JPS6119329B2 - - Google Patents
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- Publication number
- JPS6119329B2 JPS6119329B2 JP15615481A JP15615481A JPS6119329B2 JP S6119329 B2 JPS6119329 B2 JP S6119329B2 JP 15615481 A JP15615481 A JP 15615481A JP 15615481 A JP15615481 A JP 15615481A JP S6119329 B2 JPS6119329 B2 JP S6119329B2
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- Prior art keywords
- sand
- coated
- resin
- coated sand
- present
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Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B22—CASTING; POWDER METALLURGY
- B22C—FOUNDRY MOULDING
- B22C1/00—Compositions of refractory mould or core materials; Grain structures thereof; Chemical or physical features in the formation or manufacture of moulds
- B22C1/16—Compositions 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
- B22C1/20—Compositions 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
- B22C1/22—Compositions 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
- B22C1/2233—Compositions 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
- B22C1/2246—Condensation polymers of aldehydes and ketones
- B22C1/2253—Condensation polymers of aldehydes and ketones with phenols
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- 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】
本発明は、温時の鋳型強度が大きくかつ溶融金
属の注湯時の鋳型の熱崩壊性が良好である鋳造用
中子に好適な樹脂被覆砂に関する。
従来より鋳型成型、特に鋳造用中子の成型には
ノボラツク型又はレゾール型のフエノールホルム
アルデヒド樹脂を被覆した樹脂被覆砂が多用され
ているが、アルミニウム合金等の低温溶融金属の
鋳造においては、中子が十分熱崩壊しない為に排
砂が困難であり、排砂の為の鋳造品の後加熱(砂
焼き)を要し、省エネルギー、省力化の観点から
大巾な改善が望まれている。かかる観点から、
種々の熱崩壊性に優れた樹脂被覆砂の開発が試み
られているが、これを満足しても中子の造型直後
の温時強度が十分なものが得られず新しい粘結剤
の出現が望まれている。
本発明はかかる従来技術の欠点を大巾に改善
し、温時の鋳型強度が大きく。かつ熱崩壊性にす
ぐれ特にアルミニウム合金等の鋳造に好適な樹脂
被覆砂を提供するものである。
すなわち、本発明の1つは、
(A) トリグリシジルイソシアヌレートおよび/又
はトリ(βメチルグリシジル)イソシアヌレー
トと、
(B) ジシアンジアミド、ジシアンジアミド誘導
体、有機酸ヒドラジド又はイミダゾール誘導体
の1種以上と、
(C) フエノールホルムアルデヒド樹脂と、
を結合剤として被覆してなる樹脂被覆砂であ
り、他の1つの本発明は、
(A) トリグリシジルイソシアヌレートおよび/又
はトリ(βメチルグリシジル)イソシアヌレー
トと、
(B) ジシアンジアミド、ジシアンジアミド誘導
体、有機酸ヒドラジド又はイミダゾール誘導体
の1種以上と、
(C) フエノールホルムアルデヒド樹脂と、
(D) ヘキサメチレンテトラミンと、
を結合剤として被覆してなる樹脂被覆砂である。
ジグリシジルイソシアヌレート、ジ(βメチル
グリシジル)イソシアヌレートも使用可能であ
り、またトリグリシジルイソシアヌレート或いは
トリ(βメチルグリシジル)イソシアヌレートと
多価カルボン酸或いは多価フエノール等の付加反
応によつて得られる1分子中に2個以上のグリシ
ジル基を有するオリゴマーや以上から選ばれる2
種以上の混合物の使用も可能である。
本発明に用いられる(B)は、前記の(A)イソシアヌ
ル環を有する多価グリシジル化合物とは常温では
反応せず、加温時に短時間で反応をする硬化剤で
あり、通常は150℃以上の温度で数分以内にグリ
シジル基との反応を完結し得る硬化剤である。
上記の(B)としては、例えばジシアンジアミド、
グアニジン、グアニジン塩、ビグアニド、グアニ
ジン若しくはビグアニドのアリール基置換体のよ
うなジシアンジアミド系の各種誘導体、例えばコ
ハク酸ジヒドラジド、アジピン酸ジヒドラジド、
イソフタル酸ジヒドラジド、パラオキシ安息香酸
ジヒドラジド、サリチル酸ジヒドラジド、フエニ
ルアミノプロピオン酸ジヒドラジドのような有機
酸ジヒドラジド、例えばシアノエチル置換イミダ
ゾール有機酸塩、アジン置換イミダゾール、イミ
ダゾールの金属塩等のイミダゾール誘導体、等が
あり、これらの1種以上を用いることができる。
