JPS6146024B2 - - Google Patents
Info
- Publication number
- JPS6146024B2 JPS6146024B2 JP10832079A JP10832079A JPS6146024B2 JP S6146024 B2 JPS6146024 B2 JP S6146024B2 JP 10832079 A JP10832079 A JP 10832079A JP 10832079 A JP10832079 A JP 10832079A JP S6146024 B2 JPS6146024 B2 JP S6146024B2
- Authority
- JP
- Japan
- Prior art keywords
- rosin
- pressure
- sensitive adhesive
- disproportionated rosin
- purified
- 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
- RSWGJHLUYNHPMX-UHFFFAOYSA-N Abietic-Saeure Natural products C12CCC(C(C)C)=CC2=CCC2C1(C)CCCC2(C)C(O)=O RSWGJHLUYNHPMX-UHFFFAOYSA-N 0.000 claims description 91
- 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 claims description 91
- 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 claims description 91
- 150000002148 esters Chemical class 0.000 claims description 33
- 239000004820 Pressure-sensitive adhesive Substances 0.000 claims description 28
- 150000005846 sugar alcohols Polymers 0.000 claims description 12
- 244000043261 Hevea brasiliensis Species 0.000 claims description 7
- 229920003052 natural elastomer Polymers 0.000 claims description 7
- 229920001194 natural rubber Polymers 0.000 claims description 7
- 229920003051 synthetic elastomer Polymers 0.000 claims description 7
- 239000005061 synthetic rubber Substances 0.000 claims description 7
- 239000000126 substance Substances 0.000 description 16
- PEDCQBHIVMGVHV-UHFFFAOYSA-N Glycerine Chemical compound OCC(O)CO PEDCQBHIVMGVHV-UHFFFAOYSA-N 0.000 description 13
- 238000007323 disproportionation reaction Methods 0.000 description 13
- -1 glycerin ester Chemical class 0.000 description 10
- YXFVVABEGXRONW-UHFFFAOYSA-N Toluene Chemical compound CC1=CC=CC=C1 YXFVVABEGXRONW-UHFFFAOYSA-N 0.000 description 9
- 239000000853 adhesive Substances 0.000 description 9
- 230000001070 adhesive effect Effects 0.000 description 9
- 235000011187 glycerol Nutrition 0.000 description 9
- 239000002904 solvent Substances 0.000 description 9
- 238000000746 purification Methods 0.000 description 8
- 230000032683 aging Effects 0.000 description 7
- 239000003054 catalyst Substances 0.000 description 7
- QTBSBXVTEAMEQO-UHFFFAOYSA-N Acetic acid Chemical compound CC(O)=O QTBSBXVTEAMEQO-UHFFFAOYSA-N 0.000 description 6
- UHOVQNZJYSORNB-UHFFFAOYSA-N Benzene Chemical compound C1=CC=CC=C1 UHOVQNZJYSORNB-UHFFFAOYSA-N 0.000 description 6
- 239000002313 adhesive film Substances 0.000 description 5
- 239000002994 raw material Substances 0.000 description 5
- 239000000243 solution Substances 0.000 description 5
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 4
- 239000002253 acid Substances 0.000 description 4
- 230000032050 esterification Effects 0.000 description 4
- 238000005886 esterification reaction Methods 0.000 description 4
- XEKOWRVHYACXOJ-UHFFFAOYSA-N Ethyl acetate Chemical compound CCOC(C)=O XEKOWRVHYACXOJ-UHFFFAOYSA-N 0.000 description 3
- LYCAIKOWRPUZTN-UHFFFAOYSA-N Ethylene glycol Chemical compound OCCO LYCAIKOWRPUZTN-UHFFFAOYSA-N 0.000 description 3
- IMNFDUFMRHMDMM-UHFFFAOYSA-N N-Heptane Chemical compound CCCCCCC IMNFDUFMRHMDMM-UHFFFAOYSA-N 0.000 description 3
- 230000002411 adverse Effects 0.000 description 3
- 230000000052 comparative effect Effects 0.000 description 3
- MTHSVFCYNBDYFN-UHFFFAOYSA-N diethylene glycol Chemical compound OCCOCCO MTHSVFCYNBDYFN-UHFFFAOYSA-N 0.000 description 3
