JPH03199274A - Chlorinated polyolefin coating composition - Google Patents

Chlorinated polyolefin coating composition

Info

Publication number
JPH03199274A
JPH03199274A JP34465989A JP34465989A JPH03199274A JP H03199274 A JPH03199274 A JP H03199274A JP 34465989 A JP34465989 A JP 34465989A JP 34465989 A JP34465989 A JP 34465989A JP H03199274 A JPH03199274 A JP H03199274A
Authority
JP
Japan
Prior art keywords
chlorination
polyolefin
solvent
coating composition
chlorinated
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.)
Granted
Application number
JP34465989A
Other languages
Japanese (ja)
Other versions
JP2567287B2 (en
Inventor
Kazuo Shimizu
一夫 清水
Toshihide Takahashi
利英 高橋
Tadao Kimura
木村 忠男
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.)
Sanyo Kokusaku Pulp Co Ltd
Original Assignee
Sanyo Kokusaku Pulp 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 Sanyo Kokusaku Pulp Co Ltd filed Critical Sanyo Kokusaku Pulp Co Ltd
Priority to JP1344659A priority Critical patent/JP2567287B2/en
Publication of JPH03199274A publication Critical patent/JPH03199274A/en
Application granted granted Critical
Publication of JP2567287B2 publication Critical patent/JP2567287B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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Abstract

PURPOSE:To provide the title composition of high weatherability, containing a solvent-soluble chlorinated polyolefin produced by suspending pulverized polyolefin powder in an aqueous medium followed by chlorination. CONSTITUTION:The objective composition containing a chlorinated polyolefin produced by suspending pulverized polyolefin powder with a specific surface area of 300-20000cm<2>/g in an aqueous medium followed by chlorination. It is preferable that until completion of the chlorination, the disintegration treatment along with grinding treatment of the polyolefin granules under chlorination be made either repeatedly at least once or continuously.

Description

【発明の詳細な説明】 〔産業上の利用分野〕 本発明は、水媒法による塩素化ポリオレフィンを用いた
耐候性の良好な塗料用組成物に関するものである。
DETAILED DESCRIPTION OF THE INVENTION [Industrial Field of Application] The present invention relates to a coating composition with good weather resistance using a chlorinated polyolefin produced by a water-based method.

〔従来の技術〕[Conventional technology]

水媒系製法によるポリオレフィンの塩素化物は溶媒性塩
素化物と比較して塩素化の不均一性に由来する特徴から
成形品、樹脂の改質材用に用いられている。
Chlorinated polyolefins produced by a water-based method are used for molded products and resin modifiers due to their characteristics due to non-uniformity of chlorination compared to solvent-based chlorinated products.

しかし従来の水媒系塩化ポリオレフィンは通常使用され
る安価な溶剤(例えばトルエン、キシレン)中では均一
な溶液を作ることができず、加熱溶解する方法も提案さ
れているが(特開昭54−153853 ) 、All
’j足できるものではない。従って塗料用に用いること
が困難である。
However, it is not possible to make a homogeneous solution of conventional water-based chlorinated polyolefins in commonly used inexpensive solvents (e.g. toluene, xylene), and a method of dissolving them by heating has been proposed (Japanese Patent Application Laid-Open No. 1983-1989-1). 153853), All
'j It's not something I can do. Therefore, it is difficult to use it for paints.

一方従来の耐塩素溶媒中で塩素化されたものは、均一反
応ゆえに分子量巾が狭く、従って硬い波膜が形成される
樹脂となり、塗料用バインダーとして用いる場合、樹脂
100部に対しη■塑剤を常に40〜45部必要とされ
、従って耐候性に弱く経時的に塗膜が劣化する欠点を有
する。
On the other hand, when chlorinated in a conventional chlorine-resistant solvent, the molecular weight range is narrow due to a homogeneous reaction, resulting in a resin that forms a hard wave film.When used as a paint binder, η 40 to 45 parts is always required, and therefore has the drawback of poor weather resistance and deterioration of the coating film over time.

