JP3249010B2 - Manufacturing method of casting mold - Google Patents
Manufacturing method of casting moldInfo
- Publication number
- JP3249010B2 JP3249010B2 JP12471094A JP12471094A JP3249010B2 JP 3249010 B2 JP3249010 B2 JP 3249010B2 JP 12471094 A JP12471094 A JP 12471094A JP 12471094 A JP12471094 A JP 12471094A JP 3249010 B2 JP3249010 B2 JP 3249010B2
- Authority
- JP
- Japan
- Prior art keywords
- reaction
- parts
- solution
- mold
- phenol
- 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
Links
Landscapes
- Phenolic Resins Or Amino Resins (AREA)
- Mold Materials And Core Materials (AREA)
- Compositions Of Macromolecular Compounds (AREA)
Description
【0001】[0001]
【産業上の利用分野】本発明は、殊に圧縮強度に優れた
鋳造用の鋳型及び中子(本明細書の全てにわたって鋳型
と略称する。)の製造方法に関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a casting mold and a method for producing a core (hereinafter, abbreviated as a mold throughout the present specification) which are particularly excellent in compressive strength.
【0002】[0002]
【従来の技術】従来、鋳込みの際に刺激性の酸ガスを発
生しない鋳造用鋳型を迅速かつ能率よく製造するための
粘結剤としては例えば、気体状あるいは液体状エステル
系硬化剤で硬化可能な、カリウムアルカリ性フェノール
・ホルムアルデヒド樹脂を必須成分として含有する樹脂
組成物が知られている(特開昭58−154434号公
報、特開平1−40136号公報参照)。2. Description of the Related Art Conventionally, as a binder for quickly and efficiently producing a casting mold that does not generate irritating acid gas during casting, it can be cured with, for example, a gaseous or liquid ester-based curing agent. A resin composition containing a potassium alkaline phenol / formaldehyde resin as an essential component is known (see JP-A-58-154434 and JP-A-1-40136).
【0003】[0003]
【発明が解決しようとする課題】しかしながら、このよ
うな粘結剤を使用して製造した鋳型は圧縮強度などの性
能が低いため、鋳物の品質低下の原因となっている。ま
た、このような粘結剤を粒状耐火性骨材(鋳物砂)と混
合して長時間待機させた後に鋳型を製造すると、製造し
た鋳型の圧縮強度などが顕著に低下し、粘結剤の可使時
間が短く、鋳造用鋳型を工業的に製造するうえで不都合
である。However, a mold manufactured using such a binder has low performance such as compressive strength, which causes deterioration of casting quality. In addition, when such a binder is mixed with granular refractory aggregate (casting sand) and allowed to stand by for a long period of time, when a mold is manufactured, the compressive strength of the manufactured mold is remarkably reduced, and the binder of the binder is reduced. The pot life is short, which is inconvenient for industrially producing a casting mold.
【0004】[0004]
【課題を解決するための手段】本発明者は、従来公知の
粘結剤を使用して製造した鋳造用鋳型の問題点を解決す
るため、水溶性フェノール樹脂の合成反応に着目して、
フェノール類とアルデヒド類との特定の反応比において
フェノール類の2核体化合物の生成量を最大としかつ水
溶性化することにより、粒状耐火性骨材と混合した際の
可使時間が長い粘結剤が得られ、それを使用して製造さ
れる鋳造用鋳型は圧縮強度などが高いことを見い出し、
本発明を完成するに至った。Means for Solving the Problems In order to solve the problems of a casting mold manufactured using a conventionally known binder, the present inventor focused on a synthesis reaction of a water-soluble phenol resin,
Maximizes the production of binuclear compounds of phenols at a specific reaction ratio between phenols and aldehydes and renders them water-soluble, resulting in long pot life when mixed with granular refractory aggregate. Agent is obtained and found that the casting mold manufactured using it has high compressive strength,
The present invention has been completed.
【0005】すなわち、本発明の鋳造用鋳型の製造方法
は、フェノール類1モルに対しアルデヒド類を1.6〜
2.5モルの比率でpKa2.0以下の酸性物質に基づ
く酸性状態下でノボラック化反応を行わせ、フェノール
類の2核体化合物の生成量が最大となった時点で反応液
をアルカリ性にし、更にアルカリ性状態下でレゾール化
反応を行わせて得られる水溶性フェノール樹脂を必須成
分とする粘結剤と、粒状耐火性骨材とを混合し、この混
合物を鋳型枠内に収納して成形し、次いでこの成形物に
気体状の有機酸エステル系硬化剤を通過させて硬化させ
ることを特徴とする。That is, in the method for producing a casting mold of the present invention, an aldehyde is used in an amount of 1.6 to 1 mol per phenol.
