JPS603351B2 - Hot-melt water-soluble adhesive - Google Patents
Hot-melt water-soluble adhesiveInfo
- Publication number
- JPS603351B2 JPS603351B2 JP14357077A JP14357077A JPS603351B2 JP S603351 B2 JPS603351 B2 JP S603351B2 JP 14357077 A JP14357077 A JP 14357077A JP 14357077 A JP14357077 A JP 14357077A JP S603351 B2 JPS603351 B2 JP S603351B2
- Authority
- JP
- Japan
- Prior art keywords
- polymerization
- hot
- degree
- mol
- saponification
- 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
Links
- 239000000853 adhesive Substances 0.000 title claims description 14
- 230000001070 adhesive effect Effects 0.000 title claims description 14
- 239000012943 hotmelt Substances 0.000 title claims description 3
- 238000006116 polymerization reaction Methods 0.000 claims description 19
- 229920002451 polyvinyl alcohol Polymers 0.000 claims description 9
- 229920001577 copolymer Polymers 0.000 claims description 8
- HETCEOQFVDFGSY-UHFFFAOYSA-N Isopropenyl acetate Chemical compound CC(=C)OC(C)=O HETCEOQFVDFGSY-UHFFFAOYSA-N 0.000 claims 1
- 239000004372 Polyvinyl alcohol Substances 0.000 claims 1
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 description 27
- 238000007127 saponification reaction Methods 0.000 description 16
- 239000004831 Hot glue Substances 0.000 description 11
- 238000002844 melting Methods 0.000 description 11
- QTBSBXVTEAMEQO-UHFFFAOYSA-M Acetate Chemical compound CC([O-])=O QTBSBXVTEAMEQO-UHFFFAOYSA-M 0.000 description 10
- 230000008018 melting Effects 0.000 description 9
- XTXRWKRVRITETP-UHFFFAOYSA-N Vinyl acetate Chemical compound CC(=O)OC=C XTXRWKRVRITETP-UHFFFAOYSA-N 0.000 description 8
- 238000000034 method Methods 0.000 description 8
- 239000000203 mixture Substances 0.000 description 7
- 239000000155 melt Substances 0.000 description 6
- 239000000123 paper Substances 0.000 description 6
- 239000010893 paper waste Substances 0.000 description 6
- 239000004014 plasticizer Substances 0.000 description 6
- 239000000243 solution Substances 0.000 description 6
- LYCAIKOWRPUZTN-UHFFFAOYSA-N Ethylene glycol Chemical compound OCCO LYCAIKOWRPUZTN-UHFFFAOYSA-N 0.000 description 5
- PEDCQBHIVMGVHV-UHFFFAOYSA-N Glycerine Chemical compound OCC(O)CO PEDCQBHIVMGVHV-UHFFFAOYSA-N 0.000 description 4
- 239000012986 chain transfer agent Substances 0.000 description 4
- 239000003795 chemical substances by application Substances 0.000 description 4
- 239000011087 paperboard Substances 0.000 description 4
- 239000002904 solvent Substances 0.000 description 4
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 4
- RSWGJHLUYNHPMX-UHFFFAOYSA-N Abietic-Saeure Natural products C12CCC(C(C)C)=CC2=CCC2C1(C)CCCC2(C)C(O)=O RSWGJHLUYNHPMX-UHFFFAOYSA-N 0.000 description 3
- KHPCPRHQVVSZAH-HUOMCSJISA-N Rosin Natural products O(C/C=C/c1ccccc1)[C@H]1[C@H](O)[C@@H](O)[C@@H](O)[C@@H](CO)O1 KHPCPRHQVVSZAH-HUOMCSJISA-N 0.000 description 3
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 3
- 239000011248 coating agent Substances 0.000 description 3
- 238000000576 coating method Methods 0.000 description 3
