JPH03199275A - Coating film-forming composition - Google Patents
Coating film-forming compositionInfo
- Publication number
- JPH03199275A JPH03199275A JP1344660A JP34466089A JPH03199275A JP H03199275 A JPH03199275 A JP H03199275A JP 1344660 A JP1344660 A JP 1344660A JP 34466089 A JP34466089 A JP 34466089A JP H03199275 A JPH03199275 A JP H03199275A
- Authority
- JP
- Japan
- Prior art keywords
- methylpentene
- chlorinated
- chlorination
- resin
- chlorine
- 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
Links
- 239000000203 mixture Substances 0.000 title claims abstract description 8
- 239000011248 coating agent Substances 0.000 title description 2
- 238000000576 coating method Methods 0.000 title description 2
- WSSSPWUEQFSQQG-UHFFFAOYSA-N 4-methyl-1-pentene Chemical compound CC(C)CC=C WSSSPWUEQFSQQG-UHFFFAOYSA-N 0.000 claims abstract description 16
- 229920000642 polymer Polymers 0.000 claims abstract description 7
- 239000012736 aqueous medium Substances 0.000 claims abstract description 5
- ZAMOUSCENKQFHK-UHFFFAOYSA-N Chlorine atom Chemical compound [Cl] ZAMOUSCENKQFHK-UHFFFAOYSA-N 0.000 claims description 17
- 239000000460 chlorine Substances 0.000 claims description 17
- 229910052801 chlorine Inorganic materials 0.000 claims description 17
- 150000001336 alkenes Chemical class 0.000 claims 1
- JRZJOMJEPLMPRA-UHFFFAOYSA-N olefin Natural products CCCCCCCC=C JRZJOMJEPLMPRA-UHFFFAOYSA-N 0.000 claims 1
- 238000005660 chlorination reaction Methods 0.000 abstract description 16
- 239000004711 α-olefin Substances 0.000 abstract description 2
- 239000011347 resin Substances 0.000 description 18
- 229920005989 resin Polymers 0.000 description 18
- YXFVVABEGXRONW-UHFFFAOYSA-N Toluene Chemical compound CC1=CC=CC=C1 YXFVVABEGXRONW-UHFFFAOYSA-N 0.000 description 12
- 239000000976 ink Substances 0.000 description 11
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 6
- 239000000843 powder Substances 0.000 description 6
- 230000000052 comparative effect Effects 0.000 description 4
- 238000000034 method Methods 0.000 description 4
- 239000002245 particle Substances 0.000 description 4
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 4
- 238000006243 chemical reaction Methods 0.000 description 3
- 229920001577 copolymer Polymers 0.000 description 3
- 239000011521 glass Substances 0.000 description 3
- 229910052757 nitrogen Inorganic materials 0.000 description 3
- 239000000725 suspension Substances 0.000 description 3
- AFFLGGQVNFXPEV-UHFFFAOYSA-N 1-decene Chemical compound CCCCCCCCC=C AFFLGGQVNFXPEV-UHFFFAOYSA-N 0.000 description 2
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical group [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 2
- VGGSQFUCUMXWEO-UHFFFAOYSA-N Ethene Chemical compound C=C VGGSQFUCUMXWEO-UHFFFAOYSA-N 0.000 description 2
- 239000005977 Ethylene Substances 0.000 description 2
- ATJFFYVFTNAWJD-UHFFFAOYSA-N Tin Chemical compound [Sn] ATJFFYVFTNAWJD-UHFFFAOYSA-N 0.000 description 2
- 238000004458 analytical method Methods 0.000 description 2
- 238000005452 bending Methods 0.000 description 2
- 229910052799 carbon Inorganic materials 0.000 description 2
- 238000004090 dissolution Methods 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 229920001519 homopolymer Polymers 0.000 description 2
- 230000001678 irradiating effect Effects 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 239000003973 paint Substances 0.000 description 2
- 230000000704 physical effect Effects 0.000 description 2
- 238000007639 printing Methods 0.000 description 2
- 239000000376 reactant Substances 0.000 description 2
- 239000002904 solvent Substances 0.000 description 2
