixtures of binding agents of organic agents
    • B22C1/22Compositions of refractory mould or core materials; Grain structures thereof; Chemical or physical features in the formation or manufacture of moulds characterised by the use of binding agents; Mixtures of binding agents of organic agents of resins or rosins
    • B22C1/2233Compositions of refractory mould or core materials; Grain structures thereof; Chemical or physical features in the formation or manufacture of moulds characterised by the use of binding agents; Mixtures of binding agents of organic agents of resins or rosins obtained otherwise than by reactions only involving carbon-to-carbon unsaturated bonds
    • B22C1/2273Polyurethanes; Polyisocyanates

Landscapes

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Chemical Kinetics & Catalysis (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]

本発明は加熱硬化型鋳物用樹脂被覆砂およびそ
の製造方法に関するものであり、特に主にアルミ
ニウム鋳物、合金鋳物など比較的鋳込温度の低い
鋳物の製造に用いられる鋳込み後の鋳型の崩壊性
を著しく改良した加熱硬化型鋳物用樹脂被覆砂お
よびその製造方法に関するものである。 一般に加熱硬化型鋳物用樹脂被覆砂に用いられ
る被覆用粘結剤はフエノールとホルムアルデヒド
を酸性又はアルカリ性で反応して得られる樹脂で
あるが、これらのフエノール樹脂を用いるシエル
モールド法をアルミ鋳物のような鋳込み温度の低
い鋳物用砂型に適用した場合には鋳型の崩壊性が
悪く500℃位の高温で6〜12時間の加熱処理が必
要で、鋳込み後の砂落し作業に非常に大きな費用
と労力が必要となつている。そこで鋳型の崩壊性
を改良するためにフエノール樹脂にハロゲン化合
物やリン化合物を添加する方法が提案されている
が未だ十分な崩壊性が得られていない。特に最近
は、エネルギーの節減が叫ばれており加熱処理を
低減するかつ現行のシエルモールド法と同等の作
業のできる加熱硬化型鋳物用樹脂被覆砂が強く要
望されている。 本発明者は、鋳込み後加熱処理を低減し容易に
崩壊し、かつ現行のシエルモールド法と同等の作
業のできる加熱硬化型鋳物用樹脂被覆砂を鋭意検
討した結果鋳物用砂にブロツクイソシネート化合
物とレゾール型フエノール樹脂を含有する組成物
を被覆した樹脂被覆砂を使用することにより鋳込
み後の崩壊性が著しく改善され、かつ現行のシエ
ルモールド法と同等の作業(砂の流動性、硬化速
度)ができることを見い出した。 すなわち本発明によれば上記からなる加熱硬化
型鋳物用樹脂被覆砂を150℃〜350℃に加熱された
金型に充填させると、ブロツクイソシアネート化
合物のブロツク剤が解離し、発生するイソシアネ
ート化合物とレゾール型フエノール樹脂のメチロ
ール基及び水酸基等が反応しウレタン結合により
鋳型が強固になり抜型可能な強度に達する。又鋳
型の崩壊性が著しく向上する。これは鋳型の形成
にウレタン結合を用いているためと思われる。 本発明に用いる組成物のブロツクイソシアネー
ト化合物としてはポリイソシアネート化合物とイ
ソシアネートブロツク剤との付加反応生成物が用
いられる。ポリイソシアネート化合物としては従
来公知のイソシアネート基を2個以上有するイソ
シアネート化合物のいずれも使用することがで
き、又、これらのポリイソシアネート化合物とエ
チレングリコール、プロピレングリコール、トリ
メチロールプロパン、グリセリン、ポリエーテル
ポリオール類などの活性水素化合物などを反応さ
せた末端イソシアネート基含有化合物なども用い
られる。 イソシアネートブロツク剤としては、従来より
用いられているものはいずれも使用することがで
き、フエノール、クレゾール、キシレノールノニ
ルフエノール等のフエノール類、t−ブチルアル
コール等の第3級アルコール類、アセチルアセト
ン、マロン酸ジエステルなどの活性メチレン化合
物、メチルアニリン、ジフエニルアミンなどの芳
香族アミン類、フタル酸イミドなどのイミド類、
ε−カプロラクタムなどのラクタム類、エチレン
イミンなどのイミン類、尿素類、オキシム類、重
亜硫酸塩類、ホウ酸類などがある。本発明に用い
るブロツクイソシアネート化合物は、上記イソシ
アネート化合物とイソシアネートブロツク化剤と
を従来公知の方法により反応させて得られる。 又本発明に用いるレゾール型フエノール樹脂と
しては砂の乾燥性保持のためビスフエノール類を
用いたレゾール樹脂が好ましく更に常温で固形の
ものが好ましい。レゾール型フエノール樹脂とし
ては、メチロール基をもつたフエノール樹脂であ
ればいずれでも使用することができ又レゾール型
フエノール樹脂の合成についても特に限定しない
がフエノール、クレゾール、ビスフエノールA、
ビスフエノールS、ビスフエノールF等のフエノ
ール類とホルムアルデヒドをNaOH、Ba
(OH)2、アンモニア、トリメチルアミン等の合成
触媒を用いて反応させ従来公知の方法により得ら
れる。レゾール型ビスフエノール樹脂としては、
ビスフエノールA、ビスフエノールS、ビスフエ
ノールF等のビスフエノール類とホルムアルデヒ
ドをNaOH、Ba(OH)2アンモニア、トリメチル
アミン等の触媒を用いて反応させることにより得
られる樹脂が用いられる。 レゾール型ビスフエノール樹脂としてビスフエ
ノールA1モルに対してホルムアルデヒドは1.5〜
4.0モルを反応させて得られる樹脂が好ましく用
いられる。ホルムアルデヒドが1.5モル未満であ
るとメチロール基が少なくなり硬化速度が遅くな
り、又ホルムアルデヒドが4.0モルを越えると砂