- MTHSVFCYNBDYFN-UHFFFAOYSA-N diethylene glycol Chemical compound OCCOCCO MTHSVFCYNBDYFN-UHFFFAOYSA-N 0.000 description 3
- 238000010528 free radical solution polymerization reaction Methods 0.000 description 3
- -1 polyoxyethylene Polymers 0.000 description 3
- 239000000126 substance Substances 0.000 description 3
- KHPCPRHQVVSZAH-UHFFFAOYSA-N trans-cinnamyl beta-D-glucopyranoside Natural products OC1C(O)C(O)C(CO)OC1OCC=CC1=CC=CC=C1 KHPCPRHQVVSZAH-UHFFFAOYSA-N 0.000 description 3
- OZAIFHULBGXAKX-UHFFFAOYSA-N 2-(2-cyanopropan-2-yldiazenyl)-2-methylpropanenitrile Chemical compound N#CC(C)(C)N=NC(C)(C)C#N OZAIFHULBGXAKX-UHFFFAOYSA-N 0.000 description 2
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 2
- ATUOYWHBWRKTHZ-UHFFFAOYSA-N Propane Chemical compound CCC ATUOYWHBWRKTHZ-UHFFFAOYSA-N 0.000 description 2
- 238000007796 conventional method Methods 0.000 description 2
- 238000000354 decomposition reaction Methods 0.000 description 2
- 238000001035 drying Methods 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 235000011187 glycerol Nutrition 0.000 description 2
- 238000004064 recycling Methods 0.000 description 2
- 229920005989 resin Polymers 0.000 description 2
- 239000011347 resin Substances 0.000 description 2
- YIWGJFPJRAEKMK-UHFFFAOYSA-N 1-(2H-benzotriazol-5-yl)-3-methyl-8-[2-[[3-(trifluoromethoxy)phenyl]methylamino]pyrimidine-5-carbonyl]-1,3,8-triazaspiro[4.5]decane-2,4-dione Chemical group CN1C(=O)N(c2ccc3n[nH]nc3c2)C2(CCN(CC2)C(=O)c2cnc(NCc3cccc(OC(F)(F)F)c3)nc2)C1=O YIWGJFPJRAEKMK-UHFFFAOYSA-N 0.000 description 1
- 241000345998 Calamus manan Species 0.000 description 1
- 244000241257 Cucumis melo Species 0.000 description 1
- 235000015510 Cucumis melo subsp melo Nutrition 0.000 description 1
- FBPFZTCFMRRESA-FSIIMWSLSA-N D-Glucitol Natural products OC[C@H](O)[C@H](O)[C@@H](O)[C@H](O)CO FBPFZTCFMRRESA-FSIIMWSLSA-N 0.000 description 1
- FBPFZTCFMRRESA-KVTDHHQDSA-N D-Mannitol Chemical compound OC[C@@H](O)[C@@H](O)[C@H](O)[C@H](O)CO FBPFZTCFMRRESA-KVTDHHQDSA-N 0.000 description 1
- FBPFZTCFMRRESA-JGWLITMVSA-N D-glucitol Chemical compound OC[C@H](O)[C@@H](O)[C@H](O)[C@H](O)CO FBPFZTCFMRRESA-JGWLITMVSA-N 0.000 description 1
- RWSOTUBLDIXVET-UHFFFAOYSA-N Dihydrogen sulfide Chemical class S RWSOTUBLDIXVET-UHFFFAOYSA-N 0.000 description 1
- 229930195725 Mannitol Natural products 0.000 description 1
- 229920003171 Poly (ethylene oxide) Polymers 0.000 description 1
- 239000004698 Polyethylene Substances 0.000 description 1
- 239000002202 Polyethylene glycol Substances 0.000 description 1
- 239000004743 Polypropylene Substances 0.000 description 1
- FJJCIZWZNKZHII-UHFFFAOYSA-N [4,6-bis(cyanoamino)-1,3,5-triazin-2-yl]cyanamide Chemical compound N#CNC1=NC(NC#N)=NC(NC#N)=N1 FJJCIZWZNKZHII-UHFFFAOYSA-N 0.000 description 1
- 239000007864 aqueous solution Substances 0.000 description 1
- 238000012662 bulk polymerization Methods 0.000 description 1
- 230000000052 comparative effect Effects 0.000 description 1
- 238000002845 discoloration Methods 0.000 description 1
