JPS59127947A - Resin coated sand composition for shell mold - Google Patents
Resin coated sand composition for shell moldInfo
- Publication number
- JPS59127947A JPS59127947A JP287883A JP287883A JPS59127947A JP S59127947 A JPS59127947 A JP S59127947A JP 287883 A JP287883 A JP 287883A JP 287883 A JP287883 A JP 287883A JP S59127947 A JPS59127947 A JP S59127947A
- Authority
- JP
- Japan
- Prior art keywords
- resin
- parts
- coated sand
- sand
- shell mold
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Pending
Links
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
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)
- Compositions Of Macromolecular Compounds (AREA)
Abstract
Description
【発明の詳細な説明】
本発明は特定された)rラック型フェノール(&t 脂
ヲ含むシェルモールド用のレジンコーテツドサンド組成
物に関するものであり、特に、速硬化性で且つ駒型の曲
げ強度の良好なシェルモールド用のレジンコーテツドサ
ンドの組成物Vこ関するものである。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a resin-coated sand composition for shell molds containing a specified) r-lac type phenol (&t), and in particular, has fast curing properties and high bending strength of a piece type. The present invention relates to a resin-coated sand composition V for shell molds having good properties.
従来、シェルモールド用のレノンコーテツドサンドを製
造する鹸に1史用されるノボラックA!!フェノール樹
脂は、反応時の触媒としてず1ヒ酸、塩酸、硫酸、’J
ン酸、=5トルエンスルポン醒、ベンゼンスルホン酸、
マレイン酸、蟻酸などのば性物質を使用することにより
得られるオル) ieう比(フェノール類の一〇H基に
対するメチレン基の結合を示すオルト結合とパラ結合と
のメチレン基数の比;以下0/Pと略1己する)が0.
3〜1.2のノj?ラック型フェノール樹脂(以下、B
樹脂とする)と、反応時の触媒として酢酸亜鉛、酢酸マ
ンガン、酢nクマグネシウム、硼酸亜鉛などの2価金属
塩を使用することにより得られる0/′Pが2.0〜7
.0のノ?ラック型フェノール樹脂(以下、A樹脂とす
る)がある。Novolak A has been used for a long time in the production of Lennon coated sand for shell molds! ! Phenol resin can be used as a catalyst during reactions such as arsenic acid, hydrochloric acid, sulfuric acid, 'J
acid, = 5 toluenesulfonic acid, benzenesulfonic acid,
Ortho-bond and para-bond (ratio of the number of methylene groups, which indicates the bond of methylene group to 10H group of phenols; hereinafter 0) /P and approximately 1 self) is 0.
3-1.2 Noj? Lac-type phenolic resin (hereinafter referred to as B
0/'P is 2.0 to 7.
.. 0 no? There is a lac type phenolic resin (hereinafter referred to as A resin).
しかしながら、夫々のノがラック型フェノール1Mt
Bmに硬化剤としてヘキサメチレンテトラミンを用いて
iUられたレノンコーテツドサンド組成物はB引揃を使
用(またり易倚、硬化速度がおそく、また、A 4yi
711#を1史用した場合、(gI脂自体Vこ固結を
生じやすく、また得られた病型の曲げ強度が低いという
欠点があった。However, each of the 1 Mt lac-type phenols
Renone-coated sand compositions prepared using hexamethylenetetramine as a curing agent for Bm use B-coating (also easy to swallow, slow curing speed, and A-4yi).
When 711# was used for a period of time, it had the drawbacks that it was easy to cause caking and the bending strength of the obtained diseased type was low.
本発明者らは、これらの欠点を見服すべく、鋭5歳研究
した結果、A樹脂とB確(脂を併用することによりml
脂自体の固結がなく、得られたコーテツドサンドの硬化
速)dが早く且つ、それより造形された鋳型の曲げ強j
夏の篩いレジンコーテツドサンド組成物が得られるこ七
を見出l〜′に1゜A樹脂とB樹脂の併用割合は11(
融化で1:9〜9:lであるが、+!FVこ7:3〜3
ニアが好ましい。In order to overcome these shortcomings, the present inventors conducted extensive research for five years, and found that by using A resin and B resin together (ml
There is no caking of the fat itself, the hardening speed of the coated sand obtained is fast, and the bending strength of the mold formed is higher than that.
The combination ratio of A resin and B resin is 11 (1° to
The melting ratio is 1:9 to 9:l, but +! FVko7:3~3
Near is preferred.