型の加熱硬化時にホルムアルデヒド臭が強くなり
好ましくない。 本発明の鋳物用樹脂被覆砂は90〜180℃に加熱
された鋳物用砂に固形あるいは溶液のブロツクイ
ソシアネート化合物と固型あるいは溶液のレゾー
ル型フエノール樹脂を撹拌混合せしめ、この混合
工程中に必要に応じ溶媒を蒸発せしめることによ
り得られる。鋳物砂の温度が180℃を越えるとブ
ロツクイソシアネート化合物の解離が始まり鋳物
用樹脂被覆砂のライフが短かくなるばかりでなく
砂型の強度も低下し好ましくない。又温度が90℃
未満の温度、樹脂の被覆が不十分となつたり溶媒
の蒸発が不十分となり、鋳物用樹脂被覆砂の融着
点が低くなりブロツキングを起こすので好ましく
ない。 又、用いるブロツクイソシアネート化合物とレ
ゾール型フエノール樹脂の配合割合(重量比)は
95:5から5:95の範囲で用いられ好ましくは
85:15から30:70の範囲で用いられる。 ブロツクイソシアネートが多すぎると硬化が遅
くなり又、レゾール型フエノール樹脂が多すぎる
と砂型の崩壊性が悪くなる。 又、鋳物用樹脂被覆砂を製造する際にブロツク
イソシアネート化合物とレゾール型フエノール樹
脂の混合方法は特に限定するものでなく砂と撹拌
混合する前に両成分を予め混合していても又混合
時に別々に投入してもよい。 又本発明で用いる鋳物用砂としては通常鋳物用
に使用しているものはいずれでもよくジルコン
砂、オリビン砂も使用できる。 砂と混合し被覆する組成物中のブロツクイソシ
アネート化合物とレゾール型フエノール樹脂の合
計量は鋳物用砂に対して7.0醵0.3重量%であり好
ましくは3.0〜0.5重量%である。添加する樹脂合
計量が7%を越えると鋳物製造時のガス欠陥の原
因となるだけでなく価格も高くなりよくない。又
0.3%未満であると砂型の強度が低くなり実用に
耐えない。 又、本発明で得られた鋳物用樹脂被覆砂に従来
公知のブロツクイソシアネート化合物の解離触媒
のいずれも使用できジブチルチンジラウレート、
塩化第2スズナフテン酸コバルト等を添加しても
よく触媒の添加量は樹脂固形分に対し0.01〜1.0
重量%である。 又鋳物用樹脂被覆砂に流動性を良好にするため
にシエルモールド法で用いられているステアリン
酸カルシウムのような滑剤を添加してもよく、滑
剤の添加量は鋳物用砂に対して0.05〜0.2重量%
である。 以下本発明の実施例を示す。 実施例 1 (レゾール型フエノール樹脂の合成) 還流冷却器を備えつけた4つ口フラスコにビス
フエノールA2280g37%ホルマリン1620gを投入
し20%NaOH水溶液40gを添加し還流温度で2時
間反応させた後脱水濃縮を行ない固状樹脂が得ら
れた。 (鋳物用樹脂被覆砂の製造法) 混練機に160℃に加熱したフラタリー珪砂8Kg
にコロネートAPステーブル(日本ポリウレタン
社製、フエノールでマスクされたイソシアネート
化合物、軟化点約100℃)120gと上記で得られた
レゾール型フエノール樹脂40gを加えて砂が崩壊
するまで撹拌混合する。その後ステアリン酸カル
シウム8gを加え更に20秒間混合し鋳物用樹脂被
覆砂が得られた。 砂型特性を表−1に示す。 実施例 2 混練機に110℃に加熱したフラタリー珪砂8Kg
にコロネートAPステーブル100gとアセトン60g
からなる溶液と実施例1で得られたレゾール型フ
エノール樹脂100gとアセトン60gからなる溶液
を加えて砂が崩壊するまで撹拌混合する。その後
ステアリン酸カルシウム8gを加え更に20秒間混
合し、鋳物用樹脂被覆砂が得られた。 砂型特性を表−1に示す。 実施例 3 混練機に160℃に加熱したフラタリー珪砂8Kg
にクレランクロスリンキングエイジエントUT
(住友バイエルウレタン社製、ε−カプロラクタ
ムでマスクされたイソシアネート化合物、軟化点
約100℃)100gを加えて40秒撹拌混合した後実施
例1で得られたレゾール型フエノール樹脂60gと
メタノール30gからなる溶液を加えて砂が崩壊す
るまで撹拌混合する。その後ステアリン酸カルシ
ウム8gを加え更に20秒間混合し鋳物用樹脂被覆
砂が得られた。砂型特性を表−1に示す。 実施例 4 ジブチルチンジラウレート1.6gを添加した以
外は実施例3と同様にて鋳物用樹脂被覆砂が得ら
れた。砂型特性を表−1に示す。 比較例 1 (ノボラツク型フエノール樹脂の製造) 還流冷却器を備えつけた4つ口フラスコにフエ
ノール1880g37%ホルマリン244g、80%パラホ
ルムアルデヒド488gを投入しシユウ酸4gを添
加し還流温度で3時間反応させた後脱水濃縮を行
ない固状樹脂が得られた。 (鋳物用樹脂被覆砂の製造) 混練機に160℃に加熱したフラタリー珪砂8Kg
に上記で得られたノボラツク型フエノール樹脂
160gを加えて、40秒間撹拌混合した後ヘキサメ
チレンテトラミン24gと水80gからなる溶液を加
えて砂が崩壊するまで撹拌混合する。その後ステ
アリン酸カルシウム8gを加え更に20秒間混合し
鋳物用樹脂被覆砂が得られた。砂型特性を表−1
に示す。 比較例 2 混練機に160℃に加熱したフラタリー珪砂8Kg
にコロネートAPステーブル100gと比較例1で得
られたノボラツク型フエノール樹脂60gを加えて
砂が崩壊するまで撹拌混合する。その後ステアリ
ン酸カルシウム8gを加え更に20秒間混合し、鋳
物用樹脂被覆砂が得られた。砂型特性を表−1に
示す。 比較例 3 混練機に110℃に加熱したフラタリー珪砂8Kg
にコロネートAPステーブル100gとアセトン60g
からなる溶液とサンニツクスHS−207(三洋化成
工業社製、シユクローズ系ポリオール粘度約
170P/25℃)60gとアセトン30gからなる溶液
を加えて3分間混合した後ステアリン酸カルシウ
ム8gを加え更に20秒間混合し鋳物用樹脂被覆砂
が得られた。砂型特性を表−1に示す。