- 238000004821 distillation Methods 0.000 description 3
- 238000004519 manufacturing process Methods 0.000 description 3
- 239000000463 material Substances 0.000 description 3
- 238000000034 method Methods 0.000 description 3
- 239000000203 mixture Substances 0.000 description 3
- 150000002978 peroxides Chemical class 0.000 description 3
- 229910001220 stainless steel Inorganic materials 0.000 description 3
- 239000010935 stainless steel Substances 0.000 description 3
- CSCPPACGZOOCGX-UHFFFAOYSA-N Acetone Chemical compound CC(C)=O CSCPPACGZOOCGX-UHFFFAOYSA-N 0.000 description 2
- VTYYLEPIZMXCLO-UHFFFAOYSA-L Calcium carbonate Chemical compound [Ca+2].[O-]C([O-])=O VTYYLEPIZMXCLO-UHFFFAOYSA-L 0.000 description 2
- HEDRZPFGACZZDS-UHFFFAOYSA-N Chloroform Chemical compound ClC(Cl)Cl HEDRZPFGACZZDS-UHFFFAOYSA-N 0.000 description 2
- PXHVJJICTQNCMI-UHFFFAOYSA-N Nickel Chemical compound [Ni] PXHVJJICTQNCMI-UHFFFAOYSA-N 0.000 description 2
- CTQNGGLPUBDAKN-UHFFFAOYSA-N O-Xylene Chemical compound CC1=CC=CC=C1C CTQNGGLPUBDAKN-UHFFFAOYSA-N 0.000 description 2
- 239000004793 Polystyrene Substances 0.000 description 2
- 229910000831 Steel Inorganic materials 0.000 description 2
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 description 2
- RAHZWNYVWXNFOC-UHFFFAOYSA-N Sulphur dioxide Chemical compound O=S=O RAHZWNYVWXNFOC-UHFFFAOYSA-N 0.000 description 2
- 229920001400 block copolymer Polymers 0.000 description 2
- 238000007796 conventional method Methods 0.000 description 2
- 238000002425 crystallisation Methods 0.000 description 2
- 230000008025 crystallization Effects 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 239000012467 final product Substances 0.000 description 2
- 238000010438 heat treatment Methods 0.000 description 2
- UKVIEHSSVKSQBA-UHFFFAOYSA-N methane;palladium Chemical compound C.[Pd] UKVIEHSSVKSQBA-UHFFFAOYSA-N 0.000 description 2
- 238000002156 mixing Methods 0.000 description 2
- VLKZOEOYAKHREP-UHFFFAOYSA-N n-Hexane Chemical compound CCCCCC VLKZOEOYAKHREP-UHFFFAOYSA-N 0.000 description 2
- 229910052757 nitrogen Inorganic materials 0.000 description 2
- WXZMFSXDPGVJKK-UHFFFAOYSA-N pentaerythritol Chemical compound OCC(CO)(CO)CO WXZMFSXDPGVJKK-UHFFFAOYSA-N 0.000 description 2
- BASFCYQUMIYNBI-UHFFFAOYSA-N platinum Chemical compound [Pt] BASFCYQUMIYNBI-UHFFFAOYSA-N 0.000 description 2
- 229920002223 polystyrene Polymers 0.000 description 2
- 238000007670 refining Methods 0.000 description 2
- 238000005096 rolling process Methods 0.000 description 2
- 239000010959 steel Substances 0.000 description 2
- 238000010998 test method Methods 0.000 description 2
- 238000005303 weighing Methods 0.000 description 2
- 239000008096 xylene Substances 0.000 description 2
- TXBCBTDQIULDIA-UHFFFAOYSA-N 2-[[3-hydroxy-2,2-bis(hydroxymethyl)propoxy]methyl]-2-(hydroxymethyl)propane-1,3-diol Chemical compound OCC(CO)(CO)COCC(CO)(CO)CO TXBCBTDQIULDIA-UHFFFAOYSA-N 0.000 description 1
- ZCYVEMRRCGMTRW-UHFFFAOYSA-N 7553-56-2 Chemical compound [I] ZCYVEMRRCGMTRW-UHFFFAOYSA-N 0.000 description 1
- 229920000298 Cellophane Polymers 0.000 description 1
- XDTMQSROBMDMFD-UHFFFAOYSA-N Cyclohexane Chemical compound C1CCCCC1 XDTMQSROBMDMFD-UHFFFAOYSA-N 0.000 description 1
- MBMLMWLHJBBADN-UHFFFAOYSA-N Ferrous sulfide Chemical compound [Fe]=S MBMLMWLHJBBADN-UHFFFAOYSA-N 0.000 description 1
