Deprecated: The each() function is deprecated. This message will be suppressed on further calls in /home/zhenxiangba/zhenxiangba.com/public_html/phproxy-improved-master/index.php on line 456
JP3877072B2 - Paper processed products - Google Patents
[go: Go Back, main page]

JP3877072B2 - Paper processed products - Google Patents

Paper processed products Download PDF

Info

Publication number
JP3877072B2
JP3877072B2 JP2003336714A JP2003336714A JP3877072B2 JP 3877072 B2 JP3877072 B2 JP 3877072B2 JP 2003336714 A JP2003336714 A JP 2003336714A JP 2003336714 A JP2003336714 A JP 2003336714A JP 3877072 B2 JP3877072 B2 JP 3877072B2
Authority
JP
Japan
Prior art keywords
biodegradable resin
emulsion
paper
parts
polymerization
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 - Fee Related
Application number
JP2003336714A
Other languages
Japanese (ja)
Other versions
JP2005103783A (en
Inventor
健治 海老原
和久 池田
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.)
Aica Kogyo Co Ltd
Original Assignee
Aica Kogyo 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 Aica Kogyo Co Ltd filed Critical Aica Kogyo Co Ltd
Priority to JP2003336714A priority Critical patent/JP3877072B2/en
Publication of JP2005103783A publication Critical patent/JP2005103783A/en
Application granted granted Critical
Publication of JP3877072B2 publication Critical patent/JP3877072B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Landscapes

  • Laminated Bodies (AREA)
  • Polymerisation Methods In General (AREA)
  • Graft Or Block Polymers (AREA)
  • Biological Depolymerization Polymers (AREA)
  • Paper (AREA)

Description

本発明は新規な生分解性樹脂組成物からなる接着層を介して接着されている紙加工品に関するものである。   The present invention relates to a processed paper product bonded through an adhesive layer made of a novel biodegradable resin composition.

酢酸ビニルモノマー(以下VAcと略称),アクリル系モノマーなどを乳化重合して得られる樹脂エマルジョンは,従来,接着剤,塗料,紙加工,繊維加工などに広く使用されている。このように広く使用されてはいるものの,種々の問題がある。
問題になっている点には,接着剤が生分解性に不足するため紙加工品などが使用されたのち廃棄されると,分解せずに残留して環境汚染の原因になること,低温での造膜性を確保するために添加されるフタル酸ジブチルなどの可塑剤に環境ホルモンの懸念があり不安視されていること,このような可塑剤の添加により皮膜に可とう性が付与され低温造膜性が得られるものの,皮膜強度が弱くなり耐熱性が低下すること,などがある。
Resin emulsions obtained by emulsion polymerization of vinyl acetate monomer (hereinafter abbreviated as VAc), acrylic monomers and the like have been widely used in adhesives, paints, paper processing, fiber processing, and the like. Although widely used in this way, there are various problems.
The problem is that the adhesive is not biodegradable, so if it is discarded after being used after being processed into paper, it will not decompose and cause environmental pollution. There is concern about environmental hormones in plasticizers such as dibutyl phthalate that are added to ensure film-forming properties, and the addition of such plasticizers gives flexibility to the film, resulting in low temperatures. Although film-forming properties can be obtained, the film strength is weakened and heat resistance is reduced.

特開2002−97437号公報JP 2002-97437 A 特開2001−262100号公報JP 2001-262100 A

このような状況に鑑みて,生分解性樹脂組成物の接着層を介して接着された紙加工品の開発により前記のような課題を解決せんとするものである。 In view of such a situation, the above-mentioned problems are to be solved by developing a paper processed product bonded through an adhesive layer of a biodegradable resin composition.

本発明は生分解性樹脂組成物からなる接着層を介して接着された紙加工品,詳しくは生分解性樹脂を含有する酢酸ビニル樹脂系エマルジョンからなる生分解性の接着剤が使用されたものであつて,接着性,可とう性などの特性を備えるとともに,生分解性を具備する接着層を介して接着され自然環境下に廃棄されても残留して環境汚染などの問題を引き起こさない紙加工品を提供することにある。 The present invention relates to a processed paper article bonded through an adhesive layer made of a biodegradable resin composition, more specifically, a biodegradable adhesive made of a vinyl acetate resin emulsion containing a biodegradable resin. Therefore, paper that has properties such as adhesiveness and flexibility, and that remains bonded even when discarded in the natural environment through an adhesive layer that has biodegradability, does not cause problems such as environmental pollution. To provide processed products.