- 125000002485 formyl group Chemical class [H]C(*)=O 0.000 description 1
- 150000008282 halocarbons Chemical class 0.000 description 1
- WGCNASOHLSPBMP-UHFFFAOYSA-N hydroxyacetaldehyde Natural products OCC=O WGCNASOHLSPBMP-UHFFFAOYSA-N 0.000 description 1
- 231100000053 low toxicity Toxicity 0.000 description 1
- 239000000594 mannitol Substances 0.000 description 1
- 235000010355 mannitol Nutrition 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 239000000178 monomer Substances 0.000 description 1
- 239000003208 petroleum Substances 0.000 description 1
- 229920001200 poly(ethylene-vinyl acetate) Polymers 0.000 description 1
- 229920000573 polyethylene Polymers 0.000 description 1
- 229920001223 polyethylene glycol Polymers 0.000 description 1
- 229920000642 polymer Polymers 0.000 description 1
- 229920001155 polypropylene Polymers 0.000 description 1
- 229920002689 polyvinyl acetate Polymers 0.000 description 1
- 239000011118 polyvinyl acetate Substances 0.000 description 1
- 239000001294 propane Substances 0.000 description 1
- FROBCXTULYFHEJ-OAHLLOKOSA-N propaquizafop Chemical compound C1=CC(O[C@H](C)C(=O)OCCON=C(C)C)=CC=C1OC1=CN=C(C=C(Cl)C=C2)C2=N1 FROBCXTULYFHEJ-OAHLLOKOSA-N 0.000 description 1
- 235000012950 rattan cane Nutrition 0.000 description 1
- 235000011121 sodium hydroxide Nutrition 0.000 description 1
- 239000000600 sorbitol Substances 0.000 description 1
- 229920003048 styrene butadiene rubber Polymers 0.000 description 1
- 238000010557 suspension polymerization reaction Methods 0.000 description 1
- ZIBGPFATKBEMQZ-UHFFFAOYSA-N triethylene glycol Chemical compound OCCOCCOCCO ZIBGPFATKBEMQZ-UHFFFAOYSA-N 0.000 description 1
- 238000003466 welding Methods 0.000 description 1
- 239000002023 wood Substances 0.000 description 1
Landscapes
- Compositions Of Macromolecular Compounds (AREA)
- Adhesives Or Adhesive Processes (AREA)
- Addition Polymer Or Copolymer, Post-Treatments, Or Chemical Modifications (AREA)
Description
【発明の詳細な説明】
本発明は、熱溶融型水溶性接着剤、特に酢酸ィソプロベ
ニルと酢酸ビニルとの共重合体の鹸化物である変性ポリ
ピニルアルコール(以下、変性PVAと称す)からなる
熱溶融性で、かつ、水溶性の接着剤に関するものである
。DETAILED DESCRIPTION OF THE INVENTION The present invention provides a hot-melt water-soluble adhesive, particularly a modified polypinyl alcohol (hereinafter referred to as modified PVA) which is a saponified product of a copolymer of isoprobenyl acetate and vinyl acetate. It relates to a heat-melting and water-soluble adhesive.
従釆、熱溶融型接着剤は、無溶剤型で毒性が少なく作業
環境が良い、無乾燥型でセットタイムが短か〈作業能率
が良い等の利点があるので、製本背貼り、段ボールやカ
ートンの製函、ラベル貼り等の接着剤として使用されて
いる。Advantages of hot-melt adhesives include the fact that they are solvent-free, have low toxicity, provide a good work environment, and are non-drying, requiring short set times and high work efficiency. It is used as an adhesive for making boxes, attaching labels, etc.
他方、木材・パルプの不足及び資源の有効利用の観点か
ら故紙の回収・再利用が要望されている。On the other hand, in view of the shortage of wood and pulp and the effective use of resources, there is a demand for the collection and reuse of waste paper.
