JPS6337141B2 - - Google Patents

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Publication number
JPS6337141B2
JPS6337141B2 JP60272476A JP27247685A JPS6337141B2 JP S6337141 B2 JPS6337141 B2 JP S6337141B2 JP 60272476 A JP60272476 A JP 60272476A JP 27247685 A JP27247685 A JP 27247685A JP S6337141 B2 JPS6337141 B2 JP S6337141B2
Authority
JP
Japan
Prior art keywords
inorganic material
unsaturated polyester
scale
weight
resin
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
JP60272476A
Other languages
Japanese (ja)
Other versions
JPS61166851A (en
Inventor
Katsuhiro Sansen
Masaaki Kagawa
Toshiaki Hanyuda
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 Holdings Corp
Original Assignee
Showa Highpolymer 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 Showa Highpolymer Co Ltd filed Critical Showa Highpolymer Co Ltd
Priority to JP27247685A priority Critical patent/JPS61166851A/en
Publication of JPS61166851A publication Critical patent/JPS61166851A/en
Publication of JPS6337141B2 publication Critical patent/JPS6337141B2/ja
Granted legal-status Critical Current

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  • Processes Of Treating Macromolecular Substances (AREA)
  • Compositions Of Macromolecular Compounds (AREA)

Description

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

〔産業上の利用分野〕 本発明は、耐水性、耐蝕性に優れ、特に塗料お
よびライニングに適する不飽和ポリエステル樹脂
コンパウンドの製造方法に関する。 〔従来の技術〕 従来、塗膜の耐水性、耐蝕性を改良するため
に、不飽和ポリエステル等の硬化性樹脂にガラス
繊維あるいはフレーク状の無機質材料を添加した
ライニング用樹脂組成物については知られてい
る。かかる場合にライニング層の特性は、樹脂と
ガラス繊維あるいはフレーク状の無機質材料との
結合状態によつて左右される。すなわち、結合力
強化がライニング層の特性を改善することは云う
までもない。 樹脂とガラス繊維あるいはフレーク状の無機質
材料との結合力を強化するために、樹脂と無機質
材料を混合する際に単にシランカツプリング剤を
同時に混合する方法(“インテグラル法”と云わ
れる)が知られている。しかし、その効果は常に
安定して発揮させるまでに至つていない。 また、樹脂に添加する鱗片状の無機質材料を、
予めシランカツプリング剤の水またはアルコール
希釈液で濡らして処理する方法についてもよく知
られている。しかし、この場合には乾燥工程にお
いて鱗片状無機質材料が凝集するか、材料内の希
釈液が残留して塗膜またはライニング層の特性に
悪影響を与え、また必要以上の乾燥はシランカツ
プリング剤の。飛散ロスを伴い実用的でない。 〔発明が解決しようとする問題点〕 本発明者らは、前記情勢に鑑み、不飽和ポリエ
ステル樹脂を用いた耐水性、耐蝕性の優れた防蝕
性樹脂塗料およびライニングを得るべく鋭意検討
を重ねた結果、特定方法で処理したフレーク状の
無機質材料を不飽和ポリエステル樹脂に添加混合
して樹脂コンパウンドを製造することによつて、
耐水性および耐蝕性に優れた塗料およびライニン
グが得られることを見出し、本発明に到達した。 〔問題点を解決するための手段〕 即ち、本発明方法は、重合性単量体にシランカ
ツプリング剤を、鱗片状の無機質材料の100重量
部当り0.5〜5重量部に相当する範囲で溶解また
は乳化分散させた130℃以下の溶液に、その径が
3mmφ以下、厚さ1〜10ミクロンの鱗片状の無機
質材料を130℃以下で浸漬して得られる、未だ湿
潤状態にある無機質材料を、不飽和ポリエステル
と重合性単量体よりなる樹脂液に、樹脂液に対し
20〜50重量%の範囲で添加混合することを特徴と
する、不飽和ポリエステル樹脂コンパウンドの製
造方法である。 〔作用〕 本発明方法においては、重合性単量体が完全に
乾燥飛散しない状態即ち湿潤状態にある無機質材
料が樹脂液と混合されるので、樹脂中での無機質
材料の凝集が防止され、また無機質材料中に吸着
残留している0.1%以下の微量の水分がカツプリ
ング反応を促進するものと考えられる。 本発明に用いられるシランカツプリング剤を溶
解または乳化分散させる重合性単量体と不飽和ポ
リエステルを溶解するために用いられる重合性単
量体とは同一物であることが望ましいが、別の重
合性単量体を希釈剤として併用することもでき
る。かかる重合性単量体の例としては、スチレン
が一般的であるが、クロルスチレン、ビニルトル
エン、トリエチレングリコールジメタクリレート
なども有用である。 本発明に用いられるシランカツプリング剤は、
ビニルトリエトキシシラン、ビニルトリス(β−
メトキシエトキシ)シラン、γ−グリシドキシプ
ロピルトリメトキシシラン、γ−メタアクリロキ
シプロピルトリメトキシシラン、N−β(アミノ
エチル)γ−アミノプロピルトリメトキシシラン
などであり、処理する無機質材料に応じて選択さ
れる。 本発明に用いられる鱗片状の無機質材料は、無
機質材料としてガラスフレーク、雲母、タルタ、
グラフアイト、人工雲母、アルミナなどから選択
され、鱗片状としてその径が3mmφ以下好ましく
は1〜3mmφ、厚さが1〜10μ範囲のものが挙げ
られる。 鱗片状の無機質材料を処理する際の重合性単量
体とシランカツプリング剤の量は、無機質材料の
種類、大きさなどにより異なるが、重合性単量体
は無機質材料を浸漬するに足る量以上あればよ
く、またシランカツプリング剤は無機質材料の
100重量部当り0.5〜5重量部の範囲で有効であ
る。処理温度は130℃以下好適には60〜130℃の範
囲が好ましく、60℃以下では処理に長時間を要
し、また130℃以上では単量体とシランカツプリ
ング剤との反応によるゲル化、シランカツプリン
グ剤の分解などを伴い好ましくない。処理時間は
室温の場合一週間、60〜130℃の場合5〜60分間
程度が必要である。 本発明に用いられる不飽和ポリエステルは重合
性単量体に溶解して用いられるが、この際に先に
カツプリング剤で処理された鱗片状の無機質材料
が添加される。重合性単量体を含む不飽和ポリエ
ステル樹脂に対する無機質材料の重量比は、80:
20〜50:50、好ましくは75:25〜60:40の範囲で
有効である。 不飽和ポリエステル樹脂に用いられる重合触媒
は、有機過酸化物たとえば過酸化ベンゾイル、メ
チルエチルケトンパーオキサイド、キユメンハイ
ドロパーオキサイドなどであり、目的に応じて選
択することができる。 その他の配合剤としては、商品価値を高めるた
めに遥変剤たとえば微粉シリカ、石綿粉末、有機
アミンを配合した粘土質(ベーカ社製“ベント
ン”)、脱水ヒマシ油、ソルビトールとベンズアル
デヒドの縮合アセタール化合物、金属キレートや
金属せつけんなど、また顔料たとえばチタン白、
補強材としてガラス繊維、合成繊維、硬化促進剤