〔発明が解決しようとする課題〕[Problem to be solved by the invention]

不発明音らは可塑剤を大量に要しない耐候性のある塗膜
1用樹脂を開発すべく鋭意検討を行い、その結果、水性
媒体中で溶剤可溶となる条件で塩素化を行なえば粉体樹
脂の表面から塩素化され不均一反応体が形成され、塩素
化度に巾を持たせる事ができ、併せて分子量巾が広くな
る事より、可撓性のある塩素化樹脂が得られることを見
出し本発明に到達した。
Fugenon et al. conducted extensive research to develop a weather-resistant resin for coating film 1 that does not require large amounts of plasticizer, and found that if chlorinated under conditions that make it soluble in solvents in an aqueous medium, it can be used as a powder. The surface of the body resin is chlorinated to form a heterogeneous reactant, and the degree of chlorination can vary widely. At the same time, the molecular weight range is widened, making it possible to obtain a flexible chlorinated resin. This discovery led to the present invention.

これにより塗料用バインダーとして用いる場合、可争剤
の添加量を大巾に減らす事ができ、可塑剤に起因する塗
膜の劣化が生じにくく必然的に耐候性の良好な塗膜が得
られる。
As a result, when used as a paint binder, the amount of additives added can be greatly reduced, and a coating film with good weather resistance is naturally obtained, with less deterioration of the coating film caused by plasticizers.

〔課題を解決するための手段と作用〕[Means and actions to solve the problem]

溶剤可溶であり且つ耐候性のある塗料用に適した水媒系
塩素化の方法としては出頼人が別途山願したように、 1、比表面積が300〜20.000cnf/ gに微
粉化させたポリオレフィン粉末を用いて反応を行う、2
、塩素化が塩素化ポリオレフィンの熱軟化温度の最低値
に対応する塩素化度に到達するまでの間は反応温度を該
熱軟化温度の最低値以下に調節する、 3、塩素化度を50重険%以上にする、4、塩素化終了
までに塩素化中のポリオレフィン粒子の離解、粉砕処理
を併行する、 ことにより実現される。
As separately requested by the sender, the method of aqueous chlorination suitable for solvent-soluble and weather-resistant paints is as follows: 1. Micronization to a specific surface area of 300 to 20,000 cnf/g. Conducting a reaction using the prepared polyolefin powder, 2
, Until the chlorination reaches the degree of chlorination corresponding to the lowest value of the heat softening temperature of the chlorinated polyolefin, the reaction temperature is adjusted to below the lowest value of the heat softening temperature. 3. The degree of chlorination is adjusted to 50%. 4. Before the end of chlorination, the polyolefin particles being chlorinated are simultaneously disintegrated and pulverized.

これらの手段により不均一塩素化物は溶剤可溶となると
同時に可塑剤量の少い耐候性のある塗料組成物を提供す
る。
By these means, the heterogeneously chlorinated product becomes solvent soluble and at the same time provides a weather resistant coating composition with a small amount of plasticizer.

即ち適当な粉砕による表面積の増大、反応初期に於ける
塩素化温度の調節により、不均一塩素化は、溶剤可溶性
と耐候性をもたらす巾広い塩素化度分布との双方を両立
させる適度なものとなる。
In other words, by increasing the surface area through appropriate pulverization and adjusting the chlorination temperature at the initial stage of the reaction, heterogeneous chlorination can be achieved at a moderate level that achieves both solvent solubility and a wide chlorination degree distribution that provides weather resistance. Become.

更に本発明の構成について詳述すれば以下の通りである
′。
Further details of the structure of the present invention are as follows.

■、粉砕度、比表面積として300〜20.1100C
iI/gが妥当であり、20.000car/ g以上
になると作業性が低下する、 2、ポリオレフィンは塩素化により熱軟化温度が低下し
、ある平均塩素化度に於いて最低となり更に高塩素化度
では上昇する、 熱軟化温度は図19図2のようにDSC吸熱曲線の反曲
点により示される。
■, grinding degree, specific surface area: 300-20.1100C
iI/g is appropriate, and if it exceeds 20.000 car/g, workability will decrease. 2. The thermal softening temperature of polyolefins decreases due to chlorination, reaching the lowest level at a certain average degree of chlorination, and further increases in chlorination. The thermal softening temperature is indicated by the inflection point of the DSC endothermic curve as shown in Figure 19 and Figure 2.