- 238000001256 steam distillation Methods 0.000 description 2
- 238000003756 stirring Methods 0.000 description 2
- 238000003860 storage Methods 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- 239000002966 varnish Substances 0.000 description 2
- 101100313164 Caenorhabditis elegans sea-1 gene Proteins 0.000 description 1
- 229910001209 Low-carbon steel Inorganic materials 0.000 description 1
- 239000004793 Polystyrene Substances 0.000 description 1
- NIXOWILDQLNWCW-UHFFFAOYSA-N acrylic acid group Chemical group C(C=C)(=O)O NIXOWILDQLNWCW-UHFFFAOYSA-N 0.000 description 1
- 238000007605 air drying Methods 0.000 description 1
- 239000011230 binding agent Substances 0.000 description 1
- 238000007664 blowing Methods 0.000 description 1
- 150000001805 chlorine compounds Chemical class 0.000 description 1
- 238000002845 discoloration Methods 0.000 description 1
- 238000001035 drying Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 230000002349 favourable effect Effects 0.000 description 1
- 238000007646 gravure printing Methods 0.000 description 1
- 238000000227 grinding Methods 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 230000001771 impaired effect Effects 0.000 description 1
- JEIPFZHSYJVQDO-UHFFFAOYSA-N iron(III) oxide Inorganic materials O=[Fe]O[Fe]=O JEIPFZHSYJVQDO-UHFFFAOYSA-N 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 238000002844 melting Methods 0.000 description 1
- 230000008018 melting Effects 0.000 description 1
- 239000000178 monomer Substances 0.000 description 1
- 239000000049 pigment Substances 0.000 description 1
- 239000004014 plasticizer Substances 0.000 description 1
- 229920000098 polyolefin Polymers 0.000 description 1
- 229920002223 polystyrene Polymers 0.000 description 1
- 238000010298 pulverizing process Methods 0.000 description 1
- 238000010926 purge Methods 0.000 description 1
- 239000004576 sand Substances 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 238000005979 thermal decomposition reaction Methods 0.000 description 1
Landscapes
- Paints Or Removers (AREA)
- Inks, Pencil-Leads, Or Crayons (AREA)
- Addition Polymer Or Copolymer, Post-Treatments, Or Chemical Modifications (AREA)
Abstract
Description
【発明の詳細な説明】
〔産業上の利用分野〕
本発明は、インキ、塗料、OPニス等の被膜形成組成物
として可撓性と耐熱性を有する塩素化4−メチルペンテ
ン−1系樹脂に関するものである。Detailed Description of the Invention [Field of Industrial Application] The present invention relates to a chlorinated 4-methylpentene-1 resin having flexibility and heat resistance as a film-forming composition for inks, paints, OP varnishes, etc. It is something.
塩素化4−メチルペンテン−1系樹脂は、ポリ・4−メ
チルペンテン−1および/またはα−オレフィン・4−
メチルペンテン−lポリマーを塩素化して製造される物
質である。これ等塩素化4−メチルペンテン−1樹脂は
、耐候性、耐水性、耐薬品性等に優れているばかりでな
く、従来の塩素化ポリオレフィン類に比べ耐熱性が非常
に優れた樹脂で、高速印刷インキ用バインダーあるいは
耐熱用OPニス等として巾広く用いられている。The chlorinated 4-methylpentene-1 resin is poly-4-methylpentene-1 and/or α-olefin 4-
It is a substance produced by chlorinating methylpentene-1 polymer. These chlorinated 4-methylpentene-1 resins not only have excellent weather resistance, water resistance, and chemical resistance, but also have extremely superior heat resistance compared to conventional chlorinated polyolefins. It is widely used as a binder for printing inks or as a heat-resistant OP varnish.
しかし、従来の製造法である耐塩素溶媒中で塩素化され
た塩素化4−メチルペンテン−1系樹脂は、均一塩素化
合物ゆえに、被膜を形成した際、硬くてもろいので耐屈
曲性に劣る点が指摘されている。However, since the chlorinated 4-methylpentene-1 resin, which is chlorinated in a chlorine-resistant solvent using the conventional manufacturing method, is a homogeneous chlorine compound, when it forms a film, it is hard and brittle, resulting in poor bending resistance. has been pointed out.