たとえば金属せつけんん、ジメチルアニリン、ア
セチルアセトンなど空気乾燥剤としてパラフイ
ン、エチルセルロースなどを少量添加することが
できる。 〔実施例〕 次に本発明の理解を助けるために以下に実施例
を示す。 実施例 1 還流装置付のフラスコに、γ−メタクリロキシ
プロピルトリメトキシシランの1重量%スチレン
溶液700g、ガラスフレーク(径1〜3mmφ、平
均厚さ3μ)300gを投入し、100℃で20分間熱処
理したる後、吸引ロートにて過剰のスチレンを除
去し未だ表面が湿潤状態にある該ガラスフレーク
を不飽和ポリエステル樹脂(昭和高分子(株)製“リ
ゴラツクLP−1”)700gに混合し、150mmHgの
減圧マーラーを用いて混練し、ガラスフレーク含
有率30重量%になるようにモノマー量を調節して
樹脂コンパウンド(A)を得た。該コンパウンド(A)を
用いた硬化物の吸水率特性を第1表に後記する。 実施例 2 ビニルトリス(β−メトキシエトキシ)シラン
の0.6重量%スチレン溶液1500gにガラスフレー
ク(平均粒径1mmφ、厚さ3μ)300gを撹拌しな
がら投入し、室温で1週間放置した後、吸引ロー
トと紙を用いて過剰のスチレンを除去し、未だ
表面がスチレンで湿潤状態にあるガラスフレーク
を110℃のオーブン中で10分間熱処理したる後、
不飽和ポリエステル樹脂(昭和高分子(株)製“リゴ
ラツク2141”)700gに混合し、減圧ニーダーを用
いて150mmHg下で混練し、ガラスフレーク含有率
30重量%の樹脂コンパウンド(B)を得た。該コンパ
ウンド(B)を用いた硬化物の吸収率特性を第1表に
後記する。 比較例 1 不飽和ポリエステル樹脂(昭和高分子(株)製“リ
ゴラツクLP−1”)700gにγ−メタクリロキシ
プロピルトリメトキシシランの1重量%を加え、
しかる後ガラスフレーク300gを加えて、150mm
Hgの減圧マーラを用いて10分間混練し、ガラス
フレーク含有率30重量%の樹脂コンパウンド
(A′)を得た。該コンパウンド(A′)を用いた硬
化物の吸水率特性を第1表に後記する。 比較例 2 不飽和ポリエステル樹脂(昭和高分子(株)製“リ
ゴラツク2141”)700gにビニルトリス(β−メト
キシエトキシ)シランの0.6重量%を加え、さら
にガラスフレーク300gを添加し、150mmHgの減
圧ニーダーを用いて10分間混練し、ガラスフレー
ク含有率30重量%の樹脂コンパウンド(B′)を
得た。該コンパウンド(B′)を用いた硬化物の
吸水率特性を第1表に後記する。 以上の実施例1〜2、比較例1〜2の樹脂コン
パウンド、各100重量部に、それぞれ重量部でメ
チルエチルケトンパーオキサイド(55%フタル酸
ジメチル溶液として)1.0部、ナフテン酸コバル
ト(コバルト含有率6%の溶液)0.5部、ジメチ
ルアニリン0.02部を添加し、厚さ1.0mmの試験片
をコテ塗工法により成形し、120℃、2時間の後
硬化を行つた。かくして得られた試験片を沸騰水
中に150時間浸漬した場合の吸水率特性を次の第
1表に示す。本発明方法の効果が認められた。
[Industrial Application Field] The present invention relates to a method for producing an unsaturated polyester resin compound that has excellent water resistance and corrosion resistance and is particularly suitable for paints and linings. [Prior Art] Hitherto, there has been no known lining resin composition in which glass fiber or flake-like inorganic material is added to a curable resin such as unsaturated polyester in order to improve the water resistance and corrosion resistance of the coating film. ing. In such cases, the properties of the lining layer depend on the bonding state between the resin and the glass fiber or flaky inorganic material. That is, it goes without saying that strengthening the bonding strength improves the properties of the lining layer. In order to strengthen the bond between resin and glass fiber or flake-like inorganic material, there is a method (referred to as the "integral method") in which a silane coupling agent is simply mixed at the same time as the resin and inorganic material are mixed. Are known. However, this effect has not yet been achieved consistently and consistently. In addition, the scale-like inorganic material added to the resin,
A method of pre-wetting a silane coupling agent with a diluted solution of water or alcohol is also well known. However, in this case, the scale-like inorganic material aggregates during the drying process, or the diluted liquid in the material remains, which adversely affects the properties of the coating film or lining layer. . It is not practical due to scattering loss. [Problems to be Solved by the Invention] In view of the above situation, the present inventors have conducted extensive studies in order to obtain a corrosion-resistant resin paint and lining that uses unsaturated polyester resin and has excellent water resistance and corrosion resistance. As a result, by adding and mixing flake-like inorganic material treated with a specific method to unsaturated polyester resin to produce a resin compound,