The present invention relates to thermosetting resin-coated sand for castings and a method for producing the same, and in particular, to reduce the collapsibility of molds after casting, which are mainly used for producing castings with relatively low casting temperatures, such as aluminum castings and alloy castings. The present invention relates to a significantly improved thermosetting resin-coated sand for foundries and a method for producing the same. Generally, the coating binder used for resin-coated sand for thermosetting castings is a resin obtained by reacting phenol and formaldehyde in an acidic or alkaline environment. When applied to a foundry sand mold with a low casting temperature, the mold has poor collapsibility and requires heat treatment at a high temperature of around 500°C for 6 to 12 hours, resulting in extremely large costs and labor for removing sand after casting. is becoming necessary. Therefore, a method of adding a halogen compound or a phosphorus compound to the phenolic resin has been proposed in order to improve the disintegration properties of the mold, but sufficient disintegration properties have not yet been obtained. In particular, recently there has been a call for energy savings, and there is a strong demand for thermosetting resin-coated sand for castings that reduces heat treatment and can perform operations equivalent to the current shell molding method. The inventor of the present invention has developed a resin-coated sand for foundry castings that requires less heat treatment after casting, disintegrates easily, and can perform the same work as the current shell molding method. By using resin-coated sand coated with a composition containing a compound and a resol-type phenolic resin, the disintegration properties after casting are significantly improved, and the work equivalent to the current shell molding method (sand fluidity, curing speed, etc.) is significantly improved. ) was found to be possible. That is, according to the present invention, when the thermosetting resin-coated sand for castings consisting of the above is filled into a mold heated to 150°C to 350°C, the blocking agent of the blocking isocyanate compound dissociates, and the generated isocyanate compound and resol are dissociated. The methylol groups, hydroxyl groups, etc. of the mold phenolic resin react, and the mold becomes strong due to urethane bonds, reaching a strength that allows it to be removed from the mold. Furthermore, the disintegration properties of the mold are significantly improved. This seems to be due to the use of urethane bonding in forming the template. As the blocking isocyanate compound in the composition used in the present invention, an addition reaction product of a polyisocyanate compound and an isocyanate blocking agent is used. As the polyisocyanate compound, any conventionally known isocyanate compound having two or more isocyanate groups can be used, and these polyisocyanate compounds and ethylene glycol, propylene glycol, trimethylolpropane, glycerin, and polyether polyols can be used. A terminal isocyanate group-containing compound obtained by reacting an active hydrogen compound such as is also used. As the isocyanate blocking agent, any conventionally used one can be used, including phenols such as phenol, cresol, and xylenol nonylphenol, tertiary alcohols such as t-butyl alcohol, acetylacetone, and malonic acid. Active methylene compounds such as diesters, aromatic amines such as methylaniline and diphenylamine, imides such as phthalic acid imide,