本発明の係わる生分解性樹脂組成物は,1生分解性樹脂エマルジヨンの存在下においてVAcを乳化重合して調製する方法,2生分解性樹脂をVAcに溶解させたものを,乳化剤存在下において強制乳化した乳化液を乳化剤を水に溶解させた反応液中に滴下して乳化重合して調製する方法により調製される。   The biodegradable resin composition according to the present invention is prepared by emulsion-polymerizing VAc in the presence of 1 biodegradable resin emulsion, and 2 by dissolving the biodegradable resin in VAc in the presence of an emulsifier. It is prepared by a method in which an emulsion emulsified by forcible emulsification is dropped into a reaction solution in which an emulsifier is dissolved in water and emulsion polymerization is performed.

本発明になる紙加工品は,紙と紙,紙とその他の素材との接着に生分解性樹脂組成物からなる接着層を介して接着されているため,包装材などとして使用されたのち,例え其のまま廃棄された場合でも紙等とともに接着層でも生分解が進行して,当初の形状を留めないような分解状態になるため,環境汚染が避けられる。
また,本発明に係わる生分解性樹脂組成物には内分泌攪乱作用の懸念があるフタル酸ジブチルなどの可塑剤を含有しないため,環境汚染の不安なく,各種の紙加工の分野に安心して使用できる。
The processed paper product of the present invention is used as a packaging material and the like because it is bonded to the bond between paper and paper, paper and other materials via an adhesive layer made of a biodegradable resin composition. Even if it is discarded as it is, biodegradation also proceeds in the adhesive layer together with paper etc., and it will be in a decomposed state that does not retain the original shape, so environmental pollution can be avoided.
In addition, since the biodegradable resin composition according to the present invention does not contain a plasticizer such as dibutyl phthalate, which may cause endocrine disrupting action, it can be used safely in various paper processing fields without fear of environmental pollution. .

前記1の方法としては,例えばポリエチレンサクシネート,ポリエチレンサクシネートアジペート,ポリブチレンサクシネート,ポリブチレンサクシネートアジペート,ポリカプロラクトン,ポリカプロラクトンブチレンサクシネートなどの,好ましくはガラス転移点が0℃以下の生分解性樹脂から調製された生分解性樹脂エマルジョン,或いはガラス転移点が0℃以下になるように変性された変性ポリ乳酸,変性ポリヒドロキシブチレート,変性エステル化澱粉などのから調製された生分解性樹脂エマルジョンの存在下において,VAcを公知な方法により乳化重合する方法がある。
このような生分解性樹脂エマルジョンは,元々,結晶性ポリマーのため0℃では造膜しない。しかし,これらをシードとしてVAcを乳化重合することによりポリマー同士が分子レベルで複合化して,生分解性樹脂の結晶化を妨げるため,上記のようなガラス転移点に起因する低温造膜性が得られる。
Examples of the method 1 include polyethylene succinate, polyethylene succinate adipate, polybutylene succinate, polybutylene succinate adipate, polycaprolactone, and polycaprolactone butylene succinate. Biodegradable resin emulsion prepared from degradable resin, or biodegradable prepared from modified polylactic acid, modified polyhydroxybutyrate, modified esterified starch, etc. modified so that the glass transition point is 0 ° C. or lower There is a method of emulsion polymerization of VAc by a known method in the presence of a conductive resin emulsion.
Such a biodegradable resin emulsion originally does not form a film at 0 ° C. because it is a crystalline polymer. However, by emulsion polymerization of VAc using these as seeds, the polymers are combined at the molecular level to prevent crystallization of the biodegradable resin, so that the low-temperature film-forming property due to the glass transition point as described above is obtained. It is done.