The novolak reaction is performed under an acidic condition based on an acidic substance having a pKa of 2.0 or less at a ratio of 2.5 mol, and when the amount of the binuclear compound of phenols becomes maximum, the reaction solution is made alkaline, Further, a binder containing a water-soluble phenol resin obtained by performing a resolving reaction under an alkaline condition as an essential component, and a granular refractory aggregate are mixed, and the mixture is housed in a mold frame and molded. Then, the molded product is cured by passing a gaseous organic acid ester-based curing agent.
【0006】さらに、本発明の鋳造用鋳型の製造方法
は、フェノール類1モルに対しアルデヒド類を1.6〜
2.5モルの比率でpKa2.0以下の酸性物質に基づ
く酸性状態下でノボラック化反応を行わせ、フェノール
類の2核体化合物の生成量が最大となった時点で反応液
をアルカリ性にし、更にアルカリ性状態下でレゾール化
反応を行わせて得られる水溶性フェノール樹脂を必須成
分とする粘結剤と、液体状有機酸エステル系硬化剤と、
粒状耐火性骨材とを混合し、この混合物を鋳型枠内に収
納して成形し硬化させることを特徴とする。Further, in the method for producing a casting mold of the present invention, an aldehyde is added in an amount of 1.6 to 1 mol per phenol.
The novolak reaction is performed under an acidic condition based on an acidic substance having a pKa of 2.0 or less at a ratio of 2.5 mol, and when the amount of the binuclear compound of phenols becomes maximum, the reaction solution is made alkaline, Further, a binder containing a water-soluble phenol resin obtained by performing a resolving reaction under an alkaline state as an essential component, and a liquid organic acid ester-based curing agent,
It is characterized in that it is mixed with a granular refractory aggregate, this mixture is housed in a mold frame, molded and cured.
【0007】本発明における粘結剤は、気体状又は液体
状有機酸エステル系硬化剤で硬化して鋳造用鋳型を製造
することができる水溶性フェノール樹脂を必須成分とし
て含有する。このような水溶性フェノール樹脂は、例え
ば、フェノール、クレゾール、レゾルシノール、キシレ
ノール、ビスフェノールA、クミルフェノール、ノニル
フェノール、ブチルフェノール、フェニルフェノール、
エチルフェノール、オクチルフェノール、アミルフェノ
ール、ナフトール、ビスフェノールF、ビスフェノール
C、カテコール、ハイドロキノン、ピロガロール、フロ
ログルシン、リグニン、ビスフェノールA残渣、クレゾ
ール残渣、クロロフェノール、ジクロロフェノール、そ
の他の置換フェノールを含めたフェノール類と、ホルム
アルデヒド、アセトアルデヒド、フルフラール等のアル
デヒド類とのノボラック化反応、及びそれに続くレゾー
ル化反応によって得られるレゾール・ノボラック型の水
溶性フェノール樹脂である。製造される鋳型の圧縮強度
などを高くするためには、フェノール類1モルに対し
て、アルデヒド類は1.6〜2.5モルの比率で使用す
ることが必要である。ノボラック化反応はフェノール類
がアルデヒド類により連結されたノボラック樹脂を生成
する公知の反応であり、ノボラック化反応をガスクロマ
トグラフィーなどにより追跡してフェノール類の2核体
化合物の生成量が最大となった時点で引き続き行なうレ
ゾール化反応は、ノボラック化反応の生成物をヒドロキ
シアルキル化してレゾール樹脂を生成する公知の反応で
ある。この生成される水溶性フェノール樹脂の重量平均
分子量は、2000を越えて3000以下である範囲が
好ましい。通常、水溶性フェノール樹脂は固形分50〜
75重量%の溶液、特に水溶液として使用される。ノボ
ラック化反応に用いられる適当な酸性物質は、pKa
2.0以下の化合物であり、具体的には例えば、p−ト
ルエンスルホン酸(pKa1.7)、蓚酸(pKa1.