しかしながら、従釆の熱溶融型接着剤は水に不溶である
為、故紙の再生工程に於いて故紙中に不溶接着剤が小塊
として残存し、抄紙時にロールに付着したり、ピンホー
ルや紙切れを起したり、又、熱安定性の悪い接着剤では
再使用を繰返すうちに分解し紙が着色するので、従釆の
熱溶融型接着剤を使用した故紙の回収がされていない。
故紙の回収を可能な熱溶融型接着剤として、ポリピニル
アルコール(以下、PVAと称す)の様な水溶性の樹脂
を接着剤として使用して故紙再生工程中水に溶解除去し
てもよいが、PVAでは熱溶融し驚く、いかに高温で試
みても溶融粘度が著しく高く、かつ分解を併発して被接
着面への塗工が出釆ない。この欠点を無くする為水溶液
の形で行えば、塗工は可能となるが、乾燥が必要で熱溶
融型接着剤に比べて生産性が著しく低下する。However, since conventional hot-melt adhesives are insoluble in water, non-welding adhesives remain in the waste paper as small lumps during the waste paper recycling process, and may adhere to rolls during paper making or cause pinholes. Waste paper using conventional hot-melt adhesives is not recovered because it causes paper breakage and adhesives with poor thermal stability decompose and become colored after repeated reuse.
A water-soluble resin such as polypynyl alcohol (hereinafter referred to as PVA) may be used as a heat-melting adhesive that can be used to recover waste paper, and may be dissolved and removed in water during the waste paper recycling process. However, PVA melts under heat, and no matter how high the temperature is tried, the melt viscosity is extremely high and decomposition occurs, making it impossible to coat the surface to be adhered. In order to eliminate this drawback, if it is applied in the form of an aqueous solution, coating becomes possible, but drying is required and productivity is significantly lower than with hot-melt adhesives.
また低重合度のPVAを熱溶融型接着剤として使用する
提案があるが(特関昭51−77632号)この重合度
500以下、鹸化度50−90モル%のPVAでも依然
として溶融粘度が高く、特定な可塑剤を多量に併用しな
いと熱溶融型接着剤として使用出釆ない。There has also been a proposal to use PVA with a low degree of polymerization as a hot-melt adhesive (Tokusei No. 77632/1987), but even PVA with a degree of polymerization of 500 or less and a degree of saponification of 50-90 mol% still has a high melt viscosity. It cannot be used as a hot-melt adhesive unless a large amount of a specific plasticizer is used.
本発明は、これらのPVAの欠点を解消したものであっ
て、平均重合度1000以下の酢酸ビニルを酢酸ィソプ
ロベニルを含有する共重合体の鹸化物である変性PVA
を主体とするもので、これは低融点で溶融粘度が低くか
つ水落性も良好であるという特性を有する水溶性の熱溶
融型接着剤である。The present invention solves these drawbacks of PVA, and uses modified PVA which is a saponified copolymer containing vinyl acetate and isoprobenyl acetate with an average degree of polymerization of 1000 or less.
This is a water-soluble hot-melt adhesive that has the characteristics of a low melting point, low melt viscosity, and good water-removal properties.
本発明の主成分である変性PVAは、酢酸イソプロベニ
ルと酢酸ビニルとの共重合体の鹸化物であり、酢酸ビニ
ルに対して英重合体中に含有する酢酸ィソプロベニルの
量は1モル%化上、好ましくは5〜30モル%である。Modified PVA, which is the main component of the present invention, is a saponified copolymer of isoprobenyl acetate and vinyl acetate, and the amount of isoprobenyl acetate contained in the polymer is 1 mol% relative to vinyl acetate. Preferably it is 5 to 30 mol%.
1モル%以下では、鹸化して得られる変性PVAは従来
のPVAに比べてわずかに熱溶融性が良くなる程度であ
り、好ましくない。If it is less than 1 mol %, the modified PVA obtained by saponification has only slightly better heat meltability than conventional PVA, which is not preferable.
また、変性PVAの平均重合度は低い程溶融粘度が低く
なるので、1000以下であることが必要である。Further, the average degree of polymerization of the modified PVA needs to be 1000 or less, since the lower the melt viscosity is.