It was discovered that a paint and lining with excellent water resistance and corrosion resistance can be obtained, and the present invention was achieved. [Means for solving the problem] That is, the method of the present invention involves dissolving a silane coupling agent in a polymerizable monomer in an amount corresponding to 0.5 to 5 parts by weight per 100 parts by weight of the scale-like inorganic material. Alternatively, a scale-like inorganic material with a diameter of 3 mmφ or less and a thickness of 1 to 10 microns is immersed at 130°C or less in an emulsified and dispersed solution at 130°C or less, which is still in a wet state. For resin liquid made of unsaturated polyester and polymerizable monomer,
This is a method for producing an unsaturated polyester resin compound, characterized by adding and mixing in a range of 20 to 50% by weight. [Function] In the method of the present invention, since the inorganic material in which the polymerizable monomer is not completely dried and scattered, that is, in a wet state, is mixed with the resin liquid, aggregation of the inorganic material in the resin is prevented, and It is thought that a trace amount of moisture of 0.1% or less adsorbed and remaining in the inorganic material promotes the coupling reaction. It is desirable that the polymerizable monomer for dissolving or emulsifying and dispersing the silane coupling agent used in the present invention and the polymerizable monomer used for dissolving the unsaturated polyester are the same; A monomer can also be used in combination as a diluent. As an example of such a polymerizable monomer, styrene is generally used, but chlorostyrene, vinyltoluene, triethylene glycol dimethacrylate, and the like are also useful. The silane coupling agent used in the present invention is
Vinyltriethoxysilane, vinyltris (β-
methoxyethoxy) silane, γ-glycidoxypropyltrimethoxysilane, γ-methacryloxypropyltrimethoxysilane, N-β(aminoethyl)γ-aminopropyltrimethoxysilane, etc., depending on the inorganic material being treated. selected. The scale-like inorganic material used in the present invention includes glass flakes, mica, tarta,
It is selected from graphite, artificial mica, alumina, etc., and has a scale-like shape with a diameter of 3 mmφ or less, preferably 1 to 3 mmφ, and a thickness in the range of 1 to 10 μm. The amount of polymerizable monomer and silane coupling agent when treating scale-like inorganic materials varies depending on the type and size of the inorganic material, but the amount of polymerizable monomer is sufficient to soak the inorganic material. or more is sufficient, and the silane coupling agent is suitable for inorganic materials.
A range of 0.5 to 5 parts by weight per 100 parts by weight is effective. The treatment temperature is preferably 130°C or lower, preferably in the range of 60 to 130°C. At 60°C or lower, the treatment takes a long time, and at 130°C or higher, gelation occurs due to the reaction between the monomer and the silane coupling agent. This is undesirable as it causes decomposition of the silane coupling agent. The processing time is one week at room temperature, and about 5 to 60 minutes at 60 to 130°C. The unsaturated polyester used in the present invention is used after being dissolved in a polymerizable monomer, and at this time, a scale-like inorganic material that has been previously treated with a coupling agent is added. The weight ratio of the inorganic material to the unsaturated polyester resin containing the polymerizable monomer is 80:
A range of 20-50:50, preferably 75:25-60:40 is effective. The polymerization catalyst used for the unsaturated polyester resin is an organic peroxide such as benzoyl peroxide, methyl ethyl ketone peroxide, kyumene hydroperoxide, etc., and can be selected depending on the purpose. Other additives that can be used to increase commercial value include finely powdered silica, asbestos powder, clay containing organic amines (Bentone manufactured by Beca), dehydrated castor oil, and a condensed acetal compound of sorbitol and benzaldehyde. , such as metal chelates and metal soaps, and also pigments such as titanium white,