3、ポリオレフィンとしてはポリエチレン又はポリプロ
ピレンを使用する、 4、塩素化中の離解粉砕は1回以上ノ<・ソチで又は連
続して湿式1機械式、粉砕機例えばボールミル、ホモジ
ナイザー、渦巻ポンプ等の衝撃やせん断のかかる装置に
より行う、 5、塩素化度は50重隈%以上でないと溶剤可溶性は達
成しにくい、 〔実施例〕 以下実施例により本発明を説明するが、本発明はこれに
限定されるものではない。
3. Polyethylene or polypropylene is used as the polyolefin. 4. Disintegration and pulverization during chlorination is carried out one or more times in Sochi or continuously using a wet method 1. Impact using a mechanical crusher such as a ball mill, homogenizer, or centrifugal pump. 5. It is difficult to achieve solvent solubility unless the degree of chlorination is 50% or higher. [Examples] The present invention will be explained below with reference to Examples, but the present invention is not limited thereto. It's not something you can do.

実施例1 撹拌機、UV照射装置、還流冷却器付は101セパラブ
ルフラスコに樹脂(Ml値20のPE)500 g、水
81.少量の界面活t’l剤を使用してスラリーとして
、仕込み50℃に加温し、UVを照射しながら塩素ガス
を、500g/I(の速度で導入した。
Example 1 500 g of resin (PE with an Ml value of 20) and 81 g of water were placed in a 101 separable flask equipped with a stirrer, UV irradiation device, and reflux condenser. A slurry was prepared using a small amount of a surfactant T'l agent, heated to 50° C., and chlorine gas was introduced at a rate of 500 g/I (while irradiating with UV light).

図2の熱軟化曲線の最低温度を示す点に対応する推定塩
素化度35%まで反応温度を50℃に保持し、その後、
約20℃/Hの昇温速度で90℃迄昇温しその温度を保
持して、65%以上の塩素化物を得た。
The reaction temperature was maintained at 50 °C until the estimated degree of chlorination was 35%, which corresponds to the lowest temperature point on the thermal softening curve in Figure 2;
The temperature was raised to 90°C at a heating rate of about 20°C/H, and the temperature was maintained to obtain a chlorinated product of 65% or more.

実施例2 実施例1の装置、方法により平均分子@4000のPP
を使用した。図2により塩素化反応開始温度を70℃と
した。
Example 2 PP with an average molecular weight of 4000 was produced using the apparatus and method of Example 1.
It was used. According to FIG. 2, the chlorination reaction initiation temperature was set at 70°C.

実施例3 撹拌機、還流冷却器、uvn<を射装若付+01セパラ
ブルフラスコに比表面積(島?1を製作所、流動式比表
面積測定装置により測定) 6600cnf/ g(7
)PE (Ml(i+’(1,5)  500g+、−
少隈ノ界面活+1剤と水8gを入れ、加温、攪拌、UV
を照射しながら塩素を導入し、反応を中断することなく
反応液を渦巻ポンプで強制循環を行い反応中に生成する
凝集物の離解を行った。得られた塩素化度は66.8%
であった。
Example 3 A stirrer, a reflux condenser, and a UVN were placed in a separable flask with a specific surface area of 6,600 cnf/g (7).
)PE (Ml(i+'(1,5) 500g+,-
Add Shokuma surfactant +1 agent and 8g of water, heat, stir, and UV.
Chlorine was introduced while irradiating the reactor, and the reaction solution was forcedly circulated using a centrifugal pump without interrupting the reaction to disintegrate the aggregates generated during the reaction. The degree of chlorination obtained was 66.8%
Met.

実施例4 撹拌機、還流冷却器、UVII((射装置付10/セパ
ラブルフラスコに分子f13000で比表面積200c
rl/gのPPを溶剤に溶解して非溶剤により析出させ
たものをボールミルで粉砕し比表面積5、900 cn
f/ gのPPとした。このPP500gに少量の界面
活fl[剤と水81を入れ、加温、攪拌下にUVを照射
しながら塩素を導入した。塩素化度約40%で反応液を
取出し水洗後、ボールミルで粉砕し、再度フラスコに仕
込み、塩素化度67.0%に達するまで塩素化反応を行
った。
Example 4 Stirrer, reflux condenser, UVII (10/separable flask with injection device, specific surface area 200c
rl/g of PP was dissolved in a solvent and precipitated with a non-solvent, then ground in a ball mill to obtain a specific surface area of 5,900 cn.
f/g PP. A small amount of surfactant fl[agent and 81 g of water were added to 500 g of this PP, and chlorine was introduced while heating and stirring and UV irradiation. At a degree of chlorination of about 40%, the reaction solution was taken out, washed with water, pulverized in a ball mill, charged into a flask again, and chlorinated until the degree of chlorination reached 67.0%.