- VHOQXEIFYTTXJU-UHFFFAOYSA-N Isobutylene-isoprene copolymer Chemical group CC(C)=C.CC(=C)C=C VHOQXEIFYTTXJU-UHFFFAOYSA-N 0.000 description 1
- NHTMVDHEPJAVLT-UHFFFAOYSA-N Isooctane Chemical compound CC(C)CC(C)(C)C NHTMVDHEPJAVLT-UHFFFAOYSA-N 0.000 description 1
- 229920000459 Nitrile rubber Polymers 0.000 description 1
- 239000004698 Polyethylene Substances 0.000 description 1
- 239000003377 acid catalyst Substances 0.000 description 1
- 239000000654 additive Substances 0.000 description 1
- 239000012790 adhesive layer Substances 0.000 description 1
- 150000001298 alcohols Chemical class 0.000 description 1
- 229910001860 alkaline earth metal hydroxide Inorganic materials 0.000 description 1
- 125000005907 alkyl ester group Chemical group 0.000 description 1
- 239000007864 aqueous solution Substances 0.000 description 1
- 239000003849 aromatic solvent Substances 0.000 description 1
- VSGNNIFQASZAOI-UHFFFAOYSA-L calcium acetate Chemical compound [Ca+2].CC([O-])=O.CC([O-])=O VSGNNIFQASZAOI-UHFFFAOYSA-L 0.000 description 1
- 239000001639 calcium acetate Substances 0.000 description 1
- 229960005147 calcium acetate Drugs 0.000 description 1
- 235000011092 calcium acetate Nutrition 0.000 description 1
- 229910000019 calcium carbonate Inorganic materials 0.000 description 1
- 229960003563 calcium carbonate Drugs 0.000 description 1
- 235000010216 calcium carbonate Nutrition 0.000 description 1
- AXCZMVOFGPJBDE-UHFFFAOYSA-L calcium dihydroxide Chemical compound [OH-].[OH-].[Ca+2] AXCZMVOFGPJBDE-UHFFFAOYSA-L 0.000 description 1
- 239000000920 calcium hydroxide Substances 0.000 description 1
- 229910001861 calcium hydroxide Inorganic materials 0.000 description 1
- BRPQOXSCLDDYGP-UHFFFAOYSA-N calcium oxide Chemical compound [O-2].[Ca+2] BRPQOXSCLDDYGP-UHFFFAOYSA-N 0.000 description 1
- 239000000292 calcium oxide Substances 0.000 description 1
- ODINCKMPIJJUCX-UHFFFAOYSA-N calcium oxide Inorganic materials [Ca]=O ODINCKMPIJJUCX-UHFFFAOYSA-N 0.000 description 1
- 229940087373 calcium oxide Drugs 0.000 description 1
- 235000012255 calcium oxide Nutrition 0.000 description 1
- 239000011248 coating agent Substances 0.000 description 1
- 238000000576 coating method Methods 0.000 description 1
- 229940105990 diglycerin Drugs 0.000 description 1
- GPLRAVKSCUXZTP-UHFFFAOYSA-N diglycerol Chemical compound OCC(O)COCC(O)CO GPLRAVKSCUXZTP-UHFFFAOYSA-N 0.000 description 1
- JVSWJIKNEAIKJW-UHFFFAOYSA-N dimethyl-hexane Natural products CCCCCC(C)C JVSWJIKNEAIKJW-UHFFFAOYSA-N 0.000 description 1
- 238000006073 displacement reaction Methods 0.000 description 1
- 238000001035 drying Methods 0.000 description 1
- BXKDSDJJOVIHMX-UHFFFAOYSA-N edrophonium chloride Chemical compound [Cl-].CC[N+](C)(C)C1=CC=CC(O)=C1 BXKDSDJJOVIHMX-UHFFFAOYSA-N 0.000 description 1
- 229920001971 elastomer Polymers 0.000 description 1
- 150000002314 glycerols Chemical class 0.000 description 1
- 150000004694 iodide salts Chemical class 0.000 description 1
- 239000011630 iodine Substances 0.000 description 1
- 229910052740 iodine Inorganic materials 0.000 description 1
- BQZGVMWPHXIKEQ-UHFFFAOYSA-L iron(ii) iodide Chemical compound [Fe+2].[I-].[I-] BQZGVMWPHXIKEQ-UHFFFAOYSA-L 0.000 description 1
- 150000002576 ketones Chemical class 0.000 description 1
- 239000010410 layer Substances 0.000 description 1