A樹脂がB樹脂に対し、屯ilt比で9:1よりも多く
なると、鋳型の曲げ這呟が低下I7、また、A但1脂が
B樹脂に対し7ボ1辻比で1=9よりも下まわるとコー
テツドサンドの硬化速度の同上効果が低下する。1つま
り、いずれの場合においてもA@廟とB樹脂との併用に
よる相刺効果は4切侍できない。When the ratio of A resin to B resin exceeds 9:1, the bending of the mold decreases. If the ratio is lower than that, the effect of the above on the hardening speed of the coated sand will decrease. 1. In other words, in any case, the mutual effect of the combined use of A@myo and B resin cannot be achieved.
へ樹脂とB樹脂の各々の数平均分子性は300〜650
であることが望ましい。畝平均分子敵が300未満の場
合、得られたコーテツドサンドの硬化速度が低下し、と
ぐにA樹脂にあっては樹脂自体の固結が者るしい。また
、650をこえる場合、樹脂の流れが恐くなるので鋳型
の曲げ強度が低下する、。The number average molecular weight of each of the resin B and the resin B is 300 to 650.
It is desirable that When the ridge average molecular weight is less than 300, the curing speed of the obtained coated sand decreases, and in the case of resin A, the resin itself tends to solidify rapidly. Moreover, when it exceeds 650, resin flow becomes difficult and the bending strength of the mold decreases.
A樹脂とB樹脂をレジンコーテツドサンド製造工程中で
鋳型用耐火性粒状物に被検さぜるときは、各々の樹脂を
添加順序を問わず蘇加してよい。あるいはへ樹脂とB樹
脂をあらかじめ固形状で粉砕混合するか、またはエクス
トルーダーなどの混稗機により溶融混合した後、粉砕し
、レノンコーテツドサンドの製造工程中にて添加しても
よい。When Resin A and Resin B are added to the refractory granules for molds during the resin-coated sand manufacturing process, each resin may be added in any order. Alternatively, the He resin and the B resin may be pulverized and mixed in solid form in advance, or melt-mixed using a mixer such as an extruder, and then pulverized and added during the manufacturing process of Lennon coated sand.
本発明で使用するフェノール胡としては、フェノール、
クレゾール、キシレノールなどがあるが、レゾルシン、
カテコール、ハイドロキノン、アニリン、尿素、メラミ
ン、カシューナツトシェルオイルなどを存在せしめたも
のも1史用できる。アルデヒド類としては、ホルマリン
、パラホルムアルデヒド、トリオキサン、アセトアルデ
ヒドなどから選ばれたアルデヒド1勿質を1史用する。The phenol salts used in the present invention include phenol,
There are cresol, xylenol, etc., but resorcinol,
Products containing catechol, hydroquinone, aniline, urea, melamine, cashew nut shell oil, etc. can also be used. As the aldehyde, an aldehyde selected from formalin, paraformaldehyde, trioxane, acetaldehyde, etc. is used.
A樹脂の固結を防止して本発明を好まし〈実施するため
A樹脂に内含させる滑剤ば、通常の滑剤が使用できるが
、エチレンビスステアリン酸アマイド、メチレンビスス
テアリン酸アマイド、ステアリン醒アマイド、メチロー
ルステアリン酸アマイドが好ましい。なおり樹脂にこれ
ら滑剤が内含さね、ていても差支えない。また、この滑
剤は、フェノール樹脂の製造時、反応開始前、反応中、
および反応終了後のいずれのときに添加しても滑剤を内
含したフェノール位(脂ができる。滑剤の配合IはA樹
脂100瑣縫部に対1−.5重計φ以下の必要がある。The present invention is preferred by preventing the caking of resin A.For the lubricant to be included in resin A for implementation, ordinary lubricants can be used, but ethylene bisstearamide, methylene bisstearamide, stearinated amide, etc. , methylolstearamide is preferred. There is no problem even if the guide resin contains these lubricants. In addition, this lubricant is used during the production of phenolic resin, before the start of the reaction, during the reaction,
Even if it is added at any time after the completion of the reaction, a phenol (fat) containing a lubricant will be formed.The lubricant formulation I must be 1-.5 weight φ or less per 100 sq. seams of A resin.
5I((量係をこえる場合得られたコーテツドサンド°
による鋳型の強度が低下する。5I ((If the amount exceeds the coated sand obtained
This reduces the strength of the mold.