重合度1000以下では溶融温度、溶融粘度が高過ぎて
可塑剤を多量に添加しても熱溶融接着剤とはなり得ない
。次に、鹸化度は50モル%以上の部分鹸化、完全鹸化
のいずれでも良いが、重合度が500以上の場合は部分
鹸化の方が好ましい。鹸化度50モル%以下では熱溶融
性は良いが水溶性が劣る。これら共重合体の製造は、前
記の単量体を溶液重合、懸濁重合、塊状重合のいずれの
方法によってもよいが特に溶液重合の場合は、溶剤は特
に限定されないが、メタノール中での溶液重合が鹸化等
の後工程から最も好ましい。If the degree of polymerization is less than 1000, the melting temperature and melt viscosity are too high, and even if a large amount of plasticizer is added, a hot melt adhesive cannot be obtained. Next, partial saponification with a degree of saponification of 50 mol % or more or complete saponification may be used, but partial saponification is preferable when the degree of polymerization is 500 or more. If the degree of saponification is 50 mol% or less, the heat meltability is good but the water solubility is poor. These copolymers may be produced by any method such as solution polymerization, suspension polymerization, or bulk polymerization of the monomers, but especially in the case of solution polymerization, the solvent is not particularly limited, but a solution in methanol is used. Polymerization is most preferred from post-processes such as saponification.
鹸化は通常のPVAを鹸化する方法によって行われるが
、メタノール溶液中で鹸化するのが有利である。これは
、酢酸ィソプロベニルは酢酸ビニルに対して連鎖移動定
数が極めて大きいので連鎖移動定数が比較的低いメタノ
ール中での溶液重合に於いて他に連鎖移動剤を使用する
必要がなく、かつ単量体/メタノール比が高くても低重
合度品が容易に得られ生産性に優れるからである。通常
、PVAに於いて重合度500以下の低重合度品を製造
するには、酢酸ビニルのメタノール溶液重合で連鎖移動
剤、例えばアルデヒド類、ハロゲン化炭化水素類、メル
カプタン類を加えて鹸化する方法、或いは連鎖移動剤中
で酢酸ビニルを重合した後連鎖移動剤を追い出してメタ
ノール溶液に置換して鹸化する方法があるが、前者は鹸
化の際に黄色ないし褐色に着色したり熱溶融時に激しい
分解を併発する。Saponification is carried out by the usual methods of saponifying PVA, preferably in methanol solution. This is because isoprobenyl acetate has an extremely large chain transfer constant compared to vinyl acetate, so there is no need to use other chain transfer agents during solution polymerization in methanol, which has a relatively low chain transfer constant. This is because even if the /methanol ratio is high, products with a low degree of polymerization can be easily obtained and productivity is excellent. Normally, in order to produce a low polymerization degree product of PVA with a polymerization degree of 500 or less, a method is used in which vinyl acetate is polymerized in methanol solution and a chain transfer agent such as aldehydes, halogenated hydrocarbons, or mercaptans is added and saponified. Alternatively, there is a method in which vinyl acetate is polymerized in a chain transfer agent, and then the chain transfer agent is expelled and the saponification is carried out by replacing it with a methanol solution. However, the former method causes discoloration to yellow or brown during saponification and severe decomposition during hot melting. occurs concurrently.
後者の場合も同様であり、更に溶剤の追い出し‘こ多大
の時間と熱量を必要としたり、溶剤の追い出し‘こ伴う
粘度の著しい上昇から必要鷹梓動力の大きな装置が必要
となり生産性の低下及び生産コストの高騰を来たす。そ
れに対し本発明の変性PVAの製造の場合はメタノール
溶液中で上記の如き連鎖移動剤を使用する必要がなく熱
安定性の良いものが得られるし、溶剤の置換の必要がな
い。本発明の熱溶融型接着剤は変性PVA単独でも熱溶
融型接着剤となり得るが可塑剤や融剤の添加が好ましい
。The same is true in the latter case; furthermore, expulsion of the solvent requires a large amount of time and heat, and a significant increase in viscosity due to expulsion of the solvent requires equipment with a large amount of power, resulting in a decrease in productivity and This causes a rise in production costs. On the other hand, in the case of producing the modified PVA of the present invention, it is not necessary to use a chain transfer agent as described above in a methanol solution, and a product with good thermal stability can be obtained, and there is no need to replace the solvent. Although the hot-melt adhesive of the present invention can be made of modified PVA alone, it is preferable to add a plasticizer or a fluxing agent.
