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JPH0348236B2 - - Google Patents
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JPH0348236B2 - - Google Patents

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Publication number
JPH0348236B2
JPH0348236B2 JP8853382A JP8853382A JPH0348236B2 JP H0348236 B2 JPH0348236 B2 JP H0348236B2 JP 8853382 A JP8853382 A JP 8853382A JP 8853382 A JP8853382 A JP 8853382A JP H0348236 B2 JPH0348236 B2 JP H0348236B2
Authority
JP
Japan
Prior art keywords
vinyl chloride
room temperature
weight
plastisol
parts
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired
Application number
JP8853382A
Other languages
Japanese (ja)
Other versions
JPS58204075A (en
Inventor
Akio Taga
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 JP8853382A priority Critical patent/JPS58204075A/en
Publication of JPS58204075A publication Critical patent/JPS58204075A/en
Publication of JPH0348236B2 publication Critical patent/JPH0348236B2/ja
Granted legal-status Critical Current

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  • Manufacture Of Porous Articles, And Recovery And Treatment Of Waste Products (AREA)
  • Adhesives Or Adhesive Processes (AREA)

Description

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

<産業上の利用分野> 本発明は、常温では未発泡固体状で加熱使用後
には体積を膨張して発泡体を形成する発泡性ホツ
トメルト接着剤の製造法に関する。 <従来技術と問題点> 従来より、ホツトメルト接着剤はエチレン−酢
酸ビニル共重合体(EVA)樹脂又はポリアミド
樹脂などのペースレジンに、ロジンや石油樹脂な
どの各種樹脂類による粘着付与剤、及びワツク
ス、パラフインなどの低溶融化と速固化剤などの
変性剤を熱溶融させて混合することにより製造し
ていた。従つて、加熱分解型の発泡剤を混入する
とホツトメルト接着剤製造時に発泡してしまうた
め、常温では未発泡体で加熱使用後に発泡体を形
成する発泡性ホツトメルト接着剤を製造すること
は不可能であつた。 <発明の目的> 本発明の目的は、常温では未発泡固体状で加熱
使用後には体積を膨張して発泡体を形成する発泡
性ホツトメルト接着剤の製造法を提供することに
ある。 <発明の開示> 本発明は、塩化ビニル系ペーストレジン100重
量部に対して、塩化ビニル用可塑剤50〜200重量
部及び分解温度150〜210℃の加熱分解型発泡剤
0.1〜20重量部を必須成分として調整した常温で
液状のプラスチゾルを、常温放置又は加熱して半
ゲル化状態にする前後に、粒状又はペレツト状或
いはシート状に加工し、常温でべとつきがない程
度に半ゲル化状態にする発泡性ホツトメルト接着
剤の製造法である。 本発明で使用する塩化ビニル系ペーストレジン
とは、塩化ビニルモノマー単独及び共重合する酢
酸ビニルモノマー等を乳化重合して得られる微粉
末状の塩化ビニル系樹脂で、ゼオン121,131,
135,400×110A(日本ゼオンKK製)、スミリツト
PXN(住友化学工業KK製)など公知の塩化ビニ
ル系ペーストレジンでよいが、密着性、低温溶融
性、低温発泡成形性を要求する場合には、塩化ビ
ニル−酢酸ビニル共重合体又はカルボキシル基導
入レジンを混入しておくのが良い。 塩化ビニル用可塑剤とは、DOP,DBPなどの
フタル酸エステル系、TCP(リン酸トリクレジ
ル)などのリン酸エステル系、DOA(ジオクチル
アジペート)などのアジペート系、塩化パラフイ
ン系、DAP(ジアリルフタレート)モノマーの如
きアリルエステル系熱硬化性可塑剤、アクリル酸
エステル系、不飽和ポリエステル系などの他に、
安定剤の役目をなすエポキシ系など、加熱するこ
とにより塩化ビニル樹脂と相溶性を有する公知の
可塑剤で良い。 分解温度150〜210℃の加熱分解型発泡剤とは、
ニトロソ化合物、アゾジカルボンアミドやアゾビ
ス・イソブチロニトリルなどのアゾ化合物、ベン
ゼン・スルホニル・ヒドラジドなどのスルホニ
ル・ヒドラジド系など微粉末からなる加熱により
分解ガスを発生する発泡剤が使用できるが、この
うちでもアゾ化合物が一般的に用いられる。 上記必須成分の他に、プラスチゾル中には塩化
ビニル用安定剤が添加され、金属セツケン類、無
機酸塩類、有機スズ化合物、カルシウム−亜鉛
系、カドミウム有機複合体、カドミウム−バリウ
ム系などの複合安定剤などがあるが、液状の複合
安定剤が好適である。また必要に応じて、炭カ
ル、硅石粉等の無機質フイラーや繊維類も添加す
ることもできる。 プラスチゾルはこの性質上、(a)常温ではレジン
粒子の表面はわずかに可塑剤で溶媒和している
が、粒子同志は互に自由に移動し、粘稠なゾルと
して流動している。しかし、(b)レジンとの相溶性
が大きく低分子量からなる可塑剤中では常温で経
時後に、また通常の前記可塑剤中でも加熱するこ
とにより、レジン粒子の膨潤はかなり進行して粒
子同志はその表層でルーズに溶け合つて固化し、
もはや流動性は失われるが、粒子の中心部は末ゲ
ル化で、ゲルの物理的強度は乏しく、表面に光沢
なく半透明である(半ゲル化状態)。更に高温に
加熱すると、(c)レジン粒子全体が芯まで完全にケ
ル化膨潤と同時に溶融して流れ、溶媒和した塩化
ビニル分子は活発なミクロブラウン運動を起こし
て、粒子間の分子同志のからみ合いが強くなり、
物理的強度は最高に達し、表面に光沢を生じ透明
となる(完全溶融状態)。次に、(d)完全溶融状態
中で、加熱分解型発泡剤が分解してガスを発生し
発泡体を形成する(発泡体形成状態)。 本発明は、上記の如きプラスチゾルの性質を利