これらの化合物が温時の鋳型強度と崩壊性の観点
から使用できる。
更に上記の(A)イソシアヌル環を有する多価グリ
シジル化合物と上記の(B)硬化剤と鋳型造型時の反
応速度を調整する為に硬化促進剤を併用しても良
く、例えばジメチルアミノフエノールのようなア
ミノフエノール、ジアザビシクロウンデセン及び
その塩、3(p−クロロフエニル)−1,1−ジ
メチル尿素のような尿素誘導体等が硬化促進剤と
して用いられ、更に硬化剤としても作用するイミ
ダゾール誘導体及び有機酸ジヒドラジドはジシア
ンジアミド誘導体の硬化促進剤としても有効であ
る。中でも上記尿素誘導体が効果的である。
上記の(A)及び(B)からなる成分を被覆した樹脂被
覆砂は、中子等の鋳型成型した際の熱間強度に優
れ、また熱崩壊性も良好であるが湿度の高い環境
において樹脂被覆砂を貯蔵すると、砂同志の滑り
が悪くなりこれから得た鋳型の密度が低下して強
度低下を起したり、また細部への砂づまりが悪く
なつて不良率が増大するという欠点がある。
本発明では、かかる前記(A)及び(B)の成分に、(C)
フエノールホルムアルデヒド樹脂及び必要に応じ
前記(C)の硬化剤としての機能を有する(D)ヘキサメ
チレンテトラミンを加えることによつて上記した
欠点を克服し、いかなる貯蔵条件においても安定
しした鋳型の強度を維持し、かつ実用に十分な熱
崩壊性を実現することができた。
本発明に用いられる(C)フエノールホルムアルデ
ヒド樹脂は、フエノール、クレゾール、キシレノ
ール、パラターシヤリーブチルフエノール、カテ
コール、レゾルシノール、フエニルフエノール、
ビスフエノールA、ビスフエノールF、ビスフエ
ノールS、イソプロペニルフエノール等のモノフ
エノール化合物又はジフエノール化合物とホルム
アルデヒドとの縮合によつて得られる樹脂であつ
て、大別してノボラツク型フエノールホルムアル
デヒド樹脂とレゾール型フエノールホルムアルデ
ヒド樹脂に分類され、そのいずれも本発明に用い
ることができる。
前記の(C)フエノールホルムアルデヒド樹脂がノ
ボラツク型フエノールホルムアルデヒド樹脂であ
る場合には、前記の(D)が用いられる。前記の(C)フ
エノールホルムアルデヒド樹脂がレゾール型フエ
ノールホルムアルデヒド樹脂である場合には、自
己硬化性を有するので(D)は不要である。しかし、
レゾール型フエノールホルムアルデヒド樹脂を用
いる場合には、鋳型造型時の反応速度を速める為
に、例えば安息香酸、アセチル安息香酸、ヒドロ
キシ安息香酸、シユウ酸、コハク酸、パラトルエ
ンスルフオン酸、ドデシルベンゼンスルフオン
酸、アルキル燐酸等の有機酸を反応促進剤として
用いることも可能である。
本発明に用いられる前記(A)〜(D)の各成分の割合
は、全合計量を100重量%とした時(A)及び(B)の合
計量が10〜95重量%、(C)及び(D)の合計量が90〜5
重量%、好ましくは(A)及び(B)の合計量が25〜80重
量%に対し(C)及び(D)の合計量が75〜20重量%、特
に好ましく(A)及び(B)の合計量が35〜70重量%に対
し(C)及び(D)の合計量が65〜30重量%であることが
本発明の効果の達成のためによい。また、(A)及び
(B)の配合割合は、(B)の硬化剤の種類や鋳型造型温
度により最適値が異なるが、(A)の多価グリシジル
化合物の数に対し、(B)硬化剤の反応可能な活性水
素基が0.5〜4.0倍当量、好ましくは1.0〜2.5倍当
量となるような配合割合で通常用いられる。(C)及
び(D)の配合割合は、(C)がノボラツク型である場合
には(C)+(D)の合計量を100重量%とした時、(C)が
80〜95重量%に対し(D)は20〜5重量%の割合で通
常用いられ、又、レゾール型である場合には通常
D硬化剤は使用しない。本発明の樹脂被覆砂の前
記各成分(A)〜(D)の合計量は、砂に対し通常1〜10
重量%、好ましくは1.5〜4重量%で用いられ
る。
本発明の前記各成分(A)〜(D)は、有機溶剤又は水
に溶解及び/又は懸濁して常温で砂に混合してか
ら乾燥することにより砂を被覆するともできる
が、特に主要成分である(A)及び(C)は、通常150〜
200℃に予熱した砂に固型の状態で添加し、溶融
させて砂に被覆することが望ましい。
前記各成分で被覆された本発明の被覆砂を得る
方法としては、
() 個々の砂粒に(A),(B),(C)全てを被覆する
方法、
() 1方の砂粒に(A)と(B),他の砂粒に(C)を被
覆してから双方の砂粒を混合する方法、
() 1方の砂粒に(A),他方の砂粒に(B)と(C)を
被覆してから双方の砂粒を混合する方法、
() (A),(B)及び(C)を各々単独で砂粒に被覆し
てからこれら砂粒を混合する方法、
等がある。また(D)を更に用いる場合には、上記に
加え種々の方法を採用することができ、例えば前
記()及び()の方法において(D)の少なくと
も一部分を一方の砂に、残余の部分を他方の砂に
被覆すればよいが、通常は何れか一方の砂に与え
れば充分である。前述の(A)と(B)に対する硬化促進
剤や(C)の反応促進を用いる場合も同様であるが、
前者は(A)被覆の砂粒とは別の砂粒、後者は(C)被覆
の砂粒とは別の砂粒に被覆してから両方の砂粒を
混合する方が、本発明の目的達成に都合のよいこ
とが多い。
但し、()の方法においては、各成分(A)〜(D)
の添加順序は任意であるが、予熱した砂との混合
過程において(A)及び(C)が相互に反応することがな
いよう短時間に冷却しながら添加混合を行うこと
が特に必要である。尚硬化剤成分である前記(B)及
び(D)は量的に少ないので均一混合の観点から、通
常は水又は有機溶剤に溶解又は懸濁して(A)や(C)を
被覆した後に添加混合し乾燥するのが一般的であ
る。
また、本発明の樹脂被覆砂には、前記しした(A)
〜(D)の成分の他に、前記した各種の硬化促進剤や
反応促進剤は勿論のこと、例えば(A)とは異なる構
造の多価エポキシ樹脂、キシレン樹脂、クマロン
樹脂、石油樹脂、ポリエステル樹脂等の他の樹脂
を本発明の目的を阻害しない範囲で混合使用する
ことも可能であり、また鋳砂のすべり性や金型か