本発明が採用するコーテツドサンドの製造方法としては
、ドライホットコート法、セミホットコート法、コール
ドコート法、粉末靜削法のいずれの方法であってもよい
が、本発明をさらに好まし〈実施するにはドライホット
コート法が推奨される。The coated sand manufacturing method employed in the present invention may be any of the dry hot coating method, semi-hot coating method, cold coating method, and powder polishing method, but the present invention is more preferred. A dry hot coat method is recommended for this purpose.
以下、本発明を実施例により説明する。しかし、本発明
はこれら実施例によって限雉されるものではない。The present invention will be explained below using examples. However, the present invention is not limited to these Examples.
また、各実施例、比較例に6己賊されている「部」およ
び「係」は、すべてhi部」および「屯−址褒」を示す
。In addition, the "part" and "section" that are used in each of the Examples and Comparative Examples all refer to "hi-bu" and "hi-bu".
製造例1
冷却器と攪拌器付き反応釜を準備し、これにフェノール
1000 it(、37%ホルマリン604都、次いで
、#′酸捕鉛10部を仕込んだ1、徐々に昇温し、温度
が96°Cに達してから300分間還流反応後エチレン
ビスステアリン酸アマイド10部を添加した。混合物を
均一に分散させた。その後真空下で脱水反応を行ない、
釡出し、急冷[7て常温で固形の滑剤内含A樹脂960
部を得た6、
製造例2
冷却器と攪拌器付き反応釜を準備[7、これにフェノー
ル1000部、37チホルマリン650部、次いで修t
’[10部を仕込んだ6つ徐々に昇温し、温度が96℃
に達してから120分間還流反応した1、その後真空ド
で脱水反応を行ない、4出し、急冷して常温で固形のB
樹脂985部を得た。Production Example 1 A reaction vessel equipped with a cooler and a stirrer was prepared, and 1000 parts of phenol (604 parts of 37% formalin) was added to it, followed by 10 parts of lead capture with #' acid.The temperature was gradually raised until the temperature reached 1. After reaching 96°C, 10 parts of ethylene bisstearamide was added after refluxing for 300 minutes.The mixture was uniformly dispersed.Then, a dehydration reaction was carried out under vacuum.
Unloading and quenching [7] Resin A 960 containing lubricant is solid at room temperature.
6. Production Example 2 Prepare a reaction vessel with a cooler and a stirrer [7. To this, add 1000 parts of phenol, 650 parts of 37-thiformin, and then add
'[10 parts were charged into 6 batches, and the temperature was gradually raised to 96℃.
After reaching 120 minutes, the reflux reaction was carried out for 120 minutes. After that, dehydration reaction was carried out in a vacuum chamber.
985 parts of resin were obtained.
製造例3
冷却器と攪拌器付き反応釜を準備し、これにフェノール
1000部1,37%ホルマリン604部、次いで酢酸
亜鉛10部を仕込んだ。保々に昇温し、温度が:J6℃
((達してから120分間還流反応後エチレンビスステ
アリンばアマイド10部を添加した。混合物を均一に分
散させた。その後真空下で脱水反応を行ない、盃出し、
急冷して、常温で固形の滑剤内含A面脂850都を傅だ
。Production Example 3 A reaction vessel equipped with a cooler and a stirrer was prepared, and 1,000 parts of phenol, 604 parts of 1,37% formalin, and then 10 parts of zinc acetate were charged therein. The temperature rises steadily and the temperature is J6℃
After refluxing for 120 minutes, 10 parts of ethylene bisstearamide was added. The mixture was uniformly dispersed. After that, a dehydration reaction was carried out under vacuum, and the
After cooling rapidly, the lubricant contains 850 ml of A-side fat, which is solid at room temperature.
製造1列 4
冷却器と攪拌器付き反応釜を準備し、これにフェノール
1000部、#37多ホルマリン647部、次いで酢酸
亜鉛10部を仕込んだ。徐々に昇温し、温度が96℃に
達してから500分間還流反応後エチレンビスステアリ
ン酸アマイド10部を添加した。混合物を均一に分散さ
せた。その後真空下で脱水反応を行ない、釜出I〜、執
冷して常温で固形の滑剤内含A樹脂1020部を得た。Production 1 line 4 A reaction vessel equipped with a cooler and a stirrer was prepared, and 1000 parts of phenol, 647 parts of #37 polyformalin, and then 10 parts of zinc acetate were charged therein. The temperature was gradually raised, and after the temperature reached 96°C, reflux reaction was carried out for 500 minutes, and then 10 parts of ethylene bisstearamide was added. The mixture was evenly dispersed. Thereafter, a dehydration reaction was carried out under vacuum, and the mixture was cooled down to obtain 1020 parts of lubricant-containing resin A which was solid at room temperature.