Glass fibers, synthetic fibers, curing accelerators such as metal soap, dimethylaniline, acetylacetone, and air drying agents such as paraffin and ethyl cellulose may be added in small amounts as reinforcing materials. [Examples] Next, examples will be shown below to help understand the present invention. Example 1 700 g of a 1% by weight styrene solution of γ-methacryloxypropyltrimethoxysilane and 300 g of glass flakes (diameter 1 to 3 mmφ, average thickness 3 μ) were placed in a flask equipped with a reflux device, and heat treated at 100°C for 20 minutes. After that, excess styrene was removed using a suction funnel, and the glass flakes, whose surfaces were still wet, were mixed with 700 g of unsaturated polyester resin ("Rigorakku LP-1" manufactured by Showa Kobunshi Co., Ltd.) and heated at 150 mmHg. A resin compound (A) was obtained by kneading the mixture using a vacuum muller and adjusting the amount of monomer so that the glass flake content was 30% by weight. The water absorption characteristics of the cured product using the compound (A) are listed in Table 1 below. Example 2 300 g of glass flakes (average particle size 1 mmφ, thickness 3 μ) were added to 1500 g of a 0.6% by weight styrene solution of vinyltris(β-methoxyethoxy)silane with stirring, and after being left at room temperature for one week, a suction funnel was added. Excess styrene was removed using paper, and the glass flakes, whose surfaces were still wet with styrene, were heat-treated in an oven at 110°C for 10 minutes.
It was mixed with 700 g of unsaturated polyester resin (“Rigorak 2141” manufactured by Showa Kobunshi Co., Ltd.) and kneaded at 150 mmHg using a vacuum kneader to determine the glass flake content.
A 30% by weight resin compound (B) was obtained. The absorption characteristics of the cured product using the compound (B) are listed in Table 1 below. Comparative Example 1 1% by weight of γ-methacryloxypropyltrimethoxysilane was added to 700 g of unsaturated polyester resin (“Rigorak LP-1” manufactured by Showa Kobunshi Co., Ltd.),
After that, add 300g of glass flakes and make it 150mm.
The mixture was kneaded for 10 minutes using a Hg vacuum mala to obtain a resin compound (A') with a glass flake content of 30% by weight. The water absorption characteristics of the cured product using the compound (A') are shown in Table 1 below. Comparative Example 2 0.6% by weight of vinyl tris (β-methoxyethoxy) silane was added to 700 g of unsaturated polyester resin (“Rigorak 2141” manufactured by Showa Kobunshi Co., Ltd.), 300 g of glass flakes were added, and the mixture was heated in a vacuum kneader at 150 mmHg. A resin compound (B') having a glass flake content of 30% by weight was obtained by kneading for 10 minutes. The water absorption characteristics of the cured product using the compound (B') are listed in Table 1 below. To 100 parts by weight of each of the resin compounds of Examples 1 and 2 and Comparative Examples 1 and 2, 1.0 part of methyl ethyl ketone peroxide (as a 55% dimethyl phthalate solution) and cobalt naphthenate (cobalt content 6) were added. % solution) and 0.02 part of dimethylaniline were added, a test piece with a thickness of 1.0 mm was formed by a trowel coating method, and post-curing was performed at 120°C for 2 hours. Table 1 below shows the water absorption characteristics when the test piece thus obtained was immersed in boiling water for 150 hours. The effect of the method of the present invention was recognized.