らの脱型性を改良する助剤類、砂と各樹脂成分の
接着性を向上させる例えばシランカツプリング
剤、チタンカツプリング剤等の接着向上剤或いは
砂以外の充填剤の併用も可能である。
このようにして得られた本発明の樹脂被覆砂
は、通常150℃以上、好ましくは180℃〜300℃に
加熱された金型に充され、30秒〜3分間放置後脱
型し中子等の鋳型を得る。かくして得られた鋳型
は、樹脂被覆砂の貯蔵条件によらず安定した優れ
た温時の鋳型強度を有するので上記の鋳型作成時
の不良率が極めて低く、加えてアルミ等の軽合金
鋳物の中子に用いても熱崩壊性が優れているので
排砂の為の砂焼き工程が全く不要となる。
以下、実施例を示し、本発明を具体的に説明す
る。
樹脂被覆砂の製造:
実施例 1
200℃に余熱した6号硅砂1Kgを冷却可能なジ
ヤケツト付撹拌混合槽に入れ、冷却しながら撹拌
を行い、180℃でノボラツク型フエノールホルム
アルデヒド樹脂(軟化点85℃)13gを加え、次い
で140℃においてトリグリシジルイソシアヌレー
ト8gを加え急冷後、100℃にてジシアンジアミ
ド2g及びヘキサメチレンテトラミン2gを10g
の水に分散、溶解して添加混合し、冷却、乾燥し
た後混合槽より排出して本発明の樹脂被覆砂(1)を
得た。
実施例 2
実施例1と同様な装置を用い、予熱した6号硅
砂1Kgに対し160℃において固型のレゾール型フ
エノールホルムアルデヒド樹脂(軟化点84℃)8
gを加えて冷却撹拌し、140℃にてトリ(βメチ
ルグリシジル)イソシアヌレート15gを加えて急
冷後90℃にてアジピン酸ジヒドラジドの微粉末2
gを5gのメタノールに懸濁して添加混合し、冷
却、乾燥しした後混合槽より排出して本発明の樹
脂被覆砂(2)を得た。
実施例 3
実施例1と同様な装置を用い、予熱した6号硅
砂1Kgに対し、180℃でトリグリシジルイソシア
ヌレート20gを加えて撹拌冷却し、100℃にてジ
シアンジアミド5gを10c.c.の水に分散して添加混
合し、冷却、乾燥後排砂し、被覆砂(3A)を得
た。
一方、同様に予熱した6号硅砂1Kgに対し、
180℃にてノボラツク型フエノールホルムアルデ
ヒド樹脂(軟化点85℃)22gを加えて撹拌冷却
し、100℃にてヘキサメチレンテトラミン3gを
10gの水に溶解して添加混合し、冷却、乾燥後排
砂し、被覆砂(3B)を得た。
上記の被覆砂(3A)500gと上記の被覆(3B)
500gとを混合し、本発明の樹脂被覆砂(3)を得
た。
実施例 4
実施例1と同様な装置を用い、予熱した6号硅
砂1Kgに対し160℃において固型のレゾール型フ
エノールホルムアルデヒド樹脂(軟化点84℃)25
gを加えて速やかに冷却撹拌し排砂して被覆砂
(4B)を得た。
前記実施例3で得た被覆砂(3A)350gと上記
の被覆砂(4B)650gとを混し本発明の樹脂被覆
砂(4)を得た。
実施例 5
実施例1と同様な装置を用い予熱した6号硅砂
1Kgに対、160℃にてトリグリシジルイソシアヌ
レート22gを添加し、100℃に冷却してヘキサメ
チレンテトラミン3gを10gの水に溶解して添
加、混合し、冷却、乾燥後排して被覆砂(5A)
を得た。
一方、同様にして予熱した6号硅砂1Kgに対し
180℃にてノボラツク型フエノールホルムアルデ
ヒド樹脂(軟化点96℃)22gを添し、110℃に冷
却後フエニルビグアニド3gを添加混合し、冷却
後排して被覆砂(5B)を得た。
上記の被覆砂(5A)600gと被覆砂(5B)400
gを混合して本発明の樹脂被覆砂(5)を得た。
実施例 6
実施例1と同様な装置を用い、予熱した6号硅
砂1Kgに対し170℃にてトリグリシジルイソシア
ヌレート2モルとイソフタル酸1モの反応付加物
23gを添加し、100℃に冷却後ヘキサメチレンテ
トラミン3gと1−シアノエチル−2−エチル−
4−メチルイミダゾールトリメリテート2gを10
gの水に分散溶解して添加混合し、冷却、乾燥後
排砂して被覆砂(6A)を得た。
一方、同様に予熱した6号硅砂1Kgに対し、
170℃にてノボラツク型フエノールホルムアルデ
ヒド樹脂(軟化点76℃)22gを添加混合して冷却
後排砂して被覆砂(6B)を得た。
上記の被覆砂(6A)500gと被覆砂(6B)500
gとを混合して本発明の樹脂被覆砂(6)を得た。
実施例 7
実施例1と同様な装置を用いて予熱した6号硅
砂1Kgに対し、トリグリシジルイソシアヌレート
21gを160℃で添加混合し冷却後排砂して被覆砂
(7A)を得た。
一方、同様に予熱した6号硅砂1Kgに対しレゾ
ール型フエノールホルムアルデヒド樹脂(軟化点
78℃)25gを160℃で添加混合し冷却して、100℃
にて3gのグアニジン炭酸塩を10gの水に分散し
て添加混合し、冷却、乾燥後排砂して被覆砂
(7B)を得た。
上記の被覆(7A)500gと被覆砂(7B)500g
とを混して本発明の樹脂被覆砂(7)を得た。
実施例 8
実施例1と同様な装置を用いて予熱した6号硅
砂1Kgに対し、ノボラツク型フエノールホルムア
ルデヒド樹脂(軟化点85℃)22gを180℃で添加
混合し冷却して、100℃にて、ジシアンジアミド
4g、ヘキサメチレンテトラミン3gを10gの水
に分散溶解せしめて添加し、混合し、冷却、乾燥
後排砂して被覆砂(8B)を得た。
実施例7で製造した被覆砂(7A)500gと上記
の被覆砂(8B)500gとを混合し、本発明の樹脂
被覆砂(8)を得た。
比較例 1
実施例3で製造した被覆砂(3A)を比較試験
用の樹脂被覆砂(i)とした。
比較例 2
実施例3で製造した被覆砂(3B)を比較試験
用の樹脂被覆砂(ii)とした。
樹脂被覆砂の評価:
前記した本発明の樹脂被覆砂(1)〜(8)及び比較例
である樹脂被覆砂(i)及び(ii)に関し、下記の項目に
関し評価を行つた。
(イ) 温時強度の測定
上記の各被覆砂を高温引張試験機を用い230℃
90秒で成型し、直ちに230℃の温度下での温時抗
張力を測定した。
(ロ) 樹脂被覆砂貯蔵後の温時強度の測定
上記の各被覆砂を40℃95%相対湿度の環境試験
器中に1週間放置後、上記(イ)と同様にして温時抗
張力を測定した。
(ハ) 熱崩壊性試験