製造例5
冷却器と攪拌器付き反応釜を準+l1flし、これにフ
ェノール1000部、37%ホルマリン604部、次い
で(Iff: l設置0部を仕込んだ1.倣々に昇r晶
し、輻)Wが96℃に達してから60分間還流反応した
。エチレンビスステアリン酸アマイド10部を添加した
。混合物を均一に分散させた。その後真空下で脱水反応
を行ない、4出(7、油、冷して、常taで固形の滑剤
内含B樹脂920部を得た。Production Example 5 A reaction vessel equipped with a condenser and a stirrer was charged with 1000 parts of phenol, 604 parts of 37% formalin, and then (Iff: 0 parts). ) After W reached 96°C, reflux reaction was carried out for 60 minutes. 10 parts of ethylene bisstearamide was added. The mixture was evenly dispersed. Thereafter, a dehydration reaction was carried out under vacuum to obtain 920 parts of lubricant-containing Resin B which was solid at normal ta and was cooled.
製造例6
冷ム1]器と攪拌器付き反応釜を準11m1〜、これに
フェノール1000部、:37%ホルマリン690部、
次いで蓚酸10部を仕込んだ。徐々に昇温し、温度が9
6℃に達してから240分間還流反応後、エチレンビス
ステアリン酸アマイド10都を添加した。711.合物
を分散させた後、真空下で脱水反応を行なった後、4出
(〜、局、冷して、常温で固形の滑剤内宮B樹脂108
5部を得た。Production Example 6 A reaction pot with a cold 1] container and a stirrer was prepared in a quasi-11 m1 volume, and 1000 parts of phenol, 690 parts of 37% formalin,
Next, 10 parts of oxalic acid was charged. The temperature gradually increases until the temperature reaches 9
After reaching 6°C, reflux reaction was carried out for 240 minutes, and then 10 portions of ethylene bisstearamide were added. 711. After dispersing the compound and performing a dehydration reaction under vacuum, it is cooled and mixed with lubricant Naiku B Resin 108, which is solid at room temperature.
Got 5 copies.
製造例7
製造例1にて得られた滑剤内含A樹脂700Kyと製造
例2にて得られたB樹脂300縁を夫々粗砕してマ型ミ
ギサーで1時間均一に混合した。この混合物をL/D
: 8のスクリューを持つ押出機のホラ・や−に仕込み
、内温150℃、吐出耽40 Kg 7時で押出しし7
た1、その後急冷して破砕し、875 K9の樹脂を得
た。Production Example 7 The 700Ky of lubricant-containing resin A obtained in Production Example 1 and the 300Ky edge of B resin obtained in Production Example 2 were each crushed and uniformly mixed in a machine mixer for 1 hour. This mixture is L/D
: Pour into the conch of an extruder with a No. 8 screw, and extrude at 7 o'clock with an internal temperature of 150°C and a discharge weight of 40 kg.
After that, it was rapidly cooled and crushed to obtain a resin of 875K9.
実施例
温度130〜140℃に加熱した三木6号珪砂7000
部をワールミキサーに仕込み、製造例1にて傅られた滑
剤内含A樹脂ユJ8部、および製造例2にて得られたB
樹脂42部を請願した後、40秒間混練した。Example: Miki No. 6 silica sand 7000 heated to a temperature of 130 to 140°C
8 parts of A resin containing lubricant obtained in Production Example 1 and B obtained in Production Example 2.
After applying 42 parts of resin, it was kneaded for 40 seconds.
ついでヘキサメチレンテトラミン21部を水105部に
溶解して添加し、コーテツドサンドが崩壊するまで混練
した。さらにステアリング1タカルシウムフ部を添加し
、30秒間混合して、排砂してエヤレーションを行ない
レジンコーテツドサンド組成物を得た。Next, 21 parts of hexamethylenetetramine dissolved in 105 parts of water was added and kneaded until the coated sand disintegrated. Further, Steering 1 Calcium Ff was added, mixed for 30 seconds, and the sand was removed and aerated to obtain a resin coated sand composition.