可塑剤を併用することにより溶融温度が更に低下する効
果を有し、特に重合度500以上で鹸化度90モル%以
上の変性PVAの場合は併用が望ましい。可塑剤として
は、例えばグリセリン、.エチレングリコール、ジエチ
レングリコール、トリエチレングリコール、トリメチ。
ールプロパンポリオキシチレングリコール、ソルビツト
、マンニツト等の通常に用いられる物質が挙げられ、溶
融温度により揮発性のないものが選ばれる。可塑剤の量
は該変性PVAに対して10〜10の重量部である。融
剤としては、通常の熱溶融型接着剤に使用される物質で
あり、例えばポリエチレン、ポリプロピレン、ポリ酢酸
ビニル、エチレン−酢ビ共重合体等の酢ビ共重合体、ロ
ジン及びロジン誘導体、石油樹脂、スチレンーブタジェ
ンゴム等である。The combined use of a plasticizer has the effect of further lowering the melting temperature, and its combined use is particularly desirable in the case of modified PVA with a degree of polymerization of 500 or more and a degree of saponification of 90 mol% or more. Examples of plasticizers include glycerin, . Ethylene glycol, diethylene glycol, triethylene glycol, trimethy.
Commonly used substances include propane polyoxyethylene glycol, sorbitol, mannitol, and the like, and non-volatile substances are selected depending on the melting temperature. The amount of plasticizer is 10 to 10 parts by weight based on the modified PVA. Fluxing agents include substances used in ordinary hot-melt adhesives, such as polyethylene, polypropylene, polyvinyl acetate, vinyl acetate copolymers such as ethylene-vinyl acetate copolymers, rosin and rosin derivatives, and petroleum. resin, styrene-butadiene rubber, etc.
藤剤を併用することにより接着性が向上する効果がある
。融剤の量は該変性PVAに対して10の重量部以下で
あることが必要で10の重量部以下になると水溶性接着
剤となり得ない。The combined use of rattan has the effect of improving adhesion. The amount of fluxing agent must be 10 parts by weight or less based on the modified PVA, and if it is less than 10 parts by weight, it will not be possible to obtain a water-soluble adhesive.
なお明細書記載の部はいずれも重量基準である。以下、
実施例によって本発明を説明する。Note that all parts described in the specification are based on weight. below,
The invention will be explained by examples.
実施例 1
酢酸ピニル9礎都、ィソプロベニルアセテート20部、
メタノール9の瓜 アゾビスィソブチロニトリル0.8
部の混合液を重合温度60ooで重合させ重合後禾重合
の酢酸ビニル単量体を常法により除去した。Example 1 9 parts of pinyl acetate, 20 parts of isoprobenyl acetate,
Methanol 9 melon Azobisisobutyronitrile 0.8
After the polymerization, the vinyl acetate monomer resulting from the polymerization was removed by a conventional method.
この共重合体中のィソプロベニルアセテート含量は15
モル%であった。次に35%のメタノール溶液に調整し
て1′100モル当量の苛性ソーダにより35ooで鹸
化を行って重合度612、鹸化度90.4モル%の変性
PVAを得た。本変性PVAの融点は98℃であった。
次いで該変性PVAIO礎織こグリセリン15部を配合
して熱溶融型接着剤を作成した。The isoprobenyl acetate content in this copolymer is 15
It was mol%. Next, the solution was adjusted to 35% methanol and saponified with 1'100 molar equivalent of caustic soda at 35 mol% to obtain modified PVA with a degree of polymerization of 612 and a degree of saponification of 90.4 mol%. The melting point of this modified PVA was 98°C.
Next, 15 parts of glycerin was blended with the modified PVAIO base material to prepare a hot-melt adhesive.
この組成物の溶融粘度(島津高化式フローテスターで測
定)は180qoで700比pSであった。又この組成
物は常温水に溶解する。次に、単位面積当り400夕/
あの板紙の片面に180qoで溶融せしめた該組成物を
ローブーコーティングした後(塗工量60夕/〆)、も
う一枚の板紙を重ね、更に180qCに加熱されたプレ
スロールの間を通して板紙を貼り合せた。The melt viscosity of this composition (measured with a Shimadzu Koka flow tester) was 180 qo and 700 pS. This composition also dissolves in water at room temperature. Next, 400 evenings/unit area
After coating one side of that paperboard with the composition melted at 180 qo (coating amount: 60 q/end), another sheet of paper was placed on top of the paperboard, and the paper board was further passed between press rolls heated to 180 qC. Pasted together.