上記の各被覆砂を250℃に予熱した内径30mm、
高さ30mmの円筒状金型に流しこみ60秒加熱後脱型
して中子を作成し、ベントナイト系生型で別途作
成した内径70mm深70mmの円筒状主型に直径10mmの
中子砂の排出口をとりつけて、上記中子をセツト
し、650℃のアルミニウム軽合溶融物を注湯して
冷却凝固させた後、主型を壊し、ロータツプ試験
機により5分間振動を与えて、アルミニウム軽合
金鋳物の排出口からの中子の排砂重量%を測定し
た。
上記(イ)、(ロ)及び(ハ)の評価試験の結果を表1に記
載する。
【表】DETAILED DESCRIPTION OF THE INVENTION The present invention relates to resin-coated sand suitable for casting cores, which has high mold strength when hot and has good thermal disintegration properties when pouring molten metal. Traditionally, resin-coated sand coated with novolac type or resol type phenol formaldehyde resin has been widely used for mold molding, especially for molding cores for casting, but when casting low-temperature melting metals such as aluminum alloys, cores It is difficult to remove the sand because it does not thermally disintegrate sufficiently, and the cast product must be heated (sand baked) after sand removal to remove the sand.Therefore, drastic improvements are desired from the viewpoint of energy and labor saving. From this point of view,
Attempts have been made to develop various types of resin-coated sand with excellent thermal decomposition properties, but even if these methods are met, it is not possible to obtain a material with sufficient hot strength immediately after core molding, and new binders have not yet been developed. desired. The present invention greatly improves the drawbacks of the prior art, and increases the strength of the mold when hot. The present invention also provides a resin-coated sand that has excellent thermal decomposition properties and is particularly suitable for casting aluminum alloys and the like. That is, one of the present inventions includes (A) triglycidyl isocyanurate and/or tri(β-methylglycidyl)isocyanurate, (B) one or more of dicyandiamide, dicyandiamide derivative, organic acid hydrazide, or imidazole derivative; C) phenol formaldehyde resin; Another aspect of the present invention is resin-coated sand coated with (A) triglycidyl isocyanurate and/or tri(β-methylglycidyl) isocyanurate, and ( B) one or more of dicyandiamide, a dicyandiamide derivative, an organic acid hydrazide, or an imidazole derivative; (C) a phenol formaldehyde resin; and (D) hexamethylenetetramine. It is a resin-coated sand coated with the following as a binder. Diglycidyl isocyanurate and di(β-methylglycidyl)isocyanurate can also be used, and those obtained by addition reaction of triglycidyl isocyanurate or tri(β-methylglycidyl)isocyanurate with polyhydric carboxylic acid or polyhydric phenol, etc. Oligomers having two or more glycidyl groups in one molecule and two or more glycidyl groups selected from the above.