前記1の方法は,重合用反応容器に水と乳化剤となるポリビニルアルコール(以下PVAと略称)などを配合し溶解させ,生分解性樹脂エマルジョンを入れ,重合開始剤を用いてVAcを添加しながら進めることができる。この場合,VAcの一部若しくは全部を重合開始剤と水及び生分解性樹脂エマルジョンと一緒に重合用容器に添加するか,或いはVAcの一部あるいは全量を重合中に連続的若しくは断続的に添加しながら進めることができる。
この合成方法により得られる生分解性樹脂組成物の生分解性は,生分解性樹脂エマルジョンの全体中に占める比率により決まるため,配合に関しては,求められる生分解度,乳化重合時及び合成された樹脂エマルジョンの安定性並びにコスト,低温造膜性などを勘案して決めることができる。
生分解度についてはJISK6950に規定されるもので,一般的に易分解性の目安となる60%以上が求められる。
このような生分解性と併せて低温造膜性を確保するためには,生分解性樹脂エマルジョンの固形分が樹脂エマルジョン全体の固形分100重量に対して10重量部以上が求められる。10重量部以下では,十分な生分解性と,期待するような低温造膜性が得られない。
In the above method 1, water and polyvinyl alcohol (hereinafter abbreviated as PVA) as an emulsifier are mixed and dissolved in a polymerization reaction vessel, a biodegradable resin emulsion is added, and VAc is added using a polymerization initiator. Can proceed. In this case, part or all of VAc is added to the polymerization vessel together with the polymerization initiator, water and the biodegradable resin emulsion, or part or all of VAc is added continuously or intermittently during the polymerization. You can proceed while.
Since the biodegradability of the biodegradable resin composition obtained by this synthesis method is determined by the ratio of the biodegradable resin emulsion to the whole, the biodegradability required during the synthesis, emulsion polymerization, and synthesis This can be determined in consideration of the stability and cost of the resin emulsion, low-temperature film-forming properties, and the like.
The degree of biodegradation is specified in JISK6950, and generally 60% or more, which is a standard for easy degradability, is required.
In order to ensure low-temperature film-forming properties together with such biodegradability, the solid content of the biodegradable resin emulsion is required to be 10 parts by weight or more with respect to 100 weight of the solid content of the entire resin emulsion. If it is 10 parts by weight or less, sufficient biodegradability and expected low-temperature film-forming properties cannot be obtained.

前記2の方法としては,前記のポリカプロラクトン(以下PCLと略称)などの生分解性樹脂をVAcに溶解したものを,乳化剤を溶解させた水溶液中に添加して乳化物を調製しておき,乳化剤を水に溶解させた水溶液を加温した状態の中に,攪拌しながら該乳化物を滴下して乳化重合を進めて調製する方法がある。
この合成方法により得られる生分解性樹脂組成物の生分解性は,全体に占める生分解樹脂の比率により決まるため,配合に関しては,VAcに対する生分解性樹脂の溶解度,求められる生分解度,乳化重合時及び合成された樹脂エマルジョンの安定性,コスト並びに低温造膜性などを勘案して決めることができる。
生分解度については前記と同様にJISK6950に規定されるもので,一般的に易分解性の目安となる60%以上が求められる。
なお,生分解性樹脂の配合割合は,VAc及び生分解性樹脂の合計100重量部に対して15重量部以上が生分解性の面から好ましい。これ以下の配合割合では生分解性が十分ではないため適さない。
As the second method, a biodegradable resin such as polycaprolactone (hereinafter abbreviated as PCL) dissolved in VAc is added to an aqueous solution in which an emulsifier is dissolved to prepare an emulsion. There is a method in which the emulsion is added dropwise while stirring in an aqueous solution in which an emulsifier is dissolved in water, and the emulsion polymerization is advanced to prepare.
Since the biodegradability of the biodegradable resin composition obtained by this synthesis method is determined by the ratio of the biodegradable resin in the entire composition, the solubility of the biodegradable resin in VAc, the required biodegradability, and emulsification It can be determined in consideration of the stability of polymerization and the synthesized resin emulsion, cost, and low-temperature film-forming properties.
The degree of biodegradation is defined in JISK6950 as described above, and generally 60% or more, which is a standard for easy degradability, is required.
The blending ratio of the biodegradable resin is preferably 15 parts by weight or more with respect to 100 parts by weight of the total of VAc and biodegradable resin from the viewpoint of biodegradability. A blending ratio below this is not suitable because the biodegradability is not sufficient.