〔発明の効果〕〔Effect of the invention〕

本発明方法で得られる不飽和ポリエステル樹脂
コンパウンドは、耐水性および耐蝕性にすぐれた
塗料およびライニングとした有用である。
The unsaturated polyester resin compounds obtained by the method of the present invention are useful as coatings and linings with excellent water resistance and corrosion resistance.

Claims (1)

【特許請求の範囲】[Claims] 1 重合性単量体にシランカツプリング剤を、鱗
片状の無機質材料の100重量部当り0.5〜5重量部
に相当する範囲で溶解または乳化分散させた溶液
に、その径が3mmφ以下、厚さ1〜10ミクロンの
鱗片状の無機質材料を130℃以下で浸漬して得ら
れる、未だ湿潤状態にある鱗片状の無機質材料
を、不飽和ポリエステルと重合性単量体よりなる
樹脂液に添加混合することを特徴とする耐水性、
耐蝕性の優れた塗料およびライニングに適する不
飽和ポリエステル樹脂コンパウンドの製造方法。
1. In a solution in which a silane coupling agent is dissolved or emulsified in a polymerizable monomer in an amount equivalent to 0.5 to 5 parts by weight per 100 parts by weight of a scale-like inorganic material, the diameter is 3 mmφ or less and the thickness is The still-wet scale-like inorganic material obtained by soaking the scale-like inorganic material of 1 to 10 microns at 130°C or lower is added to and mixed with a resin liquid consisting of unsaturated polyester and a polymerizable monomer. Water resistance, characterized by
A method for producing an unsaturated polyester resin compound suitable for coatings and linings with excellent corrosion resistance.
JP27247685A 1985-12-05 1985-12-05 Production of resin compound Granted JPS61166851A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP27247685A JPS61166851A (en) 1985-12-05 1985-12-05 Production of resin compound

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP27247685A JPS61166851A (en) 1985-12-05 1985-12-05 Production of resin compound

Related Parent Applications (1)

Application Number Title Priority Date Filing Date
JP10948376A Division JPS5335782A (en) 1976-09-14 1976-09-14 Preparation of resin compounds

Publications (2)

Publication Number Publication Date
JPS61166851A JPS61166851A (en) 1986-07-28
JPS6337141B2 true JPS6337141B2 (en) 1988-07-22

Family

ID=17514453

Family Applications (1)

Application Number Title Priority Date Filing Date
JP27247685A Granted JPS61166851A (en) 1985-12-05 1985-12-05 Production of resin compound

Country Status (1)

Country Link
JP (1) JPS61166851A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH04259420A (en) * 1991-02-14 1992-09-16 Matsushita Electric Ind Co Ltd Coffee extractor

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5020928A (en) * 1987-05-25 1991-06-04 Seiko Epson Corporation Ribbon guiding mechanism
US5052832A (en) * 1987-05-25 1991-10-01 Seiko Epson Corporation Print head and roller biasing mechanism for a hand held thermal printer
CN103772925B (en) * 2013-12-11 2015-10-14 浙江南益生物科技有限公司 A kind of liquid nano mica modification agent for PLA

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5054634A (en) * 1973-09-14 1975-05-14
JPS5335782A (en) * 1976-09-14 1978-04-03 Showa Highpolymer Co Ltd Preparation of resin compounds

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5054634A (en) * 1973-09-14 1975-05-14
JPS5335782A (en) * 1976-09-14 1978-04-03 Showa Highpolymer Co Ltd Preparation of resin compounds

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH04259420A (en) * 1991-02-14 1992-09-16 Matsushita Electric Ind Co Ltd Coffee extractor

Also Published As

Publication number Publication date
JPS61166851A (en) 1986-07-28

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