- UEGPKNKPLBYCNK-UHFFFAOYSA-L magnesium acetate Chemical compound [Mg+2].CC([O-])=O.CC([O-])=O UEGPKNKPLBYCNK-UHFFFAOYSA-L 0.000 description 1
- 239000011654 magnesium acetate Substances 0.000 description 1
- 229940069446 magnesium acetate Drugs 0.000 description 1
- 235000011285 magnesium acetate Nutrition 0.000 description 1
- 239000000395 magnesium oxide Substances 0.000 description 1
- CPLXHLVBOLITMK-UHFFFAOYSA-N magnesium oxide Inorganic materials [Mg]=O CPLXHLVBOLITMK-UHFFFAOYSA-N 0.000 description 1
- 229960000869 magnesium oxide Drugs 0.000 description 1
- 235000012245 magnesium oxide Nutrition 0.000 description 1
- AXZKOIWUVFPNLO-UHFFFAOYSA-N magnesium;oxygen(2-) Chemical compound [O-2].[Mg+2] AXZKOIWUVFPNLO-UHFFFAOYSA-N 0.000 description 1
- 229910052751 metal Inorganic materials 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 229910044991 metal oxide Inorganic materials 0.000 description 1
- 150000004706 metal oxides Chemical class 0.000 description 1
- SLCVBVWXLSEKPL-UHFFFAOYSA-N neopentyl glycol Chemical compound OCC(C)(C)CO SLCVBVWXLSEKPL-UHFFFAOYSA-N 0.000 description 1
- 230000003472 neutralizing effect Effects 0.000 description 1
- 229910052759 nickel Inorganic materials 0.000 description 1
- 239000003921 oil Substances 0.000 description 1
- 239000003960 organic solvent Substances 0.000 description 1
- 239000002985 plastic film Substances 0.000 description 1
- 229920006255 plastic film Polymers 0.000 description 1
- 229910052697 platinum Inorganic materials 0.000 description 1
- 229920002857 polybutadiene Polymers 0.000 description 1
- 229920000728 polyester Polymers 0.000 description 1
- 229920006267 polyester film Polymers 0.000 description 1
- 229920000573 polyethylene Polymers 0.000 description 1
- 229920001289 polyvinyl ether Polymers 0.000 description 1
- 239000000843 powder Substances 0.000 description 1
- 239000000047 product Substances 0.000 description 1
- 239000005060 rubber Substances 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 150000003464 sulfur compounds Chemical class 0.000 description 1
- 239000003784 tall oil Substances 0.000 description 1
- JOXIMZWYDAKGHI-UHFFFAOYSA-N toluene-4-sulfonic acid Chemical compound CC1=CC=C(S(O)(=O)=O)C=C1 JOXIMZWYDAKGHI-UHFFFAOYSA-N 0.000 description 1
- ZIBGPFATKBEMQZ-UHFFFAOYSA-N triethylene glycol Chemical compound OCCOCCOCCO ZIBGPFATKBEMQZ-UHFFFAOYSA-N 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
Landscapes
- Adhesives Or Adhesive Processes (AREA)
- Compositions Of Macromolecular Compounds (AREA)
Description
本発明は新規な感圧性接着剤に関する。さらに
詳しくは、特定の安定化されたロジンエステルを
タツキフアイヤーとして配合してなる感圧性接着
剤に関する。
従来より、ロジンエステルは感圧性接着剤など
のタツキフアイヤーとして使用されているが、高
軟化点となりにくかつたり、耐熱性、耐老化性に
難点があり、これが感圧性接着剤の性質に悪影響
を及ぼし、満足しうる感圧性接着剤はえられがた
いという問題があつた。このためかかる性質を改
良した不均化ロジンエステルまたは水添ロジンエ
ステルが市販されているが、いずれも満足できる
ほどに高軟化点でかつ耐熱性、耐老化性に優れた
ロジンエステルとはいいえないものである。
そこで本発明者らはまず感圧性接着剤用のタツ
キフアイヤーとしてすぐれた安定化された高軟化
点ロジンエステルを見出すべく鋭意検討を行なつ
た。
まずロジンエステルの原料であるロジンにはそ
の過酸化物に起因すると思われる高分子量物ある
いは不ケン化物などが含まれており、これが最終
生成物である各種ロジンエステルに悪影響を及ぼ
すものと推察し、精製により該高分子量物、不ケ
ン化物などを除去したロジンを多価アルコールで
エステル化することを試みた。しかしながら、こ
のようにしてえられたロジンエステルは感圧性接
着剤用タツキフアイヤーとして要求されるほどに
は安定化されたものではなかつた。そこでまず原
料ロジンを不均化して不均化ロジンとし、ついで
この不均化ロジンを精製して高分子量物、不ケン
化物などを除去し、かくしてえられた精製不均化
ロジンを多価アルコールでエステル化したとこ
ろ、充分に安定化された高軟化点ロジンエステル
がえられることを見出した。
本発明者らはこの事実にもとづいてさらに研究
を重ねた結果、前記のごとき安定化された高軟化
点ロジンエステルを感圧性接着剤のタツキフアイ
ヤーとして用いるときは、すぐれた接着性、粘着
性、耐熱性および耐老化性を有する感圧性接着剤
がえられるという新たな事実を見出し、本発明を