なお,前記2の方法において,生分解性樹脂としてPCLを選定した場合では,それ自体では−60℃というガラス転移点をもつものの,結晶性があるために60℃の融点を示すために0℃での造膜は期待できない。しかし,PCLがVAcに溶解された状態で乳化重合すると両樹脂の分子レベルでの複合化が進みPCLの結晶性が失われることからPCLの持つガラス転移点−60℃という特徴が発現して酢酸ビニル樹脂に柔軟性が付与され,可塑剤の配合が無くても低温造膜性が得られるようになる。
このような作用により低温造膜性が得られるが,低温造膜性の点からも生分解性樹脂のVAcと生分解性樹脂の合計100重量物に対する配合割合は,生分解性と同様に15重量部以上が好ましい。
In the above method 2, when PCL is selected as the biodegradable resin, it itself has a glass transition point of −60 ° C., but it has a crystallinity and thus has a melting point of 60 ° C. No film formation can be expected. However, when emulsion polymerization is performed with PCL dissolved in VAc, both resins are complexed at the molecular level and the crystallinity of PCL is lost. Flexibility is imparted to the vinyl resin, and low-temperature film-forming properties can be obtained without the use of a plasticizer.
Although low-temperature film-forming property is obtained by such an action, the blending ratio of the biodegradable resin VAc and the biodegradable resin with respect to 100 weights in total is 15 as well as biodegradability from the viewpoint of low-temperature film-forming property. Part by weight or more is preferable.

前記1及び2の方法において使用される重合開始剤には,過酸化物系開始剤,アゾ系開始剤,過硫酸塩系開始剤などが使用される。
過酸化物系開始剤としては,ベンゾイルパーオキサイド,ラウリルパーオキサイド,メチルエチルケトンパーオキサイド,ジクミルパーオキサイド,ブチルヒドロパーオキサイド,過酸化水素等が挙げられる。
アゾ系開始剤としては,アゾビスイソブチルニトリル,アゾビスシアノバレリアン酸,アゾビスシアノペンタン酸などが挙げられる。
過硫酸塩系開始剤としては,過硫酸アンモニウム,過硫酸カリウム,過硫酸ナトリウムなどが挙げられる
As the polymerization initiator used in the methods 1 and 2, a peroxide-based initiator, an azo-based initiator, a persulfate-based initiator, or the like is used.
Examples of peroxide initiators include benzoyl peroxide, lauryl peroxide, methyl ethyl ketone peroxide, dicumyl peroxide, butyl hydroperoxide, and hydrogen peroxide.
Examples of the azo initiator include azobisisobutylnitrile, azobiscyanovaleric acid, azobiscyanopentanoic acid, and the like.
Examples of persulfate initiators include ammonium persulfate, potassium persulfate, and sodium persulfate.

乳化剤として使用されるPVAはケン化度86〜90%,重合度400〜4000のものが重合安定性,放置安定性,低温造膜性,構造粘性,耐水性等のバランスに優れるため,単独又は併用される。
なお,乳化剤としては,PVA以外に界面活性剤,水性高分子などが使用されてもよい。
PVA used as an emulsifier has a saponification degree of 86 to 90% and a polymerization degree of 400 to 4000, which has excellent balance of polymerization stability, standing stability, low temperature film-forming property, structural viscosity, water resistance, etc. Used together.
As the emulsifier, a surfactant, an aqueous polymer, etc. may be used in addition to PVA.

また,VAcの他に,(メタ)アクリル酸エステル,プロピオン酸ビニル,バーサチック酸ビニル,(メタ)アクリル酸等のコモノマーと共重合させることもできる。
なお,必要により充填材,顔料,消泡剤,防腐剤等を適時添加できる。
In addition to VAc, it can also be copolymerized with a comonomer such as (meth) acrylic acid ester, vinyl propionate, vinyl versatate, (meth) acrylic acid and the like.
If necessary, fillers, pigments, antifoaming agents, preservatives, etc. can be added as needed.