3)、塩酸(pKa−8)を挙げることができ、pKa
1.3〜1.7のp−トルエンスルホン酸、蓚酸などが
好ましい。酸性物質のpKaが2.0を越えると得られ
る水溶性フェノール樹脂を使用して製造される鋳型の圧
縮強度などの性能が不十分となり、pKaが小さ過ぎる
と反応装置が制限されるので、好ましくない。この酸性
物質は、フェノール類に対し0.001〜0.1の範囲
のモル比でノボラック化反応に使用するのが好ましい。
レゾール化反応に用いられる適当なアルカリ性物質は水
酸化ナトリウム、水酸化カリウム、水酸化リチウム又は
これらの混合物であるが、水酸化カリウムが最も好まし
い。The binder in the present invention contains, as an essential component, a water-soluble phenol resin which can be cured with a gaseous or liquid organic acid ester-based curing agent to produce a casting mold. Such water-soluble phenol resins include, for example, phenol, cresol, resorcinol, xylenol, bisphenol A, cumylphenol, nonylphenol, butylphenol, phenylphenol,
Phenols including ethylphenol, octylphenol, amylphenol, naphthol, bisphenol F, bisphenol C, catechol, hydroquinone, pyrogallol, phloroglucin, lignin, bisphenol A residue, cresol residue, chlorophenol, dichlorophenol, and other substituted phenols, It is a resol-novolak type water-soluble phenol resin obtained by a novolak reaction with aldehydes such as formaldehyde, acetaldehyde, and furfural, and a subsequent resolation reaction. In order to increase the compressive strength and the like of the mold to be produced, it is necessary to use aldehydes in a ratio of 1.6 to 2.5 mol per 1 mol of phenols. The novolak reaction is a known reaction in which phenols form a novolak resin in which phenols are linked by aldehydes. The novolak reaction is traced by gas chromatography or the like, and the amount of a binuclear compound of phenols is maximized. The resolelation reaction that is subsequently carried out at this point is a known reaction for producing a resole resin by hydroxyalkylating the product of the novolak reaction. The weight-average molecular weight of the resulting water-soluble phenolic resin is preferably in the range of more than 2,000 to 3,000 or less. Usually, the water-soluble phenol resin has a solid content of 50 to
It is used as a 75% by weight solution, especially as an aqueous solution. Suitable acidic substances used in the novolak reaction are pKa
2.0 or less, specifically, for example, p-toluenesulfonic acid (pKa1.7), oxalic acid (pKa1.
3) and hydrochloric acid (pKa-8).
1.3 to 1.7 p-toluenesulfonic acid, oxalic acid and the like are preferred. When the pKa of the acidic substance exceeds 2.0, the performance such as the compressive strength of a mold produced using a water-soluble phenol resin obtained becomes insufficient, and when the pKa is too small, the reaction apparatus is limited, and thus it is preferable. Absent. This acidic substance is preferably used in the novolak reaction at a molar ratio of 0.001 to 0.1 with respect to phenols.
Suitable alkaline substances used in the resolelation reaction are sodium hydroxide, potassium hydroxide, lithium hydroxide or mixtures thereof, with potassium hydroxide being most preferred.
【0008】本発明において配合され得るシラン化合物
は、鋳型の粘結性を改善するために、通常、樹脂溶液に
対して0.05〜3重量%の範囲であることが好まし
く、その例としては、γ−グリシドキシプロピルトリメ
トキシシラン、γ−アミノプロピルトリエトキシシラン
等を挙げることができる。In order to improve the cohesiveness of the mold, the silane compound which can be blended in the present invention is usually preferably in the range of 0.05 to 3% by weight with respect to the resin solution. , Γ-glycidoxypropyltrimethoxysilane, γ-aminopropyltriethoxysilane and the like.
【0009】本発明における鋳造用鋳型の製造に使用さ
れる粒状耐火性骨材としては、珪砂、クロム鉄鉱砂、ジ
ルコン砂、かんらん石砂等の従来鋳型製造用に使用され
る耐火性の粒状砂のほか、粘土質の砂、再生砂を挙げる
ことができる。The granular refractory aggregate used in the production of the casting mold according to the present invention includes, for example, refractory granules used for the production of conventional molds such as silica sand, chromite sand, zircon sand and olivine sand. In addition to sand, clay sand and recycled sand can be mentioned.