完成するにいたつた。
すなわち本発明は、天然ゴムまたは合成ゴムと
タツキフアイヤーを主成分とする感圧性接着剤に
おいて、該タツキフアイヤーが精製された不均化
ロジンを3価以上の多価アルコールでエステル化
してえられた、軟化点が65〜140℃のロジンエス
テルであることを特徴とする感圧性接着剤に関す
る。
本発明に用いる安定化された高軟化点ロジンエ
ステルは分子量が小さいにもかかわらず、今まで
にない高軟化点ロジンエステルであり、この高軟
化点の性質を利用して感圧性接着剤用タツキフア
イヤーとして使用すると卓効を奏することが判明
した。
かかる顕著な性質を有するロジンエステルは本
発明における、不均化ロジンを精製して高分子量
物、不ケン化物などを実質的に除去した精製不均
化ロジンを用い、これを特定の多価アルコールで
エステル化することによつてはじめてえられるも
のである。すなわち、不均化ロジンを精製した精
製不均化ロジンと不均化ロジンをなんら精製しな
い未精製不均化ロジンを用い、これらを同一条件
でグリセリンと反応させてえられた2種のロジン
グリセリンエステル(後記参考例1および4でえ
られたもの)について、それらの重量平均分子量
および軟化点を測定したところ、第1表に示すご
とき差が生じた。第1表から明らかなごとく、精
製不均化ロジンからえられたロジングリセリンエ
ステル(参考例1)は未精製不均化ロジンからえ
られたロジングリセリンエステル(参考例4)に
くらべて重量平均分子量が129も小さいにもかか
わらず、軟化点は16℃も高くなつている。さらに
前記各ロジングリセリンエステルをタツキフアイ
ヤーとして天然ゴムと重量比で45:55となるよう
に混合して感圧性接着剤をえ、それらについて粘
着性、凝集力および接着力を測定したところ第1
表に示すごとき差が生じた。
The present invention relates to a new pressure sensitive adhesive. More specifically, the present invention relates to a pressure-sensitive adhesive containing a specific stabilized rosin ester as a tackifier. Traditionally, rosin ester has been used as a tackifier for pressure-sensitive adhesives, etc., but it is difficult to reach a high softening point and has problems with heat resistance and aging resistance, which affect the properties of pressure-sensitive adhesives. There was a problem that it was difficult to find a satisfactory pressure-sensitive adhesive due to the adverse effects. For this reason, disproportionated rosin esters or hydrogenated rosin esters with improved properties are commercially available, but neither can be said to be a rosin ester with a satisfactorily high softening point and excellent heat resistance and aging resistance. It is something. Therefore, the present inventors first conducted intensive studies to find a stabilized high softening point rosin ester that is excellent as a tackifier for pressure-sensitive adhesives. First of all, rosin, which is the raw material for rosin esters, contains high molecular weight substances or unsaponifiable substances that are thought to be caused by peroxides, and it is assumed that these have a negative effect on the various rosin esters that are the final products. An attempt was made to esterify rosin, which had been purified to remove high molecular weight substances, unsaponifiable substances, etc., with a polyhydric alcohol. However, the rosin ester thus obtained was not stabilized to the extent required as a tackifier for pressure-sensitive adhesives. Therefore, first, the raw material rosin is disproportionated to obtain a disproportionated rosin, and then this disproportionated rosin is purified to remove high molecular weight substances, unsaponifiable substances, etc., and the purified disproportionated rosin thus obtained is converted into a polyhydric alcohol. It has been found that a sufficiently stabilized high softening point rosin ester can be obtained by esterification with. As a result of further research based on this fact, the present inventors found that when the above-mentioned stabilized high softening point rosin ester is used as a tackifier for pressure-sensitive adhesives, it has excellent adhesion and tackiness. The present invention was completed based on the new discovery that a pressure-sensitive adhesive having heat resistance and aging resistance can be obtained. That is, the present invention