用して、(a)常温で流動状態のプラスチゾルを、(b)
半ゲル化状態にする前後に、粒状又はペレツト或
いはシート状に加工するものである。また得られ
た発泡性ホツトメルト接着剤は、(c)完全溶融状態
及び(d)発泡体形成状態を経て接着剤としての機能
を発揮する。 本発明で重要な要件となるプラスチゾルの組成
としては、前記「特許請求の範囲」の如くであ
る。すなわち、その理由は前記ペーストレンジ
100重量部に対して、前記可塑剤が50重量部
(PHR)以下の組成物では、常温の液状でプラス
チゾルが得られず、また前記可塑剤が200重量部
(PHR)以上の組成物では、半ゲル化状態にして
も常温でべとつきがあるからである。次に、加熱
分解型発泡剤の分解温度としては150℃〜210℃で
あり、その理由は150℃以下では、プラスチゾル
が完全溶融状態にある以下の温度であり、良好な
発泡体が得られないからであり、また、210℃以
上の温度では溶融状態の粘度が低くて分解ガスが
発散して良好な発泡体が得られないからである。
次に、発泡剤の添加量としては、0.1〜20重量部
(PHR)であり、その理由は0.1PHR以下では発
泡体が得られず、20PHR以上では高発泡倍率に
なりすぎたり、未分解の発泡剤が残存して、接着
力の低下をもたらすからである。 次に、上記の如く常温で液状のプラスチゾルを
半ゲル化状態にする方法としては、通常、作業性
の点から加熱法を採用するが、加熱温度として
は、プラスチゾルの表面温度が完全溶融温度又は
発泡剤の分解温度以下では、かつゲル化温度以上
の範囲で行う必要があり、可塑剤の種類及び配合
量、ペーストレジンの種類及び配合量、発泡剤の
種類、及び膜厚などにより異なるが、通常50〜
100℃の範囲で数分間要すれば製造できる。例え
ば、粒状にしたい時には温水中に滴下する。また
シート状にしたい場合には剥離紙上にナイフコー
ターやロールコーターで塗布し熱風乾燥機中を通
過させればよい。また熱盤上に薄く流し込み半ゲ
ル化状態に加工後、切削又は粉砕することによつ
ても任意形状に成形できる。 <発明の作用効果> この様にして製造された該発泡性ホツトメルト
接着剤は、完全溶融温度でかつ発泡剤の分解温度
以上に加熱することにより発泡接着剤又はシーラ
ントとしての機能を発揮するが、通常150〜210℃
の範囲でその機能を発揮する。そして、凹凸面か
らなる被着体、ハニカム構造体などの接着剤とし
て、更にスポツ溶接部等のシール材などの様に、
被着材への密着性と軽量で空隙充填性が要求され
る接着シール材として有用である。 次に本発明を実施例により説明する。 実施例 1
<Industrial Application Field> The present invention relates to a method for producing a foamable hot melt adhesive which is in an unfoamed solid state at room temperature and expands in volume to form a foam after being heated and used. <Prior art and problems> Traditionally, hot melt adhesives have been made of a paste resin such as ethylene-vinyl acetate copolymer (EVA) resin or polyamide resin, a tackifier made of various resins such as rosin or petroleum resin, and wax. It was produced by hot-melting and mixing low-melting agents such as paraffin and modifiers such as fast-setting agents. Therefore, if a thermally decomposable foaming agent is mixed in, the hot melt adhesive will foam during production, so it is impossible to produce a foamable hot melt adhesive that is unfoamed at room temperature and forms a foam after heating. It was hot. <Object of the Invention> An object of the present invention is to provide a method for producing a foamable hot melt adhesive that is in an unfoamed solid state at room temperature and expands in volume to form a foam after being heated and used. <Disclosure of the invention> The present invention provides 50 to 200 parts by weight of a plasticizer for vinyl chloride and a thermally decomposable foaming agent with a decomposition temperature of 150 to 210°C to 100 parts by weight of a vinyl chloride paste resin.
Plastisol, which is liquid at room temperature with 0.1 to 20 parts by weight as an essential ingredient, is left at room temperature or heated to a semi-gelled state, and then processed into granules, pellets, or sheets to the extent that it does not become sticky at room temperature. This is a method for producing a foamable hot melt adhesive that is brought into a semi-gelled state. The vinyl chloride paste resin used in the present invention is a finely powdered vinyl chloride resin obtained by emulsion polymerization of vinyl chloride monomer alone and copolymerized vinyl acetate monomer, etc.