実施例2
温度130〜140℃に加熱した三木6号珪砂7000
部をワールミキサーに仕込み、製造例1にて得られた滑
剤内宮A樹脂42部、および製造例2にて得られたB樹
脂・+8部を6加(〜だ後、40秒間混線した。Example 2 Miki No. 6 silica sand 7000 heated to a temperature of 130 to 140°C
42 parts of the lubricant Naiku A resin obtained in Production Example 1 and +8 parts of the B resin obtained in Production Example 2 were added to the mixer for 40 seconds.
ついで、ヘキサメチレンテトラミン21部を水105部
に溶解してlf”fi )In L、、コーテツドサン
ドが朋滅するまで混fJ 1.、た。さらにステアリン
鍍カルシウム7!1≦を添加し、;30秒間混合して、
排砂してエヤレ(−ションヲ行ない、レノンコーテツド
サンド組成申グをイ拝た。Next, 21 parts of hexamethylenetetramine was dissolved in 105 parts of water and mixed until the coated sand was completely destroyed.Additionally, 71 parts of calcium stearin was added; Mix for 30 seconds and
After removing the sand and carrying out the process, I found that the composition of the Lennon coated sand was tested.
実施例3
温度130〜140℃に加熱した三木6号珪砂7000
部をワールミキサーに仕込み、映Jaし117にて得ら
れた混合樹脂140部を添加した後、710秒間混練し
た。ついでヘキサメチレンテトラミン21部を水105
部に溶解して励加L7、コーテツドサンドが崩壊するま
で混練した。さらにステアリン酸カルシウム7部を添加
し1,30秒間混合して排砂してエヤレーションヲ行な
いレノンコーテツドサンド組成物を得た。Example 3 Miki No. 6 silica sand 7000 heated to a temperature of 130 to 140°C
After adding 140 parts of the mixed resin obtained in Eija 117, the mixture was kneaded for 710 seconds. Then, 21 parts of hexamethylenetetramine was added to 105 parts of water.
The coated sand was dissolved in a portion and kneaded under excitation L7 until the coated sand disintegrated. Further, 7 parts of calcium stearate was added, mixed for 1.30 seconds, and aeration was performed by removing the sand to obtain a Lennon coated sand composition.
比較例1
温+1i3o〜140℃に加熱した三乗6号珪砂700
0部をワールミキサーに仕込み、製造例3にて得られた
滑剤内含A樹脂さ」8部、および製造例5にて得られた
隋剤内含B樹脂42部を添加した後、40秒間混練した
。ついでヘキサメチレンテトラミン21部を水105部
に溶解して’f6’fi刀1し、コーテツドサンドがF
D4麿するまで混練した。さらにステアリン酸カルシウ
ム7部を冷加し1,30秒間混合して、排砂してエヤレ
ーションを行ないレジンコーテツドサンド組成物を得た
。Comparative Example 1 Cubic No. 6 silica sand 700 heated to +1i3o to 140°C
After adding 8 parts of lubricant-containing resin A obtained in Production Example 3 and 42 parts of lubricant-containing resin B obtained in Production Example 5, the mixture was heated for 40 seconds. Kneaded. Next, 21 parts of hexamethylenetetramine was dissolved in 105 parts of water, and the coated sand was prepared by dissolving it in 105 parts of water.
The mixture was kneaded until D4. Furthermore, 7 parts of calcium stearate was cooled and mixed for 1.30 seconds, and the sand was removed and aerated to obtain a resin coated sand composition.
比較例2
温度130〜140℃にDO熱した三乗6号珪砂700
0部にワールミキサーに仕込み、製造例4にて得られた
滑剤内含A1グI脂1す8部、および製造例6にて得ら
れた滑剤内より樹脂42部を冷加した後、40秒間混練
した。ついで、ヘキサメチレンテトラミン21部を水1
05部に溶解して添加し、コーテツドサンドが崩壊する
まで混線した。さらにステアリン酸カルシウム7部を添
加し、30秒間混合して、排砂シテエヤレーションを行
ない、レジンコーテツドサンド組成物を得た1、
比較例3
温度130〜140℃に加熱した三栄6号珪砂70(1
0部をワールミキサーに仕込み、製1宥例3 V(て得
られた滑剤内含A4匍脂98部、および製造例2にて得
られたB樹脂42部を除却した後、40秒間混練した。Comparative Example 2 Cubic No. 6 silica sand 700 DO heated to a temperature of 130 to 140°C
0 part was charged in a whirl mixer, 8 parts of lubricant-containing A1 g I fat obtained in Production Example 4, and 42 parts of resin from the lubricant obtained in Production Example 6 were cooled, and 40 Kneaded for seconds. Next, 21 parts of hexamethylenetetramine was added to 1 part of water.