この耐屈曲性を改良するために従来から種々の改良策が
提案されている。例えば特開昭58−45266は塩素
化ポリ・4−メチルペンテンー1にアクリル系モノマー
を重合し可撓性を付与する事を開示し、ている。あるい
は実用時に可塑剤等の柔らかい樹脂を併用する事で物理
的に可撓性を与えている実用例もある。しかしこれ等可
撓性を付与する方法は、塩素化4−メチルペンテン−1
系樹脂の特徴である耐熱性を実質的に低下させる事とな
り、満足される改良策には至っていない。Various improvement measures have been proposed to improve this bending resistance. For example, JP-A-58-45266 discloses that chlorinated poly-4-methylpentene-1 is polymerized with an acrylic monomer to impart flexibility. Alternatively, there are practical examples where soft resins such as plasticizers are used in combination to provide physical flexibility. However, these methods of imparting flexibility are based on chlorinated 4-methylpentene-1
This results in a substantial reduction in the heat resistance, which is a characteristic of the resin, and a satisfactory improvement measure has not been achieved.
本発明は上記実情に鑑み、耐熱性を低下させる事なく、
可撓性を付与した塩素化4−メチルペンテン−1系樹脂
を提供しようとするものである。In view of the above circumstances, the present invention has been developed to
The object of the present invention is to provide a chlorinated 4-methylpentene-1 resin that has flexibility.
本発明者等は、種々検討した結果、ポリ・4−メチルペ
ンテン−1および/またはα−オレフィン−4−メチル
ペンテン−lポリマーを塩素化する段階において、水性
媒体中で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やすい事に着目し、本発明に至った
。As a result of various studies, the inventors of the present invention have found that, in the step of chlorinating poly-4-methylpentene-1 and/or α-olefin-4-methylpentene-1 polymers, if the process is carried out in an aqueous medium, powder resin The present invention was developed based on the fact that the surface is easily chlorinated and a heterogeneous reactant is easily formed.
すなわち、従来の耐塩素溶媒中で塩素化された塩素化4
−メチルペンテン−1ポリマーは、均一反応ゆえに分子
量中が狭く、従って硬い被膜が形成される樹脂となって
いたが水性媒体中で塩素化を行なえば不均一反応体が形
成され、塩素化度に巾を持たせる事ができ、合せて分子
量中が広くなる事より可撓性のある塩素化樹脂が得られ
る訳である。その際懸濁液を循環ポンプで循環し、ある
いは循環液の途中にボールミル等を配置し、機械的に粉
体樹脂表面を剥離更新しつつ塩素化すれば、その度合い
によって耐熱性を損う事なく任意に可撓性を与えた塩素
化4−メチルペンテン−1系樹脂が得られる訳である。That is, chlorinated 4 chlorinated in a conventional chlorine-resistant solvent
-Methylpentene-1 polymer has a narrow molecular weight due to its homogeneous reaction, and therefore it has become a resin that forms a hard film, but when chlorinated in an aqueous medium, a heterogeneous reactant is formed, and the degree of chlorination increases. This means that a flexible chlorinated resin can be obtained because it can have a wide width and also has a wide molecular weight. At that time, if the suspension is circulated with a circulation pump or a ball mill or the like is placed in the middle of the circulating liquid and the powder resin surface is mechanically peeled off and renewed while being chlorinated, heat resistance may be impaired depending on the degree of chlorination. This means that a chlorinated 4-methylpentene-1-based resin can be obtained which has arbitrary flexibility.
本発明に採用される樹脂はその重合体の粒子内部に多く
の空隙を持つか、粒子粒径が小さければ必要以上の不均
一塩素化が免れ、本発明の効果を出す上で好ましい条件
となる。If the resin used in the present invention has many voids inside the polymer particles or has a small particle size, unnecessary uneven chlorination can be avoided, which is a favorable condition for producing the effects of the present invention. .
本発明で塩素含有量50重量%以上としたのはそれ以下
では本発明の特徴である耐熱性が得られないからである
。The reason why the chlorine content is set to 50% by weight or more in the present invention is that if it is less than 50% by weight, the heat resistance, which is a feature of the present invention, cannot be obtained.