It is also possible to use mixtures of more than one species. (B) used in the present invention is a curing agent that does not react with the above-mentioned (A) polyvalent glycidyl compound having an isocyanuric ring at room temperature, but reacts in a short time when heated, and is usually at temperatures above 150°C. It is a curing agent that can complete the reaction with glycidyl groups within several minutes at a temperature of . Examples of (B) above include dicyandiamide,
Various dicyandiamide derivatives such as guanidine, guanidine salts, biguanides, aryl group substituted products of guanidine or biguanides, such as succinic acid dihydrazide, adipic acid dihydrazide,
Organic acid dihydrazides such as isophthalic acid dihydrazide, paraoxybenzoic acid dihydrazide, salicylic acid dihydrazide, and phenylaminopropionic acid dihydrazide, imidazole derivatives such as cyanoethyl-substituted imidazole organic acid salts, azine-substituted imidazole, and imidazole metal salts, etc. One or more of these can be used.
These compounds can be used from the viewpoints of mold strength and disintegration at elevated temperatures. Furthermore, a curing accelerator may be used in combination with the above (A) polyvalent glycidyl compound having an isocyanuric ring and the above (B) curing agent in order to adjust the reaction rate during mold making, such as dimethylaminophenol. Aminophenol, diazabicycloundecene and its salts, urea derivatives such as 3(p-chlorophenyl)-1,1-dimethylurea, etc. are used as curing accelerators, and imidazole derivatives and Organic acid dihydrazide is also effective as a curing accelerator for dicyandiamide derivatives. Among these, the above-mentioned urea derivatives are effective. Resin-coated sand coated with the components (A) and (B) above has excellent hot strength when molded into cores, etc., and also has good thermal disintegration properties, but resin-coated sand coated with the components (A) and (B) above has excellent hot strength when molded into cores, etc., and has good thermal disintegration properties. When coated sand is stored, there are drawbacks such as poor sliding between the sands, resulting in a decrease in the density and strength of the mold obtained from the sand, and an increase in the defective rate due to poor sand clogging in the details. In the present invention, in the above-mentioned components (A) and (B), (C)
By adding phenol formaldehyde resin and optionally (D) hexamethylenetetramine which functions as a curing agent as in (C) above, the above-mentioned drawbacks can be overcome and the strength of the mold can be stabilized under any storage conditions. We were able to maintain this property and achieve a thermal disintegration property sufficient for practical use. (C) Phenol formaldehyde resin used in the present invention includes phenol, cresol, xylenol, paratertiary butylphenol, catechol, resorcinol, phenylphenol,
A resin obtained by condensation of a monophenol compound or a diphenol compound such as bisphenol A, bisphenol F, bisphenol S, or isopropenylphenol with formaldehyde, which can be roughly divided into novolac type phenol formaldehyde resin and resol type phenol formaldehyde resin. It is classified as a resin, and any of them can be used in the present invention. When the phenol formaldehyde resin (C) above is a novolak type phenol formaldehyde resin, the above (D) is used. When the above-mentioned (C) phenol formaldehyde resin is a resol type phenol formaldehyde resin, (D) is not necessary because it has self-curing properties. but,
When using resol type phenol formaldehyde resin, in order to accelerate the reaction rate during mold making, for example, benzoic acid, acetylbenzoic acid, hydroxybenzoic acid, oxalic acid, succinic acid, p-toluenesulfonic acid, dodecylbenzenesulfonate. It is also possible to use organic acids such as acids and alkyl phosphoric acids as reaction promoters. The ratio of each component (A) to (D) used in the present invention is such that the total amount of (A) and (B) is 10 to 95% by weight, when the total amount is 100% by weight, and (C) and the total amount of (D) is 90-5
% by weight, preferably the total amount of (A) and (B) is 25-80% by weight, and the total amount of (C) and (D) is 75-20% by weight, particularly preferably (A) and (B). In order to achieve the effects of the present invention, it is preferable that the total amount of (C) and (D) be 65 to 30% by weight relative to the total amount of 35 to 70% by weight. Also, (A) and
The optimal blending ratio of (B) varies depending on the type of curing agent in (B) and the molding temperature, but the reactive activity of the curing agent in (B) is based on the number of polyvalent glycidyl compounds in (A). It is usually used at a blending ratio such that the amount of hydrogen groups is 0.5 to 4.0 times equivalent, preferably 1.0 to 2.5 times equivalent. The blending ratio of (C) and (D) is, if (C) is a novolak type, when the total amount of (C) + (D) is 100% by weight, (C) is
(D) is usually used in a proportion of 20 to 5% by weight relative to 80 to 95% by weight, and in the case of a resol type, usually no D curing agent is used. The total amount of each of the components (A) to (D) in the resin-coated sand of the present invention is usually 1 to 10% of the sand.