Examples include lactams such as ε-caprolactam, imines such as ethyleneimine, ureas, oximes, bisulfites, and boric acids. The blocked isocyanate compound used in the present invention can be obtained by reacting the above-mentioned isocyanate compound with an isocyanate blocking agent by a conventionally known method. The resol type phenolic resin used in the present invention is preferably a resol resin using bisphenols to maintain the dryness of sand, and more preferably one that is solid at room temperature. As the resol type phenol resin, any phenol resin having a methylol group can be used, and the synthesis of the resol type phenol resin is not particularly limited, but phenol, cresol, bisphenol A,
Phenols such as bisphenol S and bisphenol F and formaldehyde are mixed with NaOH and Ba.
It is obtained by a conventionally known method by reaction using a synthetic catalyst such as (OH) 2 , ammonia, or trimethylamine. As a resol type bisphenol resin,
A resin obtained by reacting bisphenols such as bisphenol A, bisphenol S, and bisphenol F with formaldehyde using a catalyst such as NaOH, Ba(OH) 2 ammonia, or trimethylamine is used. As a resol type bisphenol resin, formaldehyde is 1.5 to 1 mole of bisphenol A.
A resin obtained by reacting 4.0 mol is preferably used. If the amount of formaldehyde is less than 1.5 mol, the number of methylol groups will decrease and the curing rate will be slow, and if the amount of formaldehyde exceeds 4.0 mol, the odor of formaldehyde will become strong during heat curing of the sand mold, which is not preferable. The resin-coated sand for foundries of the present invention is produced by stirring and mixing a solid or solution blocking isocyanate compound and a solid or solution resol-type phenolic resin into foundry sand heated to 90 to 180°C. It is obtained by evaporating the corresponding solvent. When the temperature of the foundry sand exceeds 180° C., the blocked isocyanate compound begins to dissociate, which not only shortens the life of the foundry resin-coated sand but also reduces the strength of the sand mold, which is undesirable. Also the temperature is 90℃
Temperatures below this are not preferred because the resin coating becomes insufficient and the solvent evaporates insufficiently, lowering the melting point of the resin-coated sand for foundries and causing blocking. In addition, the blending ratio (weight ratio) of the blocked isocyanate compound and resol type phenol resin to be used is
Used in the range of 95:5 to 5:95, preferably