以下、実施例及び比較例を挙げ、本発明の詳細な説明す
るが、本発明はこれ等の実施例に限定されるものではな
い。EXAMPLES Hereinafter, the present invention will be described in detail with reference to Examples and Comparative Examples, but the present invention is not limited to these Examples.
実施例1
ガラス製反応器に500部の純水と、Mlが8g/l0
nin (ASTM D123B−65T)の4−メ
チルペンテン−1ホモポリマ一100部を投入し、容器
内を攪拌しつつ窒素パージを行なった後、常圧で光を照
射しつつ、90℃で塩素を吹き込み塩素化を行なった。Example 1 500 parts of pure water and 8 g/l0 of Ml were placed in a glass reactor.
100 parts of 4-methylpentene-1 homopolymer (ASTM D123B-65T) was added, the inside of the container was purged with nitrogen while stirring, and then chlorine was blown in at 90°C while irradiated with light at normal pressure. Chlorination was performed.
その時樹脂粒子の団塊化を防ぐ目的で懸濁液を循環ポン
プで循環し、かつ循環系の途中にボールミルを設置して
機械的に粉体樹脂表面を剥離更新しつつ塩素化を行なう
方法をとり、反応中連続的に粉砕処理を行なった。At this time, in order to prevent the resin particles from forming agglomerates, the suspension is circulated by a circulation pump, and a ball mill is installed in the middle of the circulation system to mechanically peel and renew the powder resin surface while chlorinating it. The pulverization treatment was carried out continuously during the reaction.
平均塩素含有率が54重量%に達した時塩素化反応を停
止し、残存塩素を除去した後、乾燥して試料を得た。When the average chlorine content reached 54% by weight, the chlorination reaction was stopped, residual chlorine was removed, and the sample was dried to obtain a sample.
実施例2
ガラス製反応器に500部の純水と、デセン−1を15
no1%含むMlが36g/IOiin(ASTM
D123B−657)の4−メチルペンチ、シー1コポ
リマー100部を投入し、容器内を攪拌しつつ窒素ノク
ージを行なった後、常圧で光を照射しつつ、90℃で塩
素を吹き込み塩素化を行なった。その時樹脂粒子の団塊
化を防ぐ目的で懸濁液を循環ポンプで循環し、かつ循環
系の途中にボールミルを設置して機械的に粉体樹脂表面
を剥離更新しつつ塩素化を行なう方法をとり、反応中2
時間サイクルで1時間の粉砕処理を行なった。平均塩素
含有率が62重量%に達した時塩素化反応を停止し、残
存塩素を除去した後、乾燥して試料を得た。Example 2 500 parts of pure water and 15 parts of decene-1 were placed in a glass reactor.
Ml containing no1% is 36g/IOiin (ASTM
D123B-657) 4-methyl pliers and 100 parts of Sea 1 copolymer were added, the inside of the container was stirred and flushed with nitrogen, and chlorine was blown in at 90°C while irradiated with light at normal pressure to perform chlorination. Ta. At this time, in order to prevent the resin particles from forming agglomerates, the suspension is circulated by a circulation pump, and a ball mill is installed in the middle of the circulation system to mechanically peel and renew the powder resin surface while chlorinating it. , in reaction 2
The grinding process was performed in a time cycle of 1 hour. When the average chlorine content reached 62% by weight, the chlorination reaction was stopped, residual chlorine was removed, and the sample was dried to obtain a sample.
実施例3
ガラス製反応器に500部の純水と、エチレン10no
1%含むMlが70g/IO+nin(ASTM 0
1238−657)のエチレン・4−メチルペンテン−
1コポリマ一100部を投入し、容器内を攪拌しつつ窒
素パージを行なった後、常圧で光を照射しつつ、90℃
で塩素を吹き込み塩素化を行なった。Example 3 500 parts of pure water and 10 no. of ethylene were placed in a glass reactor.
Ml containing 1% is 70g/IO+nin (ASTM 0
1238-657) ethylene/4-methylpentene-
After adding 100 parts of 1 copolymer and purging with nitrogen while stirring the inside of the container, the container was heated to 90°C while being irradiated with light at normal pressure.
Chlorination was carried out by blowing chlorine.