provides a pressure-sensitive adhesive mainly composed of natural rubber or synthetic rubber and tackifier, which is obtained by esterifying a purified disproportionated rosin with a trihydric or higher polyhydric alcohol. The present invention relates to a pressure-sensitive adhesive characterized by being a rosin ester having a softening point of 65 to 140°C. Although the stabilized high softening point rosin ester used in the present invention has a small molecular weight, it is an unprecedented high softening point rosin ester. It was found that it was very effective when used as a fire ring. Rosin esters having such remarkable properties are obtained by using purified disproportionated rosin obtained by refining disproportionated rosin to substantially remove high molecular weight substances, unsaponifiable substances, etc., and adding it to a specific polyhydric alcohol. It can only be obtained by esterification with That is, two types of rosin glycerin were obtained by using purified disproportionated rosin obtained by refining disproportionated rosin and unrefined disproportionated rosin in which disproportionated rosin was not purified in any way, and reacting them with glycerin under the same conditions. When the weight average molecular weight and softening point of the esters (obtained in Reference Examples 1 and 4 described later) were measured, differences as shown in Table 1 were found. As is clear from Table 1, the rosin glycerin ester obtained from purified disproportionated rosin (Reference Example 1) has a weight average molecular weight compared to the rosin glycerin ester obtained from unrefined disproportionated rosin (Reference Example 4). Even though the temperature is 129 lower, the softening point is 16°C higher. Furthermore, each of the above-mentioned rosin glycerin esters was mixed with natural rubber as a tackifier at a weight ratio of 45:55 to prepare a pressure-sensitive adhesive, and the tackiness, cohesive force, and adhesive force of these were measured.
There were differences as shown in the table.
【表】
第1表より明らかなごとく、感圧性接着剤の粘
着性および接着力を比較するに、精製不均化ロジ
ンからえられたロジングリセリンエステル(参考
例1)を使用したものが未精製不均化ロジンから
えられたロジングリセリンエステル(参考例4)
を使用したものにくらべ5割も高い接着力を有し
ている。一方粘着性では両者にほとんど差がな
く、いずれも非常に良好な値を示している。
本発明に用いるロジングリセリンエステルが高
軟化点を有しているにもかかわらず、これを用い
た感圧性接着剤が高粘着性および高接着力を共に
有することはきわめて驚ろくべきことである。な
んとなれば通常同系統のタツキフアイヤーにおい
ては軟化点を上げれば接着力は増すが、粘着性は
低下するというのが一般常識であるからである。
さらに本発明に用いるロジンエステルは顕著に
安定化されたものであつて耐熱性および耐老化性
にすぐれており、これをタツキフアイヤーとして
配合した感圧性接着剤は前記のごときすぐれた接
着力および粘着性が長期間維持されうる。
つぎに本発明に用いる安定化されたロジンエス
テルの製造法について詳述する。
本発明に用いる安定化されたロジンエステルは
精製された不均化ロジンを多価アルコールとエス
テル化することにより製造される。
前記の精製された不均化ロジンはロジンを不均
化反応したのち精製することにより容易に製造で
きる。
まずロジンを通常の方法で不均化反応して不均
化ロジンをうる。たとえばロジンを不均化触媒の
存在下に100〜300℃、好しくは150〜290℃で加熱
する。不均化触媒はロジンに対し0.01〜5%(重
量%、以下同様)、好しくは0.1〜1%使用すれば
よい。不均化触媒としてはパラジウムカーボン、
ニツケル、白金などの金属粉末、ヨウ素、ヨウ化
鉄などのヨウ化物、二酸化硫黄、硫化鉄などの硫
黄化合物などがあげられる。原料ロジンとしては
ガムロジン、ウツドロジン、トール油ロジンがあ
げられる。
本発明でいう精製とは前記のごとくしてえられ
た不均化ロジンから、原料ロジン中に含まれてい
た過酸化物から生起したと考えられる高分子量
物、および原料ロジン中にもともと存在していた
不ケン化物ならびに不均化反応中に生じた不ケン
化物を除くことを意味する。本発明に用いる精製
不均化ロジンは不均化ロジン中の高分子量物、不
ケン化物を取り除いた酸価が177以上のものが好
ましい。
前記精製は蒸留、結晶化などの通常の方法で行
うことができる。蒸留は通常の条件ですることが
でき、たとえば3mmHgの減圧下で釜温度210〜
300℃で留出する留分をとる。210℃より低い釜温
度で留出する留分は不ケン化物を含み、一方300
℃より高い釜温度で留出する留分は着色が激し
い。結晶化による精製はたとえば前記不均化ロジ
ンを良溶媒に溶解し、ついで溶媒を留去して濃厚
な溶液となし、この溶液に貧溶媒を加えることに
よつて行うことができる。良溶媒としてはベンゼ
ン、トルエン、キシレン、クロロホルム、低級ア