【0010】本発明における鋳造用鋳型の製造に使用さ
れる硬化剤である有機酸エステルは、気体状又は液体状
の有機酸エステル系化合物である。気体状の有機酸エス
テル系硬化剤は、蟻酸メチル、蟻酸エチル、蟻酸プロピ
ル等の蒸気又はエアロゾルである。液体状の有機酸エス
テルはその沸点が常温で100℃以上のものであり、具
体的には、一価又は多価アルコールとカルボン酸とのエ
ステル化合物、特に炭素数1〜10の一価又は多価アル
コールと炭素数2〜10のカルボン酸とのエステル化合
物、あるいはラクトン化合物、カーボネート化合物を挙
げることができる。さらに具体的には例えば、酢酸エチ
ル、アジピン酸ジメチル、コハク酸ジメチル、エチレン
グリコールジアセテート、モノアセチン、ダイアセチ
ン、トリアセチン、エチレンカーボネート、γ−ブチロ
ラクトン、プロピオラクトン、ε−カプロラクトン、あ
るいはこれらの混合物である。使用される気体状又は液
体状有機酸エステル系硬化剤の量は、粘結剤の溶液に対
して5〜110重量%、特に20〜60重量%の範囲が
好ましい。The organic acid ester as a curing agent used in the production of a casting mold in the present invention is a gaseous or liquid organic acid ester compound. The gaseous organic acid ester-based curing agent is a vapor or aerosol such as methyl formate, ethyl formate, and propyl formate. The liquid organic acid ester has a boiling point of 100 ° C. or higher at room temperature, and specifically, an ester compound of a monohydric or polyhydric alcohol and a carboxylic acid, particularly a monohydric or polyhydric alcohol having 1 to 10 carbon atoms. Examples thereof include an ester compound of a hydric alcohol and a carboxylic acid having 2 to 10 carbon atoms, a lactone compound, and a carbonate compound. More specifically, for example, ethyl acetate, dimethyl adipate, dimethyl succinate, ethylene glycol diacetate, monoacetin, diacetin, triacetin, ethylene carbonate, γ-butyrolactone, propiolactone, ε-caprolactone, or a mixture thereof. . The amount of the gaseous or liquid organic acid ester-based curing agent used is preferably in the range of 5 to 110% by weight, particularly 20 to 60% by weight, based on the binder solution.
【0011】気体状の硬化剤による鋳造用鋳型の製造
は、粒状耐火性骨材と粘結剤とを慣用の方法によって混
合し、成形することによって行う。通気性のよい中子取
りと鋳型枠もまた、従来のガス硬化法で使用されている
慣用型のものを使用することができる。粒状耐火性骨材
と粘結剤の有機溶剤、水等の溶液とを配合した混合物を
成形した型には、蟻酸メチル等の気体状の有機酸エステ
ルを、通常、不活性担時体ガス中の蒸気又はエアロゾル
として、常温あるいはそれより若干高い温度で通過・吸
収させて硬化させる。硬化剤の吸収に要する時間は、型
の大きさと形状及び樹脂の種類に依存するが、数秒間か
ら数分間の範囲である場合がほとんどである。硬化剤吸
収後、鋳型を枠から取り出す際、鋳型の損傷を防止する
ためには、十分な時間放置してから枠から鋳型を取り出
すのが好ましい。この時間は、鋳型に加温した不活性担
持体ガスを通過させることによって短縮することができ
る。The production of a casting mold using a gaseous hardener is carried out by mixing a granular refractory aggregate and a binder by a conventional method and molding. For the core and mold frame having good air permeability, the conventional ones used in the conventional gas curing method can be used. A gaseous organic acid ester such as methyl formate is usually added to a mold in which a mixture of a granular refractory aggregate and a solution of an organic solvent for a binder and water is molded. As a vapor or aerosol at room temperature or at a temperature slightly higher than that, and is cured. The time required for absorption of the curing agent depends on the size and shape of the mold and the type of resin, but in most cases ranges from several seconds to several minutes. When removing the mold from the frame after absorbing the hardener, it is preferable to leave the mold for a sufficient time before removing the mold from the frame in order to prevent damage to the mold. This time can be reduced by passing a heated inert carrier gas through the mold.
【0012】液体状の硬化剤による鋳造用鋳型の製造
は、粒状耐火性骨材と粘結剤の溶液と液体状有機酸エス
テルとを慣用の方法によって混合し、成形することによ
って行う。粒状耐火性骨材と粘結剤の有機溶剤、水等の
溶液と液体状有機酸エステルとを配合した混合物を成形
した型は、常温あるいはそれより若干高い温度で一定時
間放置して硬化させる。硬化時間は、型の大きさと形状
及び樹脂の種類に依存するが、1時間から24時間の範
囲である場合がほとんどである。本発明における粘結剤
(50%溶液として)は、粒状耐火性骨材に対して、
0.5〜8重量%の範囲で配合するのが好ましい。成形
鋳型の圧縮強度などの点からは、1〜3重量%の範囲で
配合するのが特に好ましい。The production of a casting mold using a liquid hardening agent is carried out by mixing and molding a solution of a granular refractory aggregate, a binder and a liquid organic acid ester by a conventional method. A mold formed by mixing a mixture of a granular refractory aggregate, a solution of a binder in an organic solvent, water or the like, and a liquid organic acid ester is allowed to cure at room temperature or a slightly higher temperature for a certain period of time. The curing time depends on the size and shape of the mold and the type of the resin, but is usually in the range of 1 hour to 24 hours. The binder (as a 50% solution) in the present invention is used for a granular refractory aggregate,
It is preferable to mix in the range of 0.5 to 8% by weight. From the viewpoint of the compressive strength of the molding mold and the like, it is particularly preferable to mix in a range of 1 to 3% by weight.