It is used in an amount of 1.5 to 4% by weight, preferably 1.5 to 4% by weight. Each of the above-mentioned components (A) to (D) of the present invention can be dissolved and/or suspended in an organic solvent or water, mixed with the sand at room temperature, and then dried to coat the sand, but in particular, the main components (A) and (C) are usually 150 to
It is desirable to add it in a solid state to sand preheated to 200°C, melt it, and coat the sand. Methods for obtaining the coated sand of the present invention coated with each of the above-mentioned components include () a method in which each sand grain is coated with all of (A), (B), and (C); () a method in which one sand grain is coated with (A); ) and (B), the other sand grain is coated with (C), and then both sand grains are mixed. () One sand grain is coated with (A), and the other sand grain is coated with (B) and (C). (A), (B), and (C) are individually coated on the sand grains, and then these sand grains are mixed. In addition, when (D) is further used, various methods can be adopted in addition to the above. For example, in the methods () and () above, at least a part of (D) is added to one of the sands, and the remaining part is added to the sand. Although it is sufficient to coat the other sand, it is usually sufficient to apply it to either one of the sands. The same applies when using a curing accelerator for (A) and (B) mentioned above or a reaction accelerator for (C),
It is more convenient for the purpose of the present invention to achieve the purpose of the present invention if the former is coated on (A) a different sand grain from the coated sand grain, and the latter is coated on a different sand grain from the coated sand grain (C), and then both sand grains are mixed. There are many things. However, in the method (), each component (A) to (D)
Although the order of addition of (A) and (C) is arbitrary, it is particularly necessary to perform the addition and mixing while cooling for a short time so that (A) and (C) do not react with each other during the mixing process with preheated sand. Since the curing agent components (B) and (D) are small in quantity, from the viewpoint of uniform mixing, they are usually dissolved or suspended in water or an organic solvent and added after coating (A) and (C). It is common to mix and dry. In addition, the resin-coated sand of the present invention also includes the above-mentioned (A).
In addition to the components (D), there are of course the various curing accelerators and reaction accelerators mentioned above, such as polyvalent epoxy resins, xylene resins, coumaron resins, petroleum resins, and polyesters with a structure different from that of (A). It is also possible to mix and use other resins such as resins within a range that does not impede the purpose of the present invention, and it is also possible to use auxiliary agents, sand and various resins that improve the slipperiness of casting sand and the ease with which it can be removed from molds. It is also possible to use adhesion promoters such as silane coupling agents and titanium coupling agents, or fillers other than sand, to improve the adhesion of the components. The resin-coated sand of the present invention thus obtained is filled into a mold heated to usually 150°C or higher, preferably 180°C to 300°C, and after being left for 30 seconds to 3 minutes, the mold is removed and a core etc. Obtain a mold. The mold thus obtained has stable and excellent mold strength when hot, regardless of the storage conditions of the resin-coated sand, so the defect rate during mold creation is extremely low. Even when used in sand, it has excellent thermal decomposition properties, so there is no need for a sand burning process for sand removal. EXAMPLES Hereinafter, the present invention will be specifically explained with reference to Examples. Production of resin-coated sand: Example 1 1 kg of No. 6 silica sand preheated to 200°C was placed in a stirring mixing tank with a cooling jacket, stirred while cooling, and heated to 180°C to prepare a novolak type phenol formaldehyde resin (softening point: 85°C). ), then 8 g of triglycidyl isocyanurate was added at 140°C, and after quenching, 2 g of dicyandiamide and 2 g of hexamethylenetetramine were added at 100°C.
The mixture was dispersed and dissolved in water, added and mixed, cooled and dried, and then discharged from the mixing tank to obtain resin-coated sand (1) of the present invention. Example 2 Using the same apparatus as in Example 1, a solid resol type phenol formaldehyde resin (softening point 84°C) at 160°C was added to 1 kg of preheated No. 6 silica sand.