ルコール、アセトンなどのケトン類、酢酸エチル
などの酢酸低級アルキルエステル類などがあげら
れ、貧溶媒としてはn−ヘキサン、n−ヘプタ
ン、シクロヘキサン、イソオクタンなどがあげら
れる。さらに前記精製は前記不均化反応でえられ
た不均化ロジンをアルカリ水を用いてアルカリ水
溶液となし、不溶性の不ケン化物を有機溶媒によ
り抽出したのち水層を中和して精製不均化ロジン
をうることによつてもできる。
前記精製法のなかでは経済的観点からすれば蒸
留法が最も好ましい。
本発明において、精製された不均化ロジンをう
るには前記のごとく不均化ロジンに対して精製を
施すのが好ましい。それは精製後不均化反応を行
なうと、不均化反応中に不ケン化物が生じ、これ
が最終製品としてのロジンエステルの性質に悪影
響を及ぼすからである。
前記のごとく精製されたロジンエステルはつい
で3価以上の多価アルコールとエステル化されて
最終製品としてのロジンエステルがえられる。
精製不均化ロジンと多価アルコールとのエステ
ル化は通常の方法で行なうことができる。たとえ
ば精製不均化ロジンと3価以上の多価アルコール
とを密閉容器中または開放容器中で触媒の存在下
または不存在下に溶媒の存在下または不存在下に
80〜300℃で加熱することによつて行うことがで
きる。溶媒としてはベンゼン、トルエン、キシレ
ンなどの芳香族系溶媒が使用できる。触媒として
は硫酸、酢酸、パラトルエンスルホン酸などの酸
触媒、水酸化カルシウムなどのアルカリ土類金属
の水酸化物、酸化マグネシウム、酸化カルシウム
などの金属酸化物、炭酸カルシウム、酢酸マグネ
シウム、酢酸カルシウムなどの通常のエステル化
触媒が使用できる。
本発明で用いる3価以上の多価アルコールとし
ては、グリセリン、ジグリセリン、ペンタエリス
リトール、ジペンタエリスリトールなどがあげら
れ、とくにグリセリンおよびペンタエリスリトー
ルが好ましい。なおえられるロジンエステルに悪
影響を与えない範囲内で前記以外の多価アルコー
ルを併用することができる。かかる多価アルコー
ルとしては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、ネオペンチル
グリコールなどがあげられる。
本発明に用いるロジンエステルは軟化点が65〜
140℃、好ましくは90〜140℃であり、さらに酸価
20以下、重量平均分子量700〜1100のものが好ま
しい。
本発明の感圧性接着剤は前記のごとくしてえら
れた安定化された高軟化点ロジンエステルをタツ
キフアイヤーとして天然ゴムまたは合成ゴムに配
合したものである。本発明の感圧性接着剤はすぐ
れた接着力および粘着性ならびに耐熱性および耐
老化性を有する。
前記合成ゴムとしては、ランダムSBR、ブロツ
クSBR、ポリスチレン−ポリイソプレン−ポリス
チレンブロツク共重合体、ニトリルゴム、ポリブ
タジエンゴム、イソプレン−イソブチレンゴム、
ポリビニルエーテルなどがあげられる。
天然ゴムまたは合成ゴムとタツキフアイヤーと
の配合割合は、天然ゴムまたは合成ゴム100重量
部に対しタツキフアイヤー20〜150重量部とすれ
ばよい。本発明の感圧性接着剤には前記主成分以
外に感圧性接着剤に用いられる通常の添加剤を配
合してもよい。
本発明の感圧性接着剤をミキシングロールによ
り混合し、そのまま加熱溶融して基材に塗布し、
ついでカレンダーロールにかけるか、または溶剤
を用いて溶剤溶液とし、これをスプレツダー、ア
ブリケーターなどで基材にコーテイングして加熱
乾燥することによつて感圧性接着フイルムがえら
れる。基材としてはセロフアン、紙、ポリエステ
ルなどのプラステイツクフイルムなどがあげられ
る。
つぎに参考例、実施例および比較例をあげて本
発明の感圧性接着剤を説明する。なお参考例1〜
3は本発明に用いるロジンエステルの製造法を示
すものであり、参考例4〜6は参考用のロジンエ
ステルの製造法を示すものである。
参考例 1
(1) 不均化反応
酸価170、軟化点74℃の中国産ガムロジン100
gに触媒として5%パラジウムカーボンを0.03
g加え、チツ素シール下にて280℃で4時間撹
拌して不均化反応を行ない、酸価158、軟化点
75℃、色調ガードナー10の不均化ロジン95gを
えた。
(2) 精 製
前記不均化ロジンをチツ素シール下にて3mm
Hgの減圧下で蒸留し、えられた主留を精製不
均化ロジンとした。[Table] As is clear from Table 1, when comparing the tackiness and adhesive strength of pressure-sensitive adhesives, the one using rosin glycerin ester (Reference Example 1) obtained from purified disproportionated rosin was superior to the one using unpurified rosin. Rosin glycerin ester obtained from disproportionated rosin (Reference example 4)
It has 50% higher adhesion strength than those using . On the other hand, there is almost no difference in adhesiveness between the two, and both exhibit very good values. Although the rosin glycerin ester used in the present invention has a high softening point, it is quite surprising that a pressure sensitive adhesive using the same has both high tack and high adhesive strength. This is because it is common knowledge that for similar types of tatsukifires, raising the softening point will increase the adhesive strength, but will decrease the tackiness. Furthermore, the rosin ester used in the present invention is significantly stabilized and has excellent heat resistance and aging resistance, and pressure-sensitive adhesives containing this as a tackifier have excellent adhesive strength and Adhesion can be maintained for a long time. Next, the method for producing the stabilized rosin ester used in the present invention will be described in detail. The stabilized rosin ester used in the present invention is produced by esterifying purified disproportionated rosin