【0013】[0013]
【実施例】以下、合成実施例、合成比較例、実施例及び
比較例により本発明を更に詳細に説明するが、これらに
おいて「部」は全て「重量部」を意味し、「%」は全て
「重量%」を意味する。 合成実施例1、合成比較例1〜3 100%フェノール564部(6.0モル)と水295
部からなる水溶液中に、92%パラホルムアルデヒド3
53部(10.8モル−ホルムアルデヒド換算、以下全
て同じ)を加えた(パラホルムアルデヒド:フェノール
のモル比は1.8:1)。この混合物溶液を攪拌しなが
ら加熱し50℃になったら、35%濃塩酸6.3部
(0.06モル)を加え、同温度で一定時間ノボラック
化反応を行った。ノボラック化反応について、反応時間
を追って原料のフェノールと生成物のフェノールの2核
体化合物(オルソ体とパラ体の合計)を、中和後メタノ
ールを内部標準物質とするガスクロマトグラフィーによ
り分析した。その結果を示すグラフを図1に掲げる。次
いで、48%カセイソーダ水溶液25.0部(0.3モ
ル)をノボラック化反応液中に加えてアルカリ性にし、
更に、48.6%カセイカリ水溶液554部(4.8モ
ル)を1時間かけて徐々に添加し、反応液の温度を50
℃から85℃まで昇温し同温度で3時間攪拌した。レゾ
ール化反応の液の粘度が200cpsになったら冷却し
て、反応液100部に対して3−グリシドキシプロピル
トリメトキシシランを0.5部の比率で添加し、粘結剤
の溶液を調製した。原料仕込み量及び反応条件をまとめ
て表1に示す。EXAMPLES The present invention will be described in more detail with reference to Synthesis Examples, Synthesis Comparative Examples, Examples and Comparative Examples, where "parts" means "parts by weight" and "%" means all parts by weight. It means "% by weight". Synthesis Example 1, Synthesis Comparative Examples 1 to 3 564 parts (6.0 mol) of 100% phenol and 295 of water
Parts in an aqueous solution consisting of 92% paraformaldehyde 3
53 parts (10.8 mol-formaldehyde conversion, the same applies hereinafter) were added (the molar ratio of paraformaldehyde: phenol was 1.8: 1). When the mixture solution was heated to 50 ° C. while stirring, 6.3 parts (0.06 mol) of 35% concentrated hydrochloric acid was added, and a novolak reaction was performed at the same temperature for a certain period of time. With respect to the novolak reaction, the binuclear compound of phenol as a raw material and phenol as a product (total of ortho and para forms) was neutralized and analyzed by gas chromatography using methanol as an internal standard substance. A graph showing the results is shown in FIG. Next, 25.0 parts (0.3 mol) of a 48% aqueous sodium hydroxide solution was added to the novolak reaction solution to make it alkaline, and
Further, 554 parts (4.8 mol) of a 48.6% aqueous solution of sodium hydroxide was gradually added over 1 hour, and the temperature of the reaction solution was reduced to 50%.
The temperature was raised from 85 ° C to 85 ° C, and the mixture was stirred at the same temperature for 3 hours. When the viscosity of the resolation reaction solution reaches 200 cps, the solution is cooled, and 3-glycidoxypropyltrimethoxysilane is added in a ratio of 0.5 part to 100 parts of the reaction solution to prepare a binder solution. did. Table 1 shows the amounts of raw materials charged and the reaction conditions.
【0014】[0014]
【表1】 [Table 1]
【0015】合成実施例2〜4 100%フェノール564部(6.0モル)と水328
部からなる水溶液中に、92%パラホルムアルデヒド3
92部(12.0モル)を加えた(パラホルムアルデヒ
ド:フェノールのモル比は2.0:1)。この混合物溶
液を攪拌しながら加熱し50℃になったら、触媒として
酸性物質(0.06モル)を加え、同温度で2時間(ガ
スクロマトグラフィーによりフェノールの2核体化合物
の生成量が最大となった時点)ノボラック化反応を行っ
た。次いで、48%カセイソーダ水溶液25.0部
(0.3モル)をノボラック化反応液中に加えてアルカ
リ性にし、更に、48.6%カセイカリ水溶液554部
(4.8モル)を1時間かけて徐々に添加し、反応液の
温度を50℃から85℃まで昇温し同温度で3時間攪拌
した。レゾール化反応の液の粘度が200cpsになっ
たら冷却して、反応液100部に対して3−グリシドキ
シプロピルトリメトキシシランを0.5部の比率で添加
し、粘結剤の溶液を調製した。原料仕込み量及び反応条
件をまとめて表2に示す。Synthesis Examples 2-4 564 parts (6.0 mol) of 100% phenol and water 328
Parts in an aqueous solution consisting of 92% paraformaldehyde 3
92 parts (12.0 mol) were added (paraformaldehyde: phenol molar ratio 2.0: 1). When the mixture solution was heated to 50 ° C. with stirring, an acidic substance (0.06 mol) was added as a catalyst, and the mixture was heated at the same temperature for 2 hours (the amount of the phenol binuclear compound produced by gas chromatography was maximized). (When it became) Novolak reaction was performed. Next, 25.0 parts (0.3 mol) of a 48% aqueous sodium hydroxide solution was added to the novolak reaction solution to make it alkaline, and 554 parts (4.8 mol) of a 48.6% aqueous sodium hydroxide solution were gradually added over 1 hour. And the temperature of the reaction solution was increased from 50 ° C. to 85 ° C., and the mixture was stirred at the same temperature for 3 hours. When the viscosity of the resolation reaction solution reaches 200 cps, the solution is cooled, and 3-glycidoxypropyltrimethoxysilane is added in a ratio of 0.5 part to 100 parts of the reaction solution to prepare a binder solution. did. Table 2 shows the amounts of raw materials charged and the reaction conditions.