重合温度は使用する重合開始剤の種類により異なってくる。例えば過硫酸アンモニウムなど熱分解により重合を進める場合は60℃以上の温度が適合している。また,過酸化物と還元剤を組み合わせたレドックス系では60℃以下で進めることができる。   The polymerization temperature varies depending on the type of polymerization initiator used. For example, when polymerization is advanced by thermal decomposition such as ammonium persulfate, a temperature of 60 ° C. or higher is suitable. Moreover, in the redox system which combined the peroxide and the reducing agent, it can proceed at 60 ° C. or lower.

本発明に係わる生分解性樹脂組成物は接着剤のほかに,塗料,繊維加工など各種分野の用途に使用できる。
以下に具体的な用途例として,生分解性樹脂組成物が紙加工用の接着剤として使用される場合を説明する。紙加工用接着剤としては,紙同士,紙とその他の素材との接着に使用される例があり,紙同士の接着例として,包装材,梱包材,緩衝材,紙管,合紙などが挙げられる。紙とその他の素材との接着例として,紙と布,不織布,樹脂フイルム,木材などが挙げられる。
The biodegradable resin composition according to the present invention can be used for applications in various fields such as paint and fiber processing in addition to an adhesive.
As a specific application example, a case where the biodegradable resin composition is used as an adhesive for paper processing will be described below. Examples of paper processing adhesives are used for bonding between papers and between paper and other materials. Examples of bonding between papers include packaging materials, packing materials, cushioning materials, paper tubes, and slip sheets. Can be mentioned. Examples of adhesion between paper and other materials include paper and cloth, non-woven fabric, resin film, and wood.

生分解性接着剤は紙その他の素材に刷毛,ロール,スプレー等の塗布手段により塗布される。塗布量は紙その他の素材の厚み,材質などにより1〜300g/m程度の範囲で塗布される。
また,塗布形態には全面塗布,部分塗布が適宜選択され,部分塗布として格子状,線状,点状,螺旋状など紙加工品の用途,仕上げ,その他の要求に応じた塗布形態を選択して加工することができる。
The biodegradable adhesive is applied to paper or other materials by application means such as a brush, a roll, or a spray. The coating amount is in the range of about 1 to 300 g / m 2 depending on the thickness and material of paper and other materials.
In addition, the entire application and partial application are appropriately selected as the application form, and the application form according to the application, finish, and other requirements of paper products such as grid, line, dot, and spiral is selected as the partial application. Can be processed.

以下に生分解性樹脂組成物の合成例とそれを使用した紙加工品について実施例,比較例により説明する。なお,重量部を単に部として記載する。
生分解性樹脂組成物1の調製例
攪拌機,温度調節器,還流冷却管,温度計を備えた反応容器に水282部,PVA(平均重合度500,ケン化度88%)30.4部を加え,80℃まで加熱して溶解させたのち,PVAを乳化剤として調製されたポリブチレンサクシネートアジペート樹脂エマルジョン(昭和高分子株式会社製 ビオノーレエマルジョンEM−530,固形分53%,23℃における粘度3pa・s ガラス転移温度−55℃)を85部添加した。系内の温度を80℃に保つたままで攪拌しながら,水10部に35%過酸化水素水溶液1部を溶解させた水溶液とVAc165部を3時間にわたって滴下して80℃において乳化重合を進めた。得られた生分解性樹脂組成物1の固形分41.9%,造膜温度0℃,23℃における粘度19pa・sであつた。
該生分解性樹脂組成物1のJISK6950に規定する45日後の生分解度は表1の通りであつた。
Hereinafter, synthesis examples of biodegradable resin compositions and processed paper products using the same will be described with reference to examples and comparative examples. The parts by weight are described simply as parts.
Preparation example of biodegradable resin composition 1 282 parts of water and 30.4 parts of PVA (average polymerization degree 500, saponification degree 88%) were added to a reaction vessel equipped with a stirrer, temperature controller, reflux condenser, and thermometer. In addition, after heating to 80 ° C and dissolving, polybutylene succinate adipate resin emulsion prepared with PVA as an emulsifier (Showa Polymer Co., Ltd. Bionole Emulsion EM-530, solid content 53%, viscosity at 23 ° C 85 parts of 3 pa · s glass transition temperature -55 ° C was added. While stirring while maintaining the temperature in the system at 80 ° C., an aqueous solution in which 1 part of 35% hydrogen peroxide solution was dissolved in 10 parts of water and 165 parts of VAc were added dropwise over 3 hours to proceed emulsion polymerization at 80 ° C. . The obtained biodegradable resin composition 1 had a solid content of 41.9%, a film forming temperature of 0 ° C., and a viscosity of 19 pa · s at 23 ° C.
The biodegradability of the biodegradable resin composition 1 after 45 days as defined in JISK6950 is as shown in Table 1.