The mixture was dissolved in 0.05 parts and added, and mixed until the coated sand collapsed. Furthermore, 7 parts of calcium stearate was added, mixed for 30 seconds, and sand aeration was performed to obtain a resin coated sand composition 1. Comparative Example 3 Sanei No. 6 silica sand 70 heated to a temperature of 130 to 140°C (1
0 part was placed in a Whirl mixer, and after removing 98 parts of the A4 fat in the lubricant obtained in Production Example 3 V and 42 parts of B resin obtained in Production Example 2, the mixture was kneaded for 40 seconds. .
ついでヘキサメチレンテトラミン21部を水105部に
溶解して除加し、コーテツドサンドが崩腿するまで混練
した。さらにステアリン酸カルシウム7部を添加j〜、
30秒間混合して、排砂してエヤレーションを行ない、
レジンコーテツドサンド組成物を得た。Next, 21 parts of hexamethylenetetramine was dissolved in 105 parts of water and added, and the mixture was kneaded until the coated sand crumbled. Additionally, 7 parts of calcium stearate are added.
Mix for 30 seconds, remove sand and aerate,
A resin coated sand composition was obtained.
比較例4
温度130〜140℃に加熱した三乗6号珪砂7000
都をワールミキサーに仕込み、製造例1にて得られた滑
剤内含A樹脂7部、および製造例2にて得られたB樹脂
133部を添加した後、40秒間/l!、練した。つい
で、ヘキサメチレンテトラミン21部を水冷却1−2、
:30秒間混合して、排砂して、エヤレーションを行な
い、レノンコーテツドサンド組成物を得た。Comparative Example 4 Cubic No. 6 silica sand 7000 heated to a temperature of 130 to 140°C
After adding 7 parts of lubricant-containing resin A obtained in Production Example 1 and 133 parts of B resin obtained in Production Example 2, the mixture was heated for 40 seconds/l! , practiced. Next, 21 parts of hexamethylenetetramine was cooled with water 1-2,
: The mixture was mixed for 30 seconds, the sand was removed, and aeration was performed to obtain a Lennon coated sand composition.
比較例5
温度130〜140℃に加熱した三乗6号珪砂7000
部をワールミキサーに仕込み、d fix 例] V(
てイ4られた滑剤内含A樹脂133部、および製造例2
にて得られたB樹脂7部を水105部に溶解して添加し
7、コーテツドサンドが崩壊するまで混線した。さらに
ステアリン酸カルシウム7部を冷加し、刃秒間混合して
、排砂して、エヤレーションを行ない、レノンコー・デ
ッドサンド面I成4勿をイ拝た。Comparative Example 5 Cubic No. 6 silica sand 7000 heated to a temperature of 130 to 140°C
Example] V (
133 parts of lubricant-containing resin A, and Production Example 2
7 parts of B resin obtained in step 7 was dissolved in 105 parts of water and added thereto, followed by mixing until the coated sand collapsed. Furthermore, 7 parts of calcium stearate was cooled, mixed for a few seconds, the sand was removed, and aeration was performed, and the Lenonko dead sand surface I was completely coated.
製造例1.2.3.4.5.6にて得られた各々のレジ
ンの特性値を第1−!5eに、実施例1.2.3および
比較例1.2.3.4.5にて得られた否々のレジンコ
ーテツドサンドの特性11Mを第2表に示す。The characteristic values of each resin obtained in Production Example 1.2.3.4.5.6 are shown in the first-! Table 2 shows the properties 11M of the resin coated sand obtained in Example 1.2.3 and Comparative Example 1.2.3.4.5.
なお、試鹸方法は次の辿りである。The method for testing the soap is as follows.