平均塩素含有率が68重量%に達した時塩素化反応を停
止し、残存塩素を除去した後、乾燥して試料を得た。When the average chlorine content reached 68% by weight, the chlorination reaction was stopped, residual chlorine was removed, and the sample was dried to obtain a sample.
比較例1
Mlが54g/IOiin(ASTM D123B−
65T)の4−メチルペンテン−1ホモポリマ一100
gをとリ5¥ルの四項素化炭素に溶解し、常圧下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
。塩素含有率が60重量%に達した時塩素化反応を停止
し、残存塩素を除去した後、水蒸気蒸留する事によって
白色の粉末を取出した。Comparative Example 1 Ml is 54g/IOiin (ASTM D123B-
65T) 4-methylpentene-1 homopolymer 100
Dissolve g in 5 liters of quaternary hydrogenated carbon and heat at 85°C under normal pressure.
After sufficient dissolution, chlorination was performed while irradiating with light. When the chlorine content reached 60% by weight, the chlorination reaction was stopped, residual chlorine was removed, and white powder was obtained by steam distillation.
比較例2
デセン−1を15n+o1%含むMlが36g/lOn
+jn (ASTM D+238−657)の4−メ
チルペンテン−!コポリマー100gをとり52にの四
項素化炭素に溶解し、2 kg / adの圧力下11
0℃で十分に溶解した後、光を照射しつつ塩素化を行な
った。塩素含有率が65重量%に達した時塩素化反応を
停止し、残存塩素を除去した後、水蒸気蒸留する事によ
って白色の粉末を取出した。Comparative Example 2 Ml containing 15n+o1% of decene-1 was 36g/lOn
+jn (ASTM D+238-657) 4-methylpentene-! Take 100 g of copolymer and dissolve it in 52% tetranomialized carbon under a pressure of 2 kg/ad.
After sufficiently dissolving at 0° C., 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 obtained by steam distillation.
実施例1〜3及び比較例1〜2で得られた試料について
の溶液粘度、平均分子量1分子量分散度、軟化温度及び
耐熱分解性の各分析、さらに各試料の20%トルエン溶
液をみがき軟鋼板(SPCCll53141 冷間圧
延B、 0.8x50X 150m/m)へ塗工、1
昼夜風乾後、耐層+To性。Analysis of solution viscosity, average molecular weight/molecular weight dispersity, softening temperature, and thermal decomposition resistance for the samples obtained in Examples 1 to 3 and Comparative Examples 1 to 2, and a 20% toluene solution of each sample was also applied to polished mild steel plates. Coating to (SPCCll53141 cold rolled B, 0.8x50X 150m/m), 1
After air drying day and night, layer resistance + To resistance.
耐衝撃性試験を行なった結果を表−1に示す。Table 1 shows the results of the impact resistance test.
また、各試料を用いてグラビア印刷インキを調製した。In addition, gravure printing ink was prepared using each sample.
即ち、樹脂18gとトルエン72gで20%トルエン溶
液を調製しこれに顔料(カーミノ6BN:東洋インキ製
造K K品)10gを加えサンドミルにより2時間混練
した後、インキの固形分を一定にしてコート紙状に塗工
し5〜7μのインキ膜を形成した。これを室温で十分に
乾燥後、発色性、耐熱性、インキの保存安定性の各試験
を行なった結果を表−2に示す。That is, a 20% toluene solution was prepared with 18 g of resin and 72 g of toluene, 10 g of pigment (Carmino 6BN: Toyo Ink Manufacturing K K product) was added thereto, and the mixture was kneaded in a sand mill for 2 hours.The solid content of the ink was kept constant and coated paper was prepared. The ink film was coated to form an ink film of 5 to 7 microns. After sufficiently drying this at room temperature, various tests were conducted on color development, heat resistance, and ink storage stability. The results are shown in Table 2.
表−■ 各種分析結果
注1)溶解粘度 40重微量トルエン溶演の25℃にお
けるセンチボイズを示す。Table - ■ Various analysis results Note 1) Dissolution viscosity Shows the centivoise at 25°C of 40% heavy toluene solution.
注2)平均分子量:ポリスチレンを標準としたG、
P、 C,による測定値。Note 2) Average molecular weight: G with polystyrene as standard,
Measured values by P, C,.