比較例I Ml20のポリエチレン100gを5v、zの四項素化
炭素に溶解し、常j[下85℃で十分に溶解した後、光
を照射しつつ塩素化を行なった。塩素含rr’167重
喰%に達した時、塩素化反応を停止し、残留塩素を除去
した後、水蒸気蒸留する市によって白色の粉末を取り山
した。
Comparative Example I 100 g of polyethylene of M120 was dissolved in 5 V, Z tetranomial hydrogenated carbon, and after being sufficiently dissolved at 85° C., chlorination was performed while irradiating with light. When the chlorine content reached 167% by weight, the chlorination reaction was stopped, residual chlorine was removed, and a white powder was collected by steam distillation.

比較例2 分子ff14000のポリプロピレンを1の四項素化炭
素に溶解し2 kg / LOiのIF労力下105℃
で十分に溶解した後、光を照射しつつ塩素化を行なった
。塩素含打率65重量%に達した時、塩素化反応を停止
し、残留塩素を除去した後、水蒸気蒸留する事によって
白色の粉末を取り出した。
Comparative Example 2 Polypropylene with a molecular ff of 14,000 was dissolved in 1 of quaternary hydrogenated carbon at 105°C under an IF effort of 2 kg/LOi.
After sufficient dissolution, chlorination was performed while irradiating with light. When the chlorine content reached 65% by weight, the chlorination reaction was stopped, residual chlorine was removed, and white powder was extracted by steam distillation.

実施例1〜4及び比較例1〜2で得られた試料について
、平均分子量、分子量分散度、さらに各試!′1の20
%トルエン溶液をみがき軟鋼板(SPCCll33!4
1  冷間圧延B、  0.8X50X 150m/m
)へ塗工し、l昼夜風乾後、鉛筆硬度。
Regarding the samples obtained in Examples 1 to 4 and Comparative Examples 1 to 2, the average molecular weight, molecular weight dispersity, and each test! '1 of 20
% toluene solution polishing mild steel plate (SPCCll33!4
1 Cold rolling B, 0.8X50X 150m/m
) and after air drying day and night, the pencil hardness.

耐屈曲性、耐衝撃性試験を行なった結果を表−1に示す
。また各試料を用いて白色上塗り用塗料を調製した。塗
料にとって既述の如き耐候性が必須の条件であるが、U
VI!Q射による白色度の変化を追跡し、合せて塗膜の
変化を観察した。
Table 1 shows the results of bending resistance and impact resistance tests. In addition, a white top coat paint was prepared using each sample. Weather resistance as mentioned above is an essential condition for paints, but U
VI! Changes in whiteness due to Q radiation were tracked, and changes in the coating film were also observed.

塗料組成及び試験片の作成波は下記の通りである。The composition of the paint and the waveforms used to prepare the test pieces are as follows.

塗料組成 樹脂             20.0重量部可塑剤
(トヨバラツクA−40)   4.0二酸化チタン(
R−820)     25.0安定剤(エピコート8
2g)     0.5揺変剤(ベントン34)1.5 キシレン           49.0合計    
 100.0 上記組成の塗料をサンドミルで混練して、サンドブラス
ト板上にエポジンクを下塗りし、その上にはけで塗装し
た試験片を作成した。その後テスト板を7日間風乾した
後、回転ドラムに取付けた試験片にHWの水銀灯を30
cmの距離から賄射し所定の時間毎に白色度と塗膜表面
の変化を追跡した。
Paint composition resin 20.0 parts by weight Plasticizer (Toyobarakku A-40) 4.0 Titanium dioxide (
R-820) 25.0 Stabilizer (Epicote 8
2g) 0.5 thixotropic agent (bentone 34) 1.5 xylene 49.0 total
100.0 A test piece was prepared by kneading the paint having the above composition in a sand mill, undercoating Epozinc on a sandblast board, and painting the undercoat with a brush. After the test plate was air-dried for 7 days, a HW mercury lamp was applied to the test piece attached to the rotating drum for 30 minutes.
It was irradiated from a distance of 1.5 cm and changes in whiteness and coating surface were tracked at predetermined intervals.

塗膜の性能を表11表2に示す。The performance of the coating film is shown in Table 11 and Table 2.

表−1 注1)平均分子ff1=ポリスチレンを標準としたG、
  P、  C,による測定値。
Table-1 Note 1) Average molecule ff1 = G with polystyrene as standard,
Measured values by P, C,.