生分解性樹脂組成物2の調製例
生分解性樹脂組成物の調製に使用したと同一の反応容器に水130,乳化剤として平均重合度500,ケン化度88モル%のPVA10を加え,80℃まで加温してPVAを溶解させたものを分散媒体として,生分解性樹脂であるポリカプロラクトン「セルグリーンPH−5」(ダイセル化学工業株式会社製 GPC法による測定で数平均分子量6.4万)31.3をVAc135に溶解させたものを前記と同一のPVAの15%水溶液78中に添加し,水60を加えたものを1000RPMで強制攪拌して乳化液として,該乳化液と過硫酸アンモニウム1を水10に溶解したものを,80℃に加熱され,攪拌された該分散媒体中に3時間かけて滴下しながら乳化重合をすすめて生分解性樹脂組成物2を調製した。23℃における粘度17pa・s,造膜温度0℃,固形分41.4%であつた。
該生分解性樹脂組成物2のJISK6950に規定する45日後の生分解度は表1の通りであつた。
Preparation Example of Biodegradable Resin Composition 2 To the same reaction vessel used for the preparation of biodegradable resin composition 1 , add 130 parts of water, 10 parts of PVA having an average polymerization degree of 500 and a saponification degree of 88 mol% as an emulsifier. , Polycaprolactone “Cell Green PH-5”, which is a biodegradable resin, heated to 80 ° C. and dissolved in PVA (number average molecular weight 6 measured by GPC method, manufactured by Daicel Chemical Industries, Ltd.) 40,000) 31.3 parts dissolved in 135 parts of VAc were added to 78 parts of the same 15% aqueous solution of PVA as above, and 60 parts of water was added to force stirring at 1000 RPM to give an emulsion. the emulsified liquid and 1 part of ammonium persulfate those dissolved in 10 parts of water, 80 ° C. is heated, stirred the dropwise over 3 hours in a dispersing medium recommend emulsion polymerization biodegradable tree The composition 2 was prepared. The viscosity at 23 ° C. was 17 pa · s, the film forming temperature was 0 ° C., and the solid content was 41.4%.
The biodegradability of the biodegradable resin composition 2 after 45 days as defined in JISK6950 is as shown in Table 1.

酢酸ビニル樹脂エマルジョン組成物3の調製
生分解性樹脂組成物1の調製に使用したと同一の反応容器を使用し,水を256,平均重合度500,ケン化度88モル%のPVAを17を80℃に加温して溶解させたのち,同温度において攪拌しながらVAc150と,過硫酸アンモンニウム1を水10に溶解したものを3時間かけて滴下して乳化重合を進め,滴下終了したの可塑剤としてフタル酸ジブチル18を加え,冷却して酢酸ビニル樹脂エマルジョン組成物3を調製した。23℃における粘度14pa・s,造膜温度2℃,固形分41.0%であつた。
該酢酸ビニル樹脂エマルジョン組成物3のJISK6950に規定の生分解度は表1の通りであつた。
Preparation of vinyl acetate resin emulsion composition 3 Using the same reaction vessel used for the preparation of biodegradable resin composition 1, 256 parts of water, 17 parts of PVA having an average polymerization degree of 500 and a saponification degree of 88 mol% After the parts were heated to 80 ° C. and dissolved, 150 parts of VAc and 1 part of ammonium persulfate dissolved in 10 parts of water were added dropwise over 3 hours while stirring at the same temperature to proceed with emulsion polymerization. , 18 parts of dibutyl phthalate was added as the Chi plasticizer and completion of the dropwise addition, to prepare a vinyl acetate resin emulsion composition 3 was cooled. The viscosity at 23 ° C. was 14 pa · s, the film forming temperature was 2 ° C., and the solid content was 41.0%.
The degree of biodegradation defined in JISK6950 of the vinyl acetate resin emulsion composition 3 was as shown in Table 1.