【0016】[0016]
【表2】 [Table 2]
【0017】合成比較例4及び5 100%フェノール564部(6.0モル)と水295
部からなる水溶液中に、92%パラホルムアルデヒドを
所定量加えた。この混合物溶液を攪拌しながら加熱し5
0℃になったら、35%濃塩酸6.3部(0.06モ
ル)を加え、同温度で1.5時間(ガスクロマトグラフ
ィーによりフェノールの2核体化合物の生成量が最大と
なった時点)ノボラック化反応を行った。次いで、48
%カセイソーダ水溶液25.0部(0.3モル)をノボ
ラック化反応液中に加えてアルカリ性にした後、92%
パラホルムアルデヒドを所定量加え、更に、48.6%
カセイカリ水溶液554部(4.8モル)を1時間かけ
て徐々に添加し、反応液の温度を50℃から85℃まで
昇温し同温度で3時間攪拌した。レゾール化反応の液の
粘度が200cpsになったら冷却して、反応液100
部に対して3−グリシドキシプロピルトリメトキシシラ
ンを0.5部の比率で添加し、粘結剤の溶液を調製し
た。原料仕込み量及び反応条件をまとめて表3に示す。Comparative Synthesis Examples 4 and 5 564 parts (6.0 mol) of 100% phenol and 295 water
A predetermined amount of 92% paraformaldehyde was added to the aqueous solution consisting of parts. This mixture solution was heated with stirring and 5
When the temperature reaches 0 ° C., 6.3 parts (0.06 mol) of 35% concentrated hydrochloric acid is added, and the mixture is heated at the same temperature for 1.5 hours (when the amount of the phenol binuclear compound produced by gas chromatography becomes maximum) ) A novolak reaction was performed. Then 48
25.0 parts (0.3 mol) of an aqueous sodium hydroxide solution were added to the novolak reaction solution to make it alkaline, and then 92%
Add a predetermined amount of paraformaldehyde, and further add 48.6%
554 parts (4.8 mol) of an aqueous solution of sodium hydroxide was gradually added over 1 hour, the temperature of the reaction solution was raised from 50 ° C. to 85 ° C., and the mixture was stirred at the same temperature for 3 hours. When the viscosity of the solution for the resolation reaction reaches 200 cps, the solution is cooled and the reaction solution 100
To each part, 3-glycidoxypropyltrimethoxysilane was added in a ratio of 0.5 part to prepare a binder solution. Table 3 summarizes the raw material charge amounts and reaction conditions.
【0018】合成比較例6 100%フェノール500部(5.3モル)と37%濃
塩酸67.5部(0.68モル)と水325部からなる
水溶液中に、37%ホルマリン水73部(0.9モル)
を30℃で1時間かけて滴下した。滴下後、反応液を
1.5時間静置した後、油層を分離した。分離した油層
250部に水250部とカセイカリ300部(5.3モ
ル)を加え、更に92%パラホルムアルデヒド173部
(5.3モル)を1時間かけて加えた。反応液を攪拌し
ながら徐々に温度を上げ、85℃で2時間攪拌した。反
応液の粘度が150cpsになったら冷却して、反応液
100部に対して3−グリシドキシプロピルトリメトキ
シシランを0.5部の比率で添加し、粘結剤の溶液を調
製した。原料仕込み量及び反応条件をまとめて表3に示
す。Comparative Example 6 In an aqueous solution consisting of 500 parts (5.3 mol) of 100% phenol, 67.5 parts (0.68 mol) of 37% concentrated hydrochloric acid and 325 parts of water, 73 parts of 37% formalin water (73 parts) 0.9 mol)
Was added dropwise at 30 ° C. over 1 hour. After the dropwise addition, the reaction solution was allowed to stand for 1.5 hours, and then the oil layer was separated. To 250 parts of the separated oil layer were added 250 parts of water and 300 parts (5.3 moles) of potassium hydroxide, and 173 parts (5.3 moles) of 92% paraformaldehyde were added over 1 hour. The temperature of the reaction solution was gradually raised while stirring, and the mixture was stirred at 85 ° C. for 2 hours. When the viscosity of the reaction solution reached 150 cps, it was cooled, and 3-glycidoxypropyltrimethoxysilane was added at a ratio of 0.5 part to 100 parts of the reaction solution to prepare a binder solution. Table 3 summarizes the raw material charge amounts and reaction conditions.