IA虫 点:J工E’ −K −(1064によ
る0 7 P :核磁気共鳴スペクトルにより
、2.2′メチレン、2,4′メチレン、4.4′メチ
レンのプロトン数の定
線による。IA insect point: J Engineering E' -K - (07P according to 1064): Based on the constant line of proton number of 2.2' methylene, 2,4' methylene, 4.4' methylene by nuclear magnetic resonance spectrum.
数平均分子ht :蒸気圧平衡法による。Number average molecule ht: Based on vapor pressure equilibrium method.
粘 、a 点: JAOT試験法c−1による。Viscosity, point a: According to JAOT test method c-1.
曲げ強さ: JAOT試験法5M−1による3、熱間引
張り強さ: JAOT試験法sM −10による。Bending strength: 3 according to JAOT test method 5M-1, hot tensile strength: according to JAOT test method sM-10.
Claims (3)
の結合位置を示すオルト結合(0)とパラ結合(P)と
のメチレン基数の比(0/P )が2.0〜7.0のノ
ボラック型フェノール樹脂(A) トO/Pが0.3〜
1.20ノ?ラツク型フエノール樹脂(B)を存在させ
たシェルモールド用のレジンコーテツドサンド組成物3
゜(1) Novolak with a methylene group ratio (0/P) of 2.0 to 7.0 between the ortho bond (0) and the para bond (P), which indicates the bonding position of the methylene group to the 10H group of the phenol. Type phenolic resin (A) O/P is 0.3~
1.20 no? Resin-coated sand composition 3 for shell molds containing easy-type phenolic resin (B)
゜
ボラック型フェノール樹脂(B)の屯せ比が1=9〜9
:1である特許請求のψ百聞第1項記載のシェルモール
ド用のレノンコーテツドサンド組成物。(2) Novolac! The ratio of the phenolic resin (A) to the novolac type phenolic resin (B) is 1 = 9 to 9
: 1. The Lennon coated sand composition for shell molds according to item 1 of the patent claim.
よびノがラック型フェノール樹脂(B)の各々の数平均
分子東が300〜650である特許請求の範囲第1項寸
たは第2項記載のシェルモールド用のレジンコーテツド
サンド組11父書勿1、(4) ノがラック型フェノ
ール1會()(旨(A)が5丁(j ’i@:%以下の
滑剤を内含する特、ffτ1〆I求の中巳1411 嘱
1項、第2項、または第3項記載のシェルモールド用の
レジンコーテツドサンド組成物。(3) Nogalac-type phenolic tree DW (A) B
Resin coated sand set 11 for shell mold according to claim 1 or claim 2, wherein each of the lac type phenolic resin (B) has a number average molecular weight of 300 to 650. 1, (4) Lac-type phenol 1 () (effect (A) is 5 (J'i@:%) or less of lubricant, ff , the resin-coated sand composition for shell molds according to item 2 or 3.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP287883A JPS59127947A (en) | 1983-01-13 | 1983-01-13 | Resin coated sand composition for shell mold |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP287883A JPS59127947A (en) | 1983-01-13 | 1983-01-13 | Resin coated sand composition for shell mold |
Publications (1)
Publication Number | Publication Date |
---|---|
JPS59127947A true JPS59127947A (en) | 1984-07-23 |
Family
ID=11541607
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP287883A Pending JPS59127947A (en) | 1983-01-13 | 1983-01-13 | Resin coated sand composition for shell mold |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS59127947A (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS61246237A (en) * | 1985-04-25 | 1986-11-01 | Sumitomo Deyurezu Kk | Production of phenolic resin composite foam |
WO2007049645A1 (en) * | 2005-10-27 | 2007-05-03 | Asahi Organic Chemicals Industry Co., Ltd. | Novolak type phenol resin for shell molding, method of producing the same and resin-coated sand |
-
1983
- 1983-01-13 JP JP287883A patent/JPS59127947A/en active Pending
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS61246237A (en) * | 1985-04-25 | 1986-11-01 | Sumitomo Deyurezu Kk | Production of phenolic resin composite foam |
JPH0365826B2 (en) * | 1985-04-25 | 1991-10-15 | ||
WO2007049645A1 (en) * | 2005-10-27 | 2007-05-03 | Asahi Organic Chemicals Industry Co., Ltd. | Novolak type phenol resin for shell molding, method of producing the same and resin-coated sand |
US7579075B2 (en) | 2005-10-27 | 2009-08-25 | Asahi Organic Chemicals Industry Co., Ltd. | Phenolic novolak resin for shell mold, process for producing the same, and resin coated sand |
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