Used in the range of 85:15 to 30:70. If there is too much blocking isocyanate, curing will be delayed, and if there is too much resol type phenolic resin, the disintegrability of the sand mold will deteriorate. Furthermore, when producing resin-coated sand for foundries, there is no particular limitation on the method of mixing the blocked isocyanate compound and the resol-type phenolic resin, and even if the two components are mixed in advance before stirring and mixing with the sand, they may be mixed separately at the time of mixing. You can also put it in. Further, the foundry sand used in the present invention may be any of those commonly used for foundries, and zircon sand and olivine sand can also be used. The total amount of the blocking isocyanate compound and the resol type phenolic resin in the composition mixed with and coated with the sand is 7.0 to 0.3% by weight, preferably 3.0 to 0.5% by weight, based on the foundry sand. If the total amount of resin added exceeds 7%, it is not good because it not only causes gas defects during casting manufacturing but also increases the price. or
If it is less than 0.3%, the strength of the sand mold will be too low to be of practical use. Furthermore, any of the conventionally known dissociation catalysts for blocked isocyanate compounds can be used for the foundry resin-coated sand obtained in the present invention, such as dibutyl tin dilaurate,
Cobalt stannic chloride naphthenate, etc. may be added, and the amount of catalyst added is 0.01 to 1.0 based on the resin solid content.
Weight%. In addition, a lubricant such as calcium stearate used in the shell mold method may be added to the resin-coated sand for foundries to improve fluidity, and the amount of the lubricant added is 0.05 to 0.2 to the foundry sand. weight%
It is. Examples of the present invention will be shown below. Example 1 (Synthesis of resol type phenolic resin) 2280 g of bisphenol A and 1620 g of 37% formalin were put into a four-necked flask equipped with a reflux condenser, 40 g of 20% NaOH aqueous solution was added, and the mixture was reacted at reflux temperature for 2 hours, followed by dehydration and concentration. A solid resin was obtained. (Production method of resin-coated sand for foundries) 8 kg of flattery silica sand heated to 160℃ in a kneader
Add 120 g of Coronate AP Stable (manufactured by Nippon Polyurethane Co., Ltd., phenol-masked isocyanate compound, softening point: approximately 100°C) and 40 g of the resol type phenolic resin obtained above, and stir and mix until the sand disintegrates. Thereafter, 8 g of calcium stearate was added and mixed for an additional 20 seconds to obtain resin-coated foundry sand. Table 1 shows the characteristics of the sand mold. Example 2 8 kg of flattery silica sand heated to 110°C in a kneader
100g of Coronate AP Stable and 60g of acetone