【0019】合成比較例7 100%フェノール564部(6.0モル)と水328
部からなる水溶液中に、92%パラホルムアルデヒド3
92部(12.0モル)を加えた(パラホルムアルデヒ
ド:フェノールのモル比は2.0:1)。この混合物溶
液を攪拌しながら加熱し50℃で48.6%カセイカリ
水溶液554部(4.8モル)を2時間かけて徐々に添
加し、反応液の温度を50℃から85℃まで昇温し同温
度で3時間攪拌した。反応液の粘度が200cpsにな
ったら冷却して、反応液100部に対して3−グリシド
キシプロピルトリメトキシシランを0.5部の比率で添
加し、粘結剤の溶液を調製した。原料仕込み量及び反応
条件をまとめて表3に示す。Synthesis Comparative Example 7 564 parts (6.0 mol) of 100% phenol and water 328
Parts in an aqueous solution consisting of 92% paraformaldehyde 3
92 parts (12.0 mol) were added (paraformaldehyde: phenol molar ratio 2.0: 1). The mixture solution was heated with stirring, and 554 parts (4.8 mol) of a 48.6% aqueous solution of sodium hydroxide was added gradually at 50 ° C. over 2 hours, and the temperature of the reaction solution was raised from 50 ° C. to 85 ° C. The mixture was stirred at the same temperature for 3 hours. When the viscosity of the reaction solution reached 200 cps, the solution was cooled, and 3-glycidoxypropyltrimethoxysilane was added at a ratio of 0.5 part to 100 parts of the reaction solution to prepare a binder solution. Table 3 summarizes the raw material charge amounts and reaction conditions.
【0020】[0020]
【表3】 [Table 3]
【0021】実施例1〜4、比較例1〜7 三河V6珪砂3000部に各合成実施例、各合成比較例
において製造した粘結剤の溶液を60部加え90秒間混
合して、混練砂を調製した。この混練砂を直ちにあるい
は24時間経過後に木型枠内に収納して成形し、この成
形物中に蟻酸メチル30部を含む蟻酸メチル−空気混合
ガスを常温で作用させて、直径50mm、高さ50mm
の鋳型試験片を製造した。製造した鋳型試験片の圧縮強
度を表4、表5及び表6に示す。 〔圧縮強度試験方法〕 鋳型試験片を製造した後、常温(20℃)、50%相対
温度での硬化5分経過後、1時間経過後あるいは硬化2
4時間経過後における鋳型試験片の圧縮強度(kgf/
cm2 )を測定。Examples 1 to 4 and Comparative Examples 1 to 7 To 3000 parts of Mikawa V6 silica sand, 60 parts of the binder solution prepared in each of the Synthesis Examples and Comparative Examples was added and mixed for 90 seconds to obtain a kneaded sand. Prepared. The kneaded sand is immediately or after 24 hours, housed in a wooden form and molded, and a methyl formate-air mixed gas containing 30 parts of methyl formate is allowed to act on the molded product at room temperature to obtain a diameter of 50 mm and a height of 50 mm. 50mm
Was prepared. Tables 4, 5 and 6 show the compressive strengths of the manufactured mold test pieces. [Compression strength test method] After manufacturing a mold test piece, after 5 minutes of curing at room temperature (20 ° C) and 50% relative temperature, after 1 hour, or after curing 2
After 4 hours, the compressive strength (kgf /
cm 2 ).
【0022】[0022]
【表4】 [Table 4]
【0023】[0023]
【表5】 [Table 5]
【0024】[0024]
【表6】 [Table 6]
【0025】[0025]
【発明の効果】以上説明したとおり、本発明により、粒
状耐火性骨材と混合した際の可使時間が長い粘結剤が得
られ、それを使用して製造される鋳造用鋳型は圧縮強度
などが高く収縮が小さいという顕著な効果が得られる。As described above, according to the present invention, a binder having a long pot life when mixed with a granular refractory aggregate is obtained, and a casting mold manufactured using the same has a compressive strength. The remarkable effect of high shrinkage and small shrinkage can be obtained.