After cooling and stirring at 140°C, add 15g of tri(β-methylglycidyl)isocyanurate, and after rapid cooling at 90°C, prepare fine powder of adipic dihydrazide 2.
g was suspended in 5 g of methanol, added and mixed, cooled and dried, and then discharged from the mixing tank to obtain resin-coated sand (2) of the present invention. Example 3 Using the same apparatus as in Example 1, 20 g of triglycidyl isocyanurate was added at 180°C to 1 kg of preheated No. 6 silica sand, stirred and cooled, and 5 g of dicyandiamide was added to 10 c.c. of water at 100°C. The coated sand (3A) was obtained by dispersing and mixing, cooling, drying, and removing the sand. On the other hand, for 1 kg of similarly preheated No. 6 silica sand,
At 180℃, add 22g of novolac type phenol formaldehyde resin (softening point 85℃), stir and cool, and add 3g of hexamethylenetetramine at 100℃.
It was dissolved in 10 g of water, added and mixed, cooled, dried, and then drained to obtain coated sand (3B). 500g of the above coated sand (3A) and the above coated sand (3B)
500g of the resin-coated sand (3) of the present invention was obtained. Example 4 Using the same equipment as in Example 1, a resol type phenol formaldehyde resin (softening point 84°C) which is solid at 160°C was added to 1 kg of preheated No. 6 silica sand.
g was added thereto, the mixture was quickly cooled, stirred, and the sand was discharged to obtain coated sand (4B). 350 g of the coated sand (3A) obtained in Example 3 and 650 g of the coated sand (4B) described above were mixed to obtain resin-coated sand (4) of the present invention. Example 5 22 g of triglycidyl isocyanurate was added at 160°C to 1 kg of No. 6 silica sand preheated using the same equipment as in Example 1, and the mixture was cooled to 100°C and 3 g of hexamethylenetetramine was dissolved in 10 g of water. Add, mix, cool and dry then drain and coat sand (5A)
I got it. On the other hand, for 1 kg of No. 6 silica sand preheated in the same way,
22 g of novolac type phenol formaldehyde resin (softening point 96° C.) was added at 180° C., and after cooling to 110° C., 3 g of phenyl biguanide was added and mixed, and after cooling, it was discharged to obtain coated sand (5B). 600g of the above coated sand (5A) and 400g of coated sand (5B)
g was mixed to obtain resin-coated sand (5) of the present invention. Example 6 Using the same apparatus as in Example 1, a reaction adduct of 2 moles of triglycidyl isocyanurate and 1 mole of isophthalic acid was prepared at 170°C with respect to 1 kg of preheated No. 6 silica sand.
After cooling to 100℃, add 23g of hexamethylenetetramine and 1-cyanoethyl-2-ethyl-
2g of 4-methylimidazole trimellitate for 10
The coated sand (6A) was obtained by dispersing and dissolving the mixture in 100 g of water, adding and mixing, cooling and drying, and then draining the sand. On the other hand, for 1 kg of similarly preheated No. 6 silica sand,
22 g of novolac type phenol formaldehyde resin (softening point 76°C) was added and mixed at 170°C, and after cooling, the sand was removed to obtain coated sand (6B). 500g of the above coated sand (6A) and 500g of coated sand (6B)
The resin-coated sand (6) of the present invention was obtained by mixing with g. Example 7 Triglycidyl isocyanurate was added to 1 kg of No. 6 silica sand preheated using the same equipment as in Example 1.
21 g was added and mixed at 160°C, cooled, and then drained to obtain coated sand (7A). On the other hand, resol type phenol formaldehyde resin (softening point
Add and mix 25g (78℃) at 160℃, cool, and heat to 100℃.
3 g of guanidine carbonate was dispersed in 10 g of water, added and mixed, cooled, dried, and then drained to obtain coated sand (7B). 500g of the above coating (7A) and 500g of coated sand (7B)
The resin-coated sand (7) of the present invention was obtained by mixing. Example 8 22 g of novolac-type phenol formaldehyde resin (softening point 85°C) was added and mixed at 180°C to 1 kg of No. 6 silica sand preheated using the same equipment as in Example 1, and the mixture was cooled at 100°C. 4 g of dicyandiamide and 3 g of hexamethylenetetramine were dispersed and dissolved in 10 g of water and added, mixed, cooled, dried, and then drained to obtain coated sand (8B). 500 g of the coated sand (7A) produced in Example 7 and 500 g of the above-mentioned coated sand (8B) were mixed to obtain resin-coated sand (8) of the present invention. Comparative Example 1 The coated sand (3A) produced in Example 3 was used as resin-coated sand (i) for comparative testing. Comparative Example 2 The coated sand (3B) produced in Example 3 was used as resin-coated sand (ii) for comparative testing. Evaluation of resin-coated sand: The resin-coated sands (1) to (8) of the present invention described above and the resin-coated sands (i) and (ii) as comparative examples were evaluated regarding the following items. (b) Measurement of strength at temperature The above-mentioned coated sands were tested at 230°C using a high-temperature tensile tester.