A solution consisting of 100 g of the resol type phenolic resin obtained in Example 1 and 60 g of acetone was added and mixed with stirring until the sand disintegrated. Thereafter, 8 g of calcium stearate was added and mixed for an additional 20 seconds to obtain resin-coated foundry sand. Table 1 shows the characteristics of the sand mold. Example 3 8 kg of flattery silica sand heated to 160°C in a kneader
Clelan Cross Linking Agent UT
(Manufactured by Sumitomo Bayer Urethane Co., Ltd., isocyanate compound masked with ε-caprolactam, softening point approximately 100°C) After adding 100g and stirring and mixing for 40 seconds, 60g of the resol type phenolic resin obtained in Example 1 and 30g of methanol were added. Add the solution and mix until the sand is broken down. Thereafter, 8 g of calcium stearate was added and mixed for an additional 20 seconds to obtain resin-coated foundry sand. Table 1 shows the characteristics of the sand mold. Example 4 Resin-coated sand for foundries was obtained in the same manner as in Example 3, except that 1.6 g of dibutyltin dilaurate was added. Table 1 shows the characteristics of the sand mold. Comparative Example 1 (Production of novolac type phenolic resin) 1880 g of phenol, 244 g of 37% formalin, and 488 g of 80% paraformaldehyde were put into a four-necked flask equipped with a reflux condenser, 4 g of oxalic acid was added, and the mixture was reacted at reflux temperature for 3 hours. After dehydration and concentration, a solid resin was obtained. (Manufacture of resin-coated sand for foundries) 8 kg of flattery silica sand heated to 160℃ in a kneader
The novolak type phenolic resin obtained above
After adding 160 g and stirring and mixing for 40 seconds, a solution consisting of 24 g of hexamethylenetetramine and 80 g of water was added and mixed with stirring until the sand disintegrated. Thereafter, 8 g of calcium stearate was added and mixed for an additional 20 seconds to obtain resin-coated foundry sand. Table 1: Sand mold characteristics
Shown below. Comparative Example 2 8 kg of flattery silica sand heated to 160℃ in a kneader
100 g of Coronate AP Stable and 60 g of the novolak type phenolic resin obtained in Comparative Example 1 were added to the mixture, and the mixture was stirred and mixed until the sand disintegrated. Thereafter, 8 g of calcium stearate was added and mixed for an additional 20 seconds to obtain resin-coated foundry sand. Table 1 shows the characteristics of the sand mold. Comparative Example 3 8 kg of flattery silica sand heated to 110℃ in a kneader
100g of Coronate AP Stable and 60g of acetone
A solution consisting of Sannix HS-207 (manufactured by Sanyo Chemical Industries, Ltd., Sucrose polyol with a viscosity of approx.
A solution consisting of 60 g of 170P/25°C) and 30 g of acetone was added and mixed for 3 minutes, then 8 g of calcium stearate was added and mixed for a further 20 seconds to obtain resin-coated sand for foundry use. Table 1 shows the characteristics of the sand mold.