実施例,比較例
坪量50g/mのクラフト紙に該生分解性樹脂組成物1,2並びに該酢酸ビニル樹脂エマルジョン3を50g/m塗布したのち,坪量30g/mのクラフト紙を重ねて圧着したのち,乾燥させて実施例1、2並びに比較例の合紙を加工した。
実施例1、2並びに比較例の合紙をアイカ工業株式会社,甚目寺工場の緑地の土中30cmの位置に3ヶ月間埋設したのち,掘り出したものについて剥離強度を測定したところ,表2に示す通り,実施例1及び2においては接着層が生分解して接着力が失われていたため接着層で剥離の状態となり,比較例1では接着層がほとんど生分解されていない状態のため剥離強度が認められた
Example, after the comparative example basis weight 50 g / m 2 kraft paper to biodegradable resin compositions 1, 2 and acetic acid vinyl resin emulsion 3 was 50 g / m 2 coating, basis weight 30 g / m 2 kraft paper After being laminated and pressure-bonded, they were dried to process the slip sheets of Examples 1 and 2 and Comparative Example 1 .
After burying the interleaving papers of Examples 1 and 2 and Comparative Example 1 for 3 months in the green ground of Aika Kogyo Co., Ltd., Kajimeji Factory for 3 months, the peel strength was measured for those dug out. As shown, in Examples 1 and 2, the adhesive layer was biodegraded and the adhesive strength was lost, so the adhesive layer was peeled off. In Comparative Example 1, the adhesive layer was hardly biodegraded, so the peel strength was Was recognized



測定方法
JISK6950に規定する生分解度の測定方法において,45日後の生分解度を測定する。


Measurement method In the biodegradation measurement method specified in JISK6950, the biodegradation after 45 days is measured.


本発明になる紙加工品は,各種の紙加工品として使用されたのち廃棄され,生分解することが期待されるような品目,例えば包装材,梱包材,飲食品容器,ラベルなどの用途分野において,今後使用拡大が予想される。 The processed paper products according to the present invention are used as various paper processed products, and are discarded and expected to be biodegradable, such as packaging materials, packaging materials, food and drink containers, labels, etc. In the future, the use is expected to expand.

Claims (2)

生分解性樹脂エマルジョンの存在下において酢酸ビニルモノマーが乳化重合されて調製された最低造膜温度が0℃以下である水系生分解性樹脂エマルジョン組成物を塗布し、圧締することによって接着され、生分解性を有することを特徴とする紙加工品。A water-based biodegradable resin emulsion composition prepared by emulsion polymerization of vinyl acetate monomer in the presence of a biodegradable resin emulsion and having a minimum film forming temperature of 0 ° C. or less is applied and bonded by pressing. Paper processed product characterized by being biodegradable. 生分解性樹脂を酢酸ビニルモノマーに溶解させたものを乳化剤存在下において強制乳化してなる乳化液を、乳化剤を水に溶解させた反応液中に滴下して乳化重合して調製された最低造膜温度が0℃以下である水系生分解性樹脂エマルジョン組成物を塗布し、圧締することによって接着され、生分解性を有することを特徴とする紙加工品。An emulsion prepared by forcibly emulsifying a biodegradable resin dissolved in a vinyl acetate monomer in the presence of an emulsifier and dropping it into a reaction solution in which the emulsifier is dissolved in water. A paper processed product characterized in that it is bonded by applying a water-based biodegradable resin emulsion composition having a membrane temperature of 0 ° C. or less and pressing, and has biodegradability.
JP2003336714A 2003-09-29 2003-09-29 Paper processed products Expired - Fee Related JP3877072B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2003336714A JP3877072B2 (en) 2003-09-29 2003-09-29 Paper processed products