135,400×110A (manufactured by Nippon Zeon KK), Sumiritz
Known vinyl chloride paste resins such as PXN (manufactured by Sumitomo Chemical KK) may be used, but if adhesion, low-temperature melting properties, and low-temperature foaming moldability are required, vinyl chloride-vinyl acetate copolymers or carboxyl group-introduced resins may be used. It is better to mix resin. Plasticizers for vinyl chloride include phthalate esters such as DOP and DBP, phosphate esters such as TCP (tricresyl phosphate), adipates such as DOA (dioctyl adipate), chlorinated paraffin, and DAP (diallyl phthalate). In addition to monomers such as allyl ester thermosetting plasticizers, acrylic esters, unsaturated polyesters, etc.
Any known plasticizer that is compatible with vinyl chloride resin when heated, such as an epoxy-based plasticizer that acts as a stabilizer, may be used. What is a thermally decomposable blowing agent with a decomposition temperature of 150 to 210℃?
Foaming agents that generate decomposed gas when heated are available, including fine powders such as nitroso compounds, azo compounds such as azodicarbonamide and azobis/isobutyronitrile, and sulfonyl/hydrazide systems such as benzene/sulfonyl/hydrazide. However, azo compounds are commonly used. In addition to the above essential components, stabilizers for vinyl chloride are added to plastisol to stabilize complexes such as metal soaps, inorganic acid salts, organic tin compounds, calcium-zinc systems, cadmium organic complexes, and cadmium-barium systems. There are various stabilizers, but liquid composite stabilizers are preferred. Inorganic fillers such as charcoal and silica powder and fibers may also be added as required. Plastisol has these properties: (a) At room temperature, the surfaces of resin particles are slightly solvated with plasticizer, but the particles move freely among themselves and flow as a viscous sol. However, (b) in a plasticizer that has high compatibility with the resin and has a low molecular weight, the swelling of the resin particles progresses considerably after aging at room temperature, or when heated in a normal plasticizer. They melt together loosely on the surface layer and solidify,
Although fluidity is no longer lost, the center of the particle is partially gelled, the physical strength of the gel is poor, and the surface is translucent with no gloss (semi-gelled state). When heated to a higher temperature, (c) the entire resin particle completely melts and swells to the core and flows, and the solvated vinyl chloride molecules cause active micro-Brownian motion, causing molecular entanglement between the particles. The relationship becomes stronger,
Its physical strength reaches its maximum, and the surface becomes glossy and transparent (completely molten state). Next, (d) in a completely molten state, the thermally decomposable foaming agent decomposes to generate gas and form a foam (foam forming state). The present invention takes advantage of the properties of plastisol as described above to convert (a) plastisol in a fluid state at room temperature, and (b)