江3)分散度・Mw/Mn Mt−mF&平均分子量
Mn・・・数平均分子置注4)軟化温度:融点測定
装植により測定。3) Dispersity/Mw/Mn Mt-mF & average molecular weight Mn...Number average molecular weight Note 4) Softening temperature: Measured by melting point measuring device.
注5)熱変色性:180℃、 30分後の加熱変色。Note 5) Thermochromic property: Discoloration after heating at 180°C for 30 minutes.
注6)耐屈曲性:172φインチマンドレルで180°
折り曲げ塗膜の状態を調べた。Note 6) Flexibility: 180° with 172φ inch mandrel
The condition of the bent paint film was examined.
注7)耐衝撃性:デュポン式衝撃試験機で、撃芯1/2
φインチ荷重500gを使用し、表打ちの場合50cI
11より落下、裏打ちの場合25cmより落下させた。Note 7) Impact resistance: DuPont type impact tester, striking core 1/2
Using a φ inch load of 500g, 50cI for surface striking
11, and in the case of lining, it was dropped from 25 cm.
表−2印刷インキの諸物性
〔発明の効果〕
表−1及び表−2から本発明組成物は自己可撓性を持ち
、その他の物性は従来の均一塩素化法で得られた物質と
遜色のない性状を有するものである事が判る。Table 2 Physical properties of printing ink [Effects of the invention] From Tables 1 and 2, the composition of the present invention has self-flexibility, and other physical properties are inferior to those obtained by the conventional uniform chlorination method. It can be seen that it has properties that do not have
注1)発色性:色濃度で判定 ○・・・発色性良好性2
)耐熱性:インキ而にコート原紙を置き各温度に設定し
たヒートシールバーを当てプレスした後30分以上放冷
しこれを剥がしたときの紙むけの状態でfす定した。Note 1) Color development: Determined by color density ○...Good color development 2
) Heat resistance: A coated base paper was placed over the ink, a heat seal bar set at each temperature was applied and pressed, and the coated base paper was left to cool for 30 minutes or more, and then the paper was peeled off and fixed.
◎・・・紙むけなし ○・・・紙むけ5%以下
△・・・紙むけ30%以下
注3)保存安定性:インキをブリキ缶に保存し50℃に
おけるブリキ缶のサビ又はインキのゲル化と一1O℃に
おける流動状態の変(t、。◎...No paper peeling ○...Paper peeling 5% or less△...Paper peeling 30% or lessNote 3) Storage stability: When ink is stored in a tin can, rust on the tin can or ink gel at 50℃ Changes in the flow state at -10°C (t,.
○・・・良好○...Good
Claims (2)
−オレフィン・4−メチルペンテン−1ポリマーを水性
媒体中に懸濁させ、塩素含有率50重量%以上に塩素化
して得られる可撓性を有する耐熱性被膜形成組成物。(1) Poly-4-methylpentene-1 and/or α
- A flexible heat-resistant film-forming composition obtained by suspending an olefin/4-methylpentene-1 polymer in an aqueous medium and chlorinating it to a chlorine content of 50% by weight or more.
載の組成物。(2) The composition according to claim 1, which is chlorinated while being pulverized.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP1344660A JPH0668087B2 (en) | 1989-12-27 | 1989-12-27 | Ink composition |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP1344660A JPH0668087B2 (en) | 1989-12-27 | 1989-12-27 | Ink composition |
Related Child Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP3651694A Division JP2665879B2 (en) | 1994-02-09 | 1994-02-09 | Composition for OP varnish |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH03199275A true JPH03199275A (en) | 1991-08-30 |
JPH0668087B2 JPH0668087B2 (en) | 1994-08-31 |
Family
ID=18370995
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP1344660A Expired - Fee Related JPH0668087B2 (en) | 1989-12-27 | 1989-12-27 | Ink composition |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH0668087B2 (en) |
Citations (2)
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 |
-
1989
- 1989-12-27 JP JP1344660A patent/JPH0668087B2/en not_active Expired - Fee Related
Patent Citations (2)
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 |
Also Published As
Publication number | Publication date |
---|---|
JPH0668087B2 (en) | 1994-08-31 |
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Legal Events
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---|---|---|---|
LAPS | Cancellation because of no payment of annual fees |