【表】 本発明で得られた加熱硬化型鋳物用樹脂被覆砂
は砂の流動性、砂型の硬化速度及び砂型の崩壊性
に優れている。
[Table] The thermosetting resin-coated sand for foundries obtained in the present invention is excellent in sand fluidity, sand mold hardening speed, and sand mold disintegration property.

Claims (1)

【特許請求の範囲】 1 鋳物用砂にブロツクイソシアネート化合物と
レゾール型フエノール樹脂を含有する組成物を被
覆したことを特徴とする加熱硬化型鋳物用樹脂被
覆砂。 2 レゾール型フエノール樹脂がレゾール型ビス
フエノール樹脂であることを特徴とする特許請求
の範囲第1項記載の加熱硬化型鋳物用樹脂被覆
砂。 3 レゾール型ビスフエノール樹脂がビスフエノ
ールA1モルに対してホルムアルデヒド1.5〜4.0モ
ルを反応させて得られる樹脂であることを特徴と
する特許請求の範囲第2項記載の加熱硬化型鋳物
用樹脂被覆砂。 4 (a)90〜180℃に加熱した鋳物用砂と(b)ブロツ
クイソシアネート化合物と(c)レゾール型フエノー
ル樹脂を撹拌混合することを特徴とする加熱硬化
型鋳物用樹脂被覆砂の製造方法。 5 ブロツクイソシアネート化合物が常温で固形
であることを特徴とする特許請求の範囲第4項記
載の加熱硬化型鋳物用樹脂被覆砂の製造方法。 6 レゾール型フエノール樹脂が常温で固形であ
ることを特徴とする特許請求の範囲第4項記載の
加熱硬化型鋳物用樹脂被覆砂の製造方法。 7 レゾール型フエノール樹脂がレゾール型ビス
フエノール樹脂であることを特徴とする特許請求
の範囲第4項又は第6項記載の加熱硬化型鋳物用
樹脂被覆砂の製造方法。 8 レゾール型ビスフエノール樹脂がビスフエノ
ールA1モルに対してホルムアルデヒド1.5〜4.0モ
ルを反応させて得られる樹脂であることを特徴と
する特許請求の範囲第7項記載の加熱硬化型鋳物
用樹脂被覆砂の製造方法。
[Scope of Claims] 1. Resin-coated sand for thermosetting foundries, characterized in that foundry sand is coated with a composition containing a blocked isocyanate compound and a resol type phenolic resin. 2. The resin-coated sand for thermosetting castings according to claim 1, wherein the resol type phenolic resin is a resol type bisphenol resin. 3. Resin-coated sand for thermosetting castings according to claim 2, wherein the resol-type bisphenol resin is a resin obtained by reacting 1.5 to 4.0 moles of formaldehyde with 1 mole of bisphenol A. . 4. A method for producing thermosetting resin-coated foundry sand, which comprises stirring and mixing (a) foundry sand heated to 90 to 180°C, (b) a blocked isocyanate compound, and (c) a resol type phenolic resin. 5. The method for producing thermosetting resin-coated sand for foundries according to claim 4, wherein the blocked isocyanate compound is solid at room temperature. 6. The method for producing thermosetting resin-coated sand for castings according to claim 4, wherein the resol type phenolic resin is solid at room temperature. 7. The method for producing resin-coated sand for thermosetting castings according to claim 4 or 6, wherein the resol type phenolic resin is a resol type bisphenol resin. 8. Resin-coated sand for thermosetting castings according to claim 7, wherein the resol type bisphenol resin is a resin obtained by reacting 1.5 to 4.0 moles of formaldehyde with 1 mole of bisphenol A. manufacturing method.
JP15935183A 1983-08-31 1983-08-31 Resin-coated molding sand curable by heating and its production Granted JPS6049829A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP15935183A JPS6049829A (en) 1983-08-31 1983-08-31 Resin-coated molding sand curable by heating and its production

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP15935183A JPS6049829A (en) 1983-08-31 1983-08-31 Resin-coated molding sand curable by heating and its production

Publications (2)

Publication Number Publication Date
JPS6049829A JPS6049829A (en) 1985-03-19
JPS6258809B2 true JPS6258809B2 (en) 1987-12-08

Family

ID=15691945

Family Applications (1)

Application Number Title Priority Date Filing Date
JP15935183A Granted JPS6049829A (en) 1983-08-31 1983-08-31 Resin-coated molding sand curable by heating and its production

Country Status (1)

Country Link
JP (1) JPS6049829A (en)

Also Published As

Publication number Publication date
JPS6049829A (en) 1985-03-19

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