It is processed into granules, pellets, or sheets before and after making it into a semi-gelled state. Further, the obtained foamable hot melt adhesive exhibits its function as an adhesive after passing through (c) a completely melted state and (d) a foamed state. The composition of plastisol, which is an important requirement in the present invention, is as described in the claims above. That is, the reason is the paste range
If the composition contains 50 parts by weight (PHR) or less of the plasticizer per 100 parts by weight, plastisol cannot be obtained in liquid form at room temperature, and if the composition contains 200 parts by weight (PHR) or more of the plasticizer, This is because even in a semi-gelled state, it remains sticky at room temperature. Next, the decomposition temperature of thermally decomposable foaming agents is 150°C to 210°C.The reason is that below 150°C, plastisol is in a completely molten state, and good foam cannot be obtained. Moreover, at a temperature of 210° C. or higher, the viscosity of the molten state is low and decomposition gas is released, making it impossible to obtain a good foam.
Next, the amount of foaming agent added is 0.1 to 20 parts by weight (PHR).The reason for this is that if it is less than 0.1 PHR, a foam cannot be obtained, and if it is more than 20 PHR, the foaming ratio will be too high or the undecomposed This is because the foaming agent remains, resulting in a decrease in adhesive strength. Next, as a method for converting plastisol, which is liquid at room temperature, into a semi-gelled state as described above, a heating method is usually adopted from the viewpoint of workability. It is necessary to carry out the process at a temperature below the decomposition temperature of the blowing agent and above the gelling temperature, which varies depending on the type and amount of plasticizer, the type and amount of paste resin, the type of blowing agent, and the film thickness. Usually 50~
It can be manufactured in a few minutes at a temperature of 100°C. For example, if you want to make it into granules, drop it into warm water. If it is desired to form a sheet, it may be coated on release paper using a knife coater or roll coater and passed through a hot air dryer. It can also be molded into any shape by pouring it thinly onto a hot plate, processing it into a semi-gelled state, and then cutting or crushing it. <Operations and Effects of the Invention> The foamable hot melt adhesive produced in this manner exhibits its function as a foam adhesive or sealant by heating to a complete melting temperature and above the decomposition temperature of the foaming agent. Normally 150~210℃
It performs its functions within the range of. It can be used as an adhesive for adherends with uneven surfaces, honeycomb structures, etc., and as a sealant for spot welds, etc.
It is useful as an adhesive sealant that requires adhesion to adherends, light weight, and void-filling properties. Next, the present invention will be explained by examples. Example 1