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2003336714A JP3877072B2 (en) 2003-09-29 2003-09-29 Paper processed products

Publications (2)

Publication Number Publication Date
JP2005103783A JP2005103783A (en) 2005-04-21
JP3877072B2 true JP3877072B2 (en) 2007-02-07

Family

ID=34532732

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2003336714A Expired - Fee Related JP3877072B2 (en) 2003-09-29 2003-09-29 Paper processed products

Country Status (1)

Country Link
JP (1) JP3877072B2 (en)

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2007070423A (en) * 2005-09-06 2007-03-22 Oshika:Kk Polylactic acid-based aqueous adhesive composition for wood
FR2916203B1 (en) * 2007-05-14 2012-07-20 Arkema COEXTRUSION BINDERS BASED ON RENEWABLE / BIODEGRADABLE
CN112409551B (en) * 2020-11-26 2022-12-06 广东省邦得利新材料技术有限公司 Degradable polylactic resin film-forming emulsion and preparation method and application thereof

Also Published As

Publication number Publication date
JP2005103783A (en) 2005-04-21

Similar Documents

Publication Publication Date Title
JPS5829871A (en) Manufacture of flexible laminate
US4725639A (en) Process for preparing pressure sensitive adhesives
EP0530013B1 (en) Emulsion polymerisation
JP3877072B2 (en) Paper processed products
CN108251047A (en) A kind of preparation method of compound type starch adhesive
JP3670049B2 (en) Delayed tack type pressure-sensitive adhesive composition
US3692713A (en) Labeling adhesive composition
JPH08218039A (en) Biodegradable adhesive sheet
US3515630A (en) Resin adhesive composition and laminated structure utilizing the same
US5055504A (en) Surface coating compositions
EP0727469A2 (en) Aqueous adhesive compositions for use in binding books
JP2006036878A (en) Aqueous adhesive composition
JP4151950B2 (en) Adhesive composition
EP0351193A2 (en) Surface coating compositions
JPH0543855A (en) Releasable self-adhesive composition
JP3979657B2 (en) Adhesive composition
JP3681122B2 (en) Woodworking bonding method
WO2023021975A1 (en) Composition for forming pressure-sensitive adhesive, production method therefor, and pressure-sensitive adhesive composition
JPH0118112B2 (en)
JP4092924B2 (en) Biodegradable adhesive
JP3065255B2 (en) Adhesive composition and paper tube using the same
JP4012971B2 (en) Water-based adhesive composition and process for producing the same
JPS6248993B2 (en)
US7488765B2 (en) Gum adhesive based on a filled polymer dispersion
Kim et al. Characteristics of non-plasticizer PVAc resin for wood products

Legal Events

Date Code Title Description
A977 Report on retrieval

Free format text: JAPANESE INTERMEDIATE CODE: A971007

Effective date: 20060418

A131 Notification of reasons for refusal

Free format text: JAPANESE INTERMEDIATE CODE: A131

Effective date: 20060420

A521 Written amendment

Free format text: JAPANESE INTERMEDIATE CODE: A523

Effective date: 20060614

A131 Notification of reasons for refusal

Free format text: JAPANESE INTERMEDIATE CODE: A131

Effective date: 20060628

A521 Written amendment

Free format text: JAPANESE INTERMEDIATE CODE: A523

Effective date: 20060720

A131 Notification of reasons for refusal

Free format text: JAPANESE INTERMEDIATE CODE: A131

Effective date: 20060810

A521 Written amendment

Free format text: JAPANESE INTERMEDIATE CODE: A523

Effective date: 20061004

TRDD Decision of grant or rejection written
A01 Written decision to grant a patent or to grant a registration (utility model)

Free format text: JAPANESE INTERMEDIATE CODE: A01

Effective date: 20061019

A61 First payment of annual fees (during grant procedure)

Free format text: JAPANESE INTERMEDIATE CODE: A61

Effective date: 20061025

R150 Certificate of patent or registration of utility model

Free format text: JAPANESE INTERMEDIATE CODE: R150

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20101110

Year of fee payment: 4

LAPS Cancellation because of no payment of annual fees