【図1】ノボラック化反応において、反応時間の経過に
よる原料のフェノールと生成物のフェノールの2核体化
合物の変化をガスクロマトグラフィーにより分析した結
果を示すグラフである。BRIEF DESCRIPTION OF DRAWINGS FIG. 1 is a graph showing the results of analyzing, by gas chromatography, a change in a binuclear compound of phenol as a raw material and phenol as a product over time in a novolak reaction.
───────────────────────────────────────────────────── フロントページの続き (72)発明者 塩川 盛雄 神奈川県横浜市鶴見区大黒町7番43号 保土谷アシュランド株式会社 技術研究 所内 (56)参考文献 特公 昭35−17247(JP,B1) (58)調査した分野(Int.Cl.7,DB名) B22C 1/00 - 1/26 ──────────────────────────────────────────────────続 き Continuation of the front page (72) Inventor Morio Shiokawa 7-43, Oguro-cho, Tsurumi-ku, Yokohama-shi, Kanagawa Prefecture Hodogaya Ashland Co., Ltd. Technical Research Institute (56) References JP-B 35-17247 (JP, B1 (58) Field surveyed (Int. Cl. 7 , DB name) B22C 1/00-1/26
Claims (2)
を1.6〜2.5モルの比率でpKa2.0以下の酸性
物質に基づく酸性状態下でノボラック化反応を行わせ、
フェノール類の2核体化合物の生成量が最大となった時
点で反応液をアルカリ性にし、更にアルカリ性状態下で
レゾール化反応を行わせて得られる水溶性フェノール樹
脂を必須成分とする粘結剤と、粒状耐火性骨材とを混合
し、この混合物を鋳型枠内に収納して成形し、次いでこ
の成形物に気体状の有機酸エステル系硬化剤を通過させ
て硬化させること、を特徴とする鋳造用鋳型の製造方
法。1. A novolak reaction is carried out in an acidic state based on an acidic substance having a pKa of 2.0 or less at a ratio of 1.6 to 2.5 moles of an aldehyde to 1 mole of a phenol,
At the time when the amount of the binuclear compound of phenols is maximized, the reaction solution is made alkaline, and a binder containing a water-soluble phenol resin obtained by performing a resolving reaction under an alkaline condition as an essential component is further included. Mixed with a granular refractory aggregate, housed in a mold frame and molded, and then cured by passing a gaseous organic acid ester-based curing agent through the molded product. Manufacturing method of casting mold.
を1.6〜2.5モルの比率でpKa2.0以下の酸性
物質に基づく酸性状態下でノボラック化反応を行わせ、
フェノール類の2核体化合物の生成量が最大となった時
点で反応液をアルカリ性にし、更にアルカリ性状態下で
レゾール化反応を行わせて得られる水溶性フェノール樹
脂を必須成分とする粘結剤と、液体状有機酸エステル系
硬化剤と、粒状耐火性骨材とを混合し、この混合物を鋳
型枠内に収納して成形し硬化させること、を特徴とする
鋳造用鋳型の製造方法。2. A novolak reaction is carried out in an acidic state based on an acidic substance having a pKa of 2.0 or less at a ratio of 1.6 to 2.5 moles of aldehyde to 1 mole of phenol,
At the time when the amount of the binuclear compound of phenols is maximized, the reaction solution is made alkaline, and a binder containing a water-soluble phenol resin obtained by performing a resolving reaction under an alkaline condition as an essential component is further included. Mixing a liquid organic acid ester-based curing agent and a granular refractory aggregate, storing the mixture in a mold frame, and molding and curing the mixture.
Priority Applications (1)
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---|---|---|---|
JP12471094A JP3249010B2 (en) | 1994-05-16 | 1994-05-16 | Manufacturing method of casting mold |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP12471094A JP3249010B2 (en) | 1994-05-16 | 1994-05-16 | Manufacturing method of casting mold |
Publications (2)
Publication Number | Publication Date |
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JPH07308732A JPH07308732A (en) | 1995-11-28 |
JP3249010B2 true JP3249010B2 (en) | 2002-01-21 |
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ID=14892194
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JP12471094A Expired - Lifetime JP3249010B2 (en) | 1994-05-16 | 1994-05-16 | Manufacturing method of casting mold |
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KR100336978B1 (en) * | 1995-12-29 | 2002-11-07 | 고려화학 주식회사 | Binder resin composition for casting |
WO2010117022A1 (en) * | 2009-04-10 | 2010-10-14 | 花王株式会社 | Curing agent composition |
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1994
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