【表】【table】

【表】 第1表に示すプラスチゾル配合物を、ナイフコ
ーターを用いて、剥離紙上に約300g/m2(厚さ
0.3mm)になる様に塗布し、80℃の熱風乾燥器中
を3分間要して通過させて常温に冷却し、そのま
ま巻き取ることにより本発明の発泡性ホツトメル
ト接着剤を製造した。 次に、網目のついたセメント石綿板表面と、凹
凸度0.2〜0.3mmのエンボス加工された銅箔とを、
該発泡性ホツトメルト接着剤(シート)を挾ん
で、200℃の熱風乾燥器中で5分間要して接着し
た。接着加工後の接着層は凹凸部も完全に発泡体
で充填接着加工されていることを確認した。
[Table] The plastisol formulation shown in Table 1 was coated on release paper using a knife coater at approximately 300 g/m 2 (thickness
The foamable hot melt adhesive of the present invention was produced by applying the adhesive to a thickness of 0.3 mm), passing it through a hot air dryer at 80° C. for 3 minutes, cooling it to room temperature, and winding it up. Next, the meshed cement asbestos board surface and the embossed copper foil with an unevenness of 0.2 to 0.3 mm were
The foamable hot melt adhesive (sheet) was sandwiched and bonded for 5 minutes in a hot air dryer at 200°C. It was confirmed that the uneven parts of the adhesive layer after adhesive processing were completely filled with foam and adhesive processed.

Claims (1)

【特許請求の範囲】 1 塩化ビニル系ペーストレジン100重量部に対
して、塩化ビニル用可塑剤50〜200重量部及び分
解温度150〜210℃の加熱分解型発泡剤0.1〜20重
量部を必須成分として調整した常温で液状のプラ
スチゾルを、常温放置又は加熱して半ゲル化状態
にする前後に、粒状又はペレツト状或いはシート
状に加工し、常温でべとつきがない程度に半ゲル
化状態にすることを特徴とする発泡性ホツトメル
ト接着剤の製造法。 2 塩化ビニル系ペーストレジンが、塩化ビニル
−酢酸ビニル共重合体又はカルボキシル基導入レ
ジンが混入されている特許請求の範囲第1項記載
の発泡性ホツトメルト接着剤の製造法。
[Claims] 1. 50 to 200 parts by weight of a plasticizer for vinyl chloride and 0.1 to 20 parts by weight of a thermally decomposable blowing agent with a decomposition temperature of 150 to 210°C are essential components for 100 parts by weight of vinyl chloride paste resin. Plastisol, which is liquid at room temperature and has been prepared as a plastisol, is left at room temperature or heated to make it into a semi-gelled state, and then processed into granules, pellets, or sheets to make it into a semi-gelled state to the extent that it is not sticky at room temperature. A method for producing a foamable hot melt adhesive characterized by: 2. The method for producing a foamable hot melt adhesive according to claim 1, wherein the vinyl chloride paste resin contains a vinyl chloride-vinyl acetate copolymer or a carboxyl group-introduced resin.
JP8853382A 1982-05-25 1982-05-25 Preparation of foamable hot-melt adhesive Granted JPS58204075A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP8853382A JPS58204075A (en) 1982-05-25 1982-05-25 Preparation of foamable hot-melt adhesive

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP8853382A JPS58204075A (en) 1982-05-25 1982-05-25 Preparation of foamable hot-melt adhesive

Publications (2)

Publication Number Publication Date
JPS58204075A JPS58204075A (en) 1983-11-28
JPH0348236B2 true JPH0348236B2 (en) 1991-07-23

Family

ID=13945470

Family Applications (1)

Application Number Title Priority Date Filing Date
JP8853382A Granted JPS58204075A (en) 1982-05-25 1982-05-25 Preparation of foamable hot-melt adhesive

Country Status (1)

Country Link
JP (1) JPS58204075A (en)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0296042A (en) * 1988-09-30 1990-04-06 Yodogawa Steel Works Ltd Manufacturing of member with packing and connection structure of building material with packing and metallic building material
TWI714815B (en) * 2016-12-26 2021-01-01 日商迪愛生股份有限公司 Articles, article manufacturing methods and void filling methods

Also Published As

Publication number Publication date
JPS58204075A (en) 1983-11-28

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