注2)分散度・Mw/Mn  My・・・重量平均分子
a   Mn・・・数平均分子隈注3)耐屈曲性:17
2φインチマンドレルで180’折り曲げ塗膜の状態を
調べた。
Note 2) Dispersity/Mw/Mn My...Weight average molecule a Mn...Number average molecular area Note 3) Flexibility: 17
The condition of the coating film was examined by bending it 180' using a 2φ inch mandrel.

注4)耐衝撃性:デュポン式衝撃試験機で撃芯1/2φ
インチ、荷重500gを使用し、表打ちの場合50cm
より落下、裏rrちの場合25cmより落下させた。
Note 4) Impact resistance: Strike core 1/2φ using DuPont impact tester
inch, load 500g, 50cm for surface striking
In the case of back RR, it was dropped from 25 cm.

表 2 UV照射時間と塗膜劣化の関係(耐候性)オレフィンを
含有させることにより耐候性の優れた塗料が得られ本発
明を完成した。
Table 2 Relationship between UV irradiation time and coating film deterioration (weather resistance) By incorporating an olefin, a coating material with excellent weather resistance was obtained and the present invention was completed.

【図面の簡単な説明】[Brief explanation of drawings]

第1図は本発明の実施例におけるDSC吸熱曲線で吸熱
量と温度との関係図であり、第2図は同上の温度と塩素
化度の関係曲線図である。 表−1かられかる如く、本発明組成物を用いれば表面の
優れたコーチング組成物が得られる。 又表−2から明らかな如〈従来法で得られた比較試料は
本試験の如く可塑剤の添加量を戚らした場合P!I!膜
の劣化が著しく耐候性に劣るが、本発明組成物を介する
塗料は可塑剤をほとんど必要とせず耐候11に優れた塗
膜を形成する11が判る。 〔発明の効果〕 以上の実施例に示したように溶剤可溶であり■つ適度の
不均一性をイiする水媒系塩素化ポリ第1図 手続補正書 (自 発) 第2図 1、事件の表示 平成1年 特許願 第344659号 2、発明の名称 塩素化ポリオレフィン系塗料用組成物 3゜ 補正をする者 事件との関係 特許出願人 住 所   東京都千代田区丸の内−丁目4番5号名 
称   (234)山陽国策パルプ株式会社4、代理人 住所 東京都千代田区神01北乗物町16番地5、補正の対象 塩素化度 (W%) 明細書第7頁17行目に「溶剤に溶解して非溶剤により
」とあるを「溶剤に溶解して貧溶剤によりJと訂正=、
1、諒トゲ゛、
FIG. 1 is a DSC endothermic curve in an example of the present invention, which is a diagram showing the relationship between the amount of heat absorbed and the temperature, and FIG. 2 is a diagram showing the relationship between the temperature and the degree of chlorination. As shown in Table 1, by using the composition of the present invention, a coating composition with an excellent surface can be obtained. Also, as is clear from Table 2, the comparison sample obtained by the conventional method had a P! I! Although the film was significantly deteriorated and its weather resistance was poor, the paint using the composition of the present invention hardly required a plasticizer and formed a film with excellent weather resistance. [Effects of the Invention] As shown in the above examples, water-based chlorinated polyurethane that is solvent soluble and exhibits moderate heterogeneity (ii) Figure 1 procedural amendment (voluntary) Figure 2 1, Description of the case 1999 Patent Application No. 344659 2 Title of the invention Chlorinated polyolefin coating composition 3゜Relationship with the case Patent applicant Address 4-5 Marunouchi-chome, Chiyoda-ku, Tokyo given name
Name (234) Sanyo Kokusaku Pulp Co., Ltd. 4, Agent Address: 16-5 Kitajomono-cho, Kami 01, Chiyoda-ku, Tokyo, Subject to Correction Chlorination Degree (W%) Page 7, line 17 of the specification states, “Dissolved in solvent” and corrected it to "J by dissolving it in a solvent and using a poor solvent".
1. Sorry,

Claims (5)