It was molded for 90 seconds, and the tensile strength at a temperature of 230°C was immediately measured. (b) Measurement of hot strength of resin-coated sand after storage After each coated sand described above was left in an environmental test chamber at 40°C and 95% relative humidity for one week, the hot tensile strength was measured in the same manner as in (a) above. did. (c) Thermal disintegration test Each of the above coated sands was preheated to 250℃ and had an inner diameter of 30 mm.
Pour the sand into a cylindrical mold with a height of 30 mm, heat it for 60 seconds, remove it to create a core, and place a core of sand with a diameter of 10 mm into a cylindrical main mold with an inner diameter of 70 mm and a depth of 70 mm, which was separately prepared using a bentonite mold. After attaching the discharge port and setting the above-mentioned core, pouring the 650°C aluminum light composite melt and cooling and solidifying it, the main mold was broken and vibrated for 5 minutes using a rotor-tap tester. The weight percent of sand discharged from the core from the outlet of the alloy casting was measured. The results of the evaluation tests (a), (b), and (c) above are listed in Table 1. 【table】
Claims (1)
び/又はトリ(βメチルグリシジル)イソシア
ヌレートと、 (B) ジシアンジアミド、ジシアンジアミド誘導
体、有機酸ヒドラジド又はイミダゾール誘導体
の1種以上と、 (C) フエノールホルムアルデヒド樹脂と、を結合
剤として被覆してなる樹脂被覆砂。 2 前記(A)及び(B)を被覆してなる砂と前記(C)を被
覆してなる砂とを混合してなる特許請求の範囲第
1項記載の樹脂被覆砂。 3 前記(A)を被覆してなる砂と前記(B)及び(C)を被
覆してなる砂とを混合してなる特許請求の範囲第
1項記載の樹脂被覆砂。 4 (A) トリグリシジルイソシアヌレートおよ
び/又はトリ(βメチルグリシジル)イソシア
ヌレートと、 (B) ジシアンジアミド、ジシアンジアミド誘導
体、有機酸ヒドラジド又はイミダゾール誘導体
の1種以上と、 (C) フエノールホルムアルデヒド樹脂と、 (D) ヘキサメチレンテトラミンと、 を結合剤として被覆してなる樹脂被覆砂。 5 前記(A)及び(B)を被覆してなる砂と前記(C)及び
(D)を被覆してなる砂とを混合してなる特許請求の
範囲第4項記載の樹脂被覆砂。 6 前記(A),(B)及び(D)を被覆してなる砂と前記(C)
を被覆してなる砂とを混合してなる特許請求の範
囲第4項記載の樹脂被覆砂。 7 前記(A)を被覆してなる砂と前記(B)、(C)及び(D)
を被覆してなる砂とを混合してなる特許請求の範
囲第4項記載の樹脂被覆砂。 8 前記(A)及び(D)を被覆してなる砂と前記(B)及び
(C)を被覆してなる砂とを混合してなる特許請求の
範囲第4項記載の樹脂被覆砂。[Scope of Claims] 1 (A) triglycidyl isocyanurate and/or tri(β-methylglycidyl)isocyanurate, (B) one or more of dicyandiamide, dicyandiamide derivative, organic acid hydrazide, or imidazole derivative, and (C) Resin-coated sand made by coating phenol formaldehyde resin as a binder. 2. Resin-coated sand according to claim 1, which is obtained by mixing sand coated with (A) and (B) and sand coated with (C). 3. Resin-coated sand according to claim 1, which is obtained by mixing sand coated with (A) and sand coated with (B) and (C). 4 (A) triglycidyl isocyanurate and/or tri(β-methylglycidyl)isocyanurate; (B) one or more of dicyandiamide, dicyandiamide derivative, organic acid hydrazide, or imidazole derivative; (C) phenol formaldehyde resin; D) Resin-coated sand made by coating hexamethylenetetramine with as a binder. 5 Sand coated with the above (A) and (B) and the above (C) and
The resin-coated sand according to claim 4, which is obtained by mixing sand coated with (D). 6 Sand coated with the above (A), (B) and (D) and the above (C)
The resin-coated sand according to claim 4, which is obtained by mixing the resin-coated sand with the sand coated with the resin-coated sand. 7 Sand coated with the above (A) and the above (B), (C) and (D)
The resin-coated sand according to claim 4, which is obtained by mixing the resin-coated sand with the sand coated with the resin-coated sand. 8 Sand coated with the above (A) and (D) and the above (B) and
The resin-coated sand according to claim 4, which is obtained by mixing the sand coated with (C).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP15615481A JPS5858954A (en) | 1981-10-02 | 1981-10-02 | Resin coated sand |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP15615481A JPS5858954A (en) | 1981-10-02 | 1981-10-02 | Resin coated sand |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS5858954A JPS5858954A (en) | 1983-04-07 |
| JPS6119329B2 true JPS6119329B2 (en) | 1986-05-16 |
Family
ID=15621524
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP15615481A Granted JPS5858954A (en) | 1981-10-02 | 1981-10-02 | Resin coated sand |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS5858954A (en) |
-
1981
- 1981-10-02 JP JP15615481A patent/JPS5858954A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS5858954A (en) | 1983-04-07 |
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