この板紙の接着強度を島津製作所製オートグラフにより
測定したところ常温で紙破し、この時の強度は670夕
/肌中であった。The adhesive strength of this paperboard was measured using an Autograph manufactured by Shimadzu Corporation, and the paper broke at room temperature, and the strength at this time was 670 μm/skin.
実施例 2
実施例1と同様な方法でィソプロベニルアセテート10
モル%のィソプロベニルアセテートー酢酸ビニル共重合
体を得、常法により鹸化して重合度460、鹸化度77
.0モル%の変性M′Aを得た。Example 2 Isoprobenyl acetate 10 was prepared in the same manner as in Example 1.
Mol% of isoprobenyl acetate-vinyl acetate copolymer was obtained and saponified by a conventional method to give a degree of polymerization of 460 and a degree of saponification of 77.
.. 0 mol % of modified M'A was obtained.
この変性PVAの融点は105℃であり、単味の溶融粘
度は180℃で1000比psであった。次いで下記の
組成の接着剤組成物を調製した。The melting point of this modified PVA was 105°C, and the simple melt viscosity was 1000 ps at 180°C. Next, an adhesive composition having the following composition was prepared.
本発明変性PVA IO碇都ロ
ジン変性物 4庇郡ポリエ
チレングリコール#300 25部この組
成物の融点は90oo、溶融粘度は180℃で500比
psであった。実施例1と同じ条件で接着強度を測定し
たところ紙破した。Modified PVA of the Invention IO Ikarito Rosin Modified Product 4 Shogun Polyethylene Glycol #300 25 parts The melting point of this composition was 90oo, and the melt viscosity was 500 ps at 180°C. When the adhesive strength was measured under the same conditions as in Example 1, the paper was torn.
実施例 3
実施例1と同様な方法で、イソプロベニルアセテート2
0モル%、重合度290、鹸化度83モル%の変性PV
Aを得た。Example 3 In a similar manner to Example 1, isoprobenyl acetate 2
Modified PV with a degree of polymerization of 0 mol%, a degree of polymerization of 290, and a degree of saponification of 83 mol%
I got an A.
この変性PVAは、融点90℃、溶融粘度は18ぴ0で
筋0比pSであった。同じく、接着強度を測定したとこ
ろ紙破した。比較例実施例2に於いて、変性PVAに換
えて、重合度420、鹸化度概.3モル%の通常のPV
Aを用いて、実施例2と同様な接着剤組成物を調製した
。This modified PVA had a melting point of 90° C., a melt viscosity of 18 pS, and a sinusoidal ratio pS. Similarly, when the adhesive strength was measured, the paper was found to be torn. Comparative Example In Example 2, modified PVA was replaced with a polymerization degree of 420 and a saponification degree of approximately . 3 mol% normal PV
An adhesive composition similar to Example 2 was prepared using A.
Claims (1)
重合体を50モル%以上鹸化して得られる重合度100
0以下の変性ポリビニルアルコールを主体とする熱溶融
型水溶性接着剤。1 Degree of polymerization 100 obtained by saponifying 50 mol% or more of a vinyl acetate copolymer containing 1 mol% or more of isopropenyl acetate
A hot-melt water-soluble adhesive mainly composed of modified polyvinyl alcohol with a molecular weight of 0 or less.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP14357077A JPS603351B2 (en) | 1977-11-30 | 1977-11-30 | Hot-melt water-soluble adhesive |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP14357077A JPS603351B2 (en) | 1977-11-30 | 1977-11-30 | Hot-melt water-soluble adhesive |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS5476634A JPS5476634A (en) | 1979-06-19 |
| JPS603351B2 true JPS603351B2 (en) | 1985-01-28 |
Family
ID=15341814
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP14357077A Expired JPS603351B2 (en) | 1977-11-30 | 1977-11-30 | Hot-melt water-soluble adhesive |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS603351B2 (en) |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS6395281A (en) * | 1986-10-09 | 1988-04-26 | Unitika Chem Kk | Water-soluble hot melt adhesive for temporary bonding of padding cloth |
-
1977
- 1977-11-30 JP JP14357077A patent/JPS603351B2/en not_active Expired
Also Published As
| Publication number | Publication date |
|---|---|
| JPS5476634A (en) | 1979-06-19 |
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