【特許請求の範囲】[Claims] (1)比表面積が300cm^2/g〜20,000c
m^2/gに微粉化されたポリオレフィン粉末を水性媒
体中に懸濁し塩素化して得られる溶剤可溶な塩素化ポリ
オレフィンを含有する耐候性の良好な塗料用組成物。
(1) Specific surface area is 300cm^2/g ~ 20,000c
A coating composition with good weather resistance containing a solvent-soluble chlorinated polyolefin obtained by suspending a polyolefin powder finely divided into m^2/g in an aqueous medium and chlorinating it.
(2)塩素化終了までに1回以上繰返して又は連続して
塩素化反応中のポリオレフィン粒子の離解,粉砕処理を
併行する請求項1記載の溶剤可溶な塩素化ポリフィンを
含有する耐候性の良好な塗料用組成物。
(2) The weather-resistant material containing the solvent-soluble chlorinated polyfin according to claim 1, wherein the polyolefin particles undergoing the chlorination reaction are subjected to disintegration and pulverization treatment repeatedly or continuously one or more times until the chlorination is completed. Good paint composition.
(3)塩素化が塩素化ポリオレフィンの熱軟化温度の最
低値に対応する塩素化度に到達するまでの間は、反応温
度を該熱軟化温度の最低値以下とする請求項1または2
記載の溶剤可溶な塩素化ポリオレフィンを含有する耐候
性の良好な塗料用組成物。
(3) Until the chlorination reaches a degree of chlorination corresponding to the lowest thermal softening temperature of the chlorinated polyolefin, the reaction temperature is kept at or below the lowest thermal softening temperature of the chlorinated polyolefin.
A coating composition with good weather resistance containing the solvent-soluble chlorinated polyolefin described above.
(4)塩素化度が50重量%以上である請求項1〜3ま
でのいずれか1項記載の溶剤可溶な塩素化ポリオレフィ
ンを含有する耐候性の良好な塗料用組成物。
(4) A coating composition with good weather resistance, containing the solvent-soluble chlorinated polyolefin according to any one of claims 1 to 3, which has a degree of chlorination of 50% by weight or more.
(5)ポリオレフィンがポリエチレン又はポリプロピレ
ンである請求項1〜4までのいずれか1項記載の溶剤可
溶な塩素化ポリフィンを含有する耐候性の良好な塗料用
組成物。
(5) A coating composition with good weather resistance containing the solvent-soluble chlorinated polyfin according to any one of claims 1 to 4, wherein the polyolefin is polyethylene or polypropylene.
JP1344659A 1989-12-27 1989-12-27 Chlorinated polyolefin coating composition Expired - Fee Related JP2567287B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP1344659A JP2567287B2 (en) 1989-12-27 1989-12-27 Chlorinated polyolefin coating composition

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP1344659A JP2567287B2 (en) 1989-12-27 1989-12-27 Chlorinated polyolefin coating composition

Publications (2)

Publication Number Publication Date
JPH03199274A true JPH03199274A (en) 1991-08-30
JP2567287B2 JP2567287B2 (en) 1996-12-25

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ID=18370986

Family Applications (1)

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Country Status (1)

Country Link
JP (1) JP2567287B2 (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5385979A (en) * 1994-01-11 1995-01-31 Lord Corporation Primer and adhesive compositions based on chlorinated polyolefins having high chlorine contents
US5492963A (en) * 1994-01-11 1996-02-20 Lord Corporation Overcoat and adhesive compositions based on chlorinated polyolefins having high chlorine contents
JP2017075298A (en) * 2015-07-29 2017-04-20 リライアンス、インダストリーズ、リミテッドReliance Industries Limited Process for chlorination of polymer

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5426839A (en) * 1977-08-02 1979-02-28 Osaka Soda Co Ltd Preparation of chlorinated polyethylene solution
JPS54153831A (en) * 1978-05-24 1979-12-04 Osaka Soda Co Ltd Chlorinated polyethylene coating composition

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5426839A (en) * 1977-08-02 1979-02-28 Osaka Soda Co Ltd Preparation of chlorinated polyethylene solution
JPS54153831A (en) * 1978-05-24 1979-12-04 Osaka Soda Co Ltd Chlorinated polyethylene coating composition

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5385979A (en) * 1994-01-11 1995-01-31 Lord Corporation Primer and adhesive compositions based on chlorinated polyolefins having high chlorine contents
US5492963A (en) * 1994-01-11 1996-02-20 Lord Corporation Overcoat and adhesive compositions based on chlorinated polyolefins having high chlorine contents
US5534591A (en) * 1994-01-11 1996-07-09 Lord Corporation Overcoat and adhesive compositions based on chlorinated polyolefins having high chlorine contents
JP2017075298A (en) * 2015-07-29 2017-04-20 リライアンス、インダストリーズ、リミテッドReliance Industries Limited Process for chlorination of polymer

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