with a polyhydric alcohol. The above-mentioned purified disproportionated rosin can be easily produced by subjecting rosin to a disproportionation reaction and then purifying it. First, rosin is subjected to a disproportionation reaction in a conventional manner to obtain a disproportionated rosin. For example, rosin is heated at 100-300°C, preferably 150-290°C in the presence of a disproportionation catalyst. The disproportionation catalyst may be used in an amount of 0.01 to 5% (by weight, hereinafter the same), preferably 0.1 to 1%, based on the rosin. Palladium carbon as a disproportionation catalyst,
Examples include metal powders such as nickel and platinum, iodides such as iodine and iron iodide, and sulfur compounds such as sulfur dioxide and iron sulfide. Examples of raw material rosin include gum rosin, oil rosin, and tall oil rosin. In the present invention, purification refers to high molecular weight substances that are thought to have arisen from peroxides contained in the raw material rosin, as well as high molecular weight substances that are thought to have arisen from the peroxides contained in the raw material rosin, from the disproportionated rosin obtained as described above. This means removing unsaponifiable substances that were present during the disproportionation reaction as well as unsaponifiable substances that were generated during the disproportionation reaction. The purified disproportionated rosin used in the present invention preferably has an acid value of 177 or more after removing high molecular weight substances and unsaponifiable substances from the disproportionated rosin. The purification can be carried out by conventional methods such as distillation and crystallization. Distillation can be carried out under normal conditions, for example under a reduced pressure of 3 mmHg and at a kettle temperature of 210 -
Take the fraction distilled out at 300℃. Fractions distilled at kettle temperatures lower than 210°C contain unsaponifiables, whereas 300°C
The fraction distilled at a pot temperature higher than ℃ is intensely colored. Purification by crystallization can be carried out, for example, by dissolving the disproportionated rosin in a good solvent, then distilling off the solvent to form a concentrated solution, and adding a poor solvent to this solution. Good solvents include benzene, toluene, xylene, chloroform, lower alcohols, ketones such as acetone, and acetic acid lower alkyl esters such as ethyl acetate. Poor solvents include n-hexane, n-heptane, cyclohexane, and isooctane. etc. can be mentioned. Furthermore, the purification process involves converting the disproportionated rosin obtained in the disproportionation reaction into an alkaline aqueous solution using alkaline water, extracting insoluble unsaponifiable substances with an organic solvent, and then neutralizing the aqueous layer to purify the disproportionated rosin. It can also be obtained by obtaining chemically modified rosin. Among the purification methods mentioned above, the distillation method is the most preferred from an economic point of view. In the present invention, in order to obtain purified disproportionated rosin, it is preferable to subject the disproportionated rosin to purification as described above. This is because if a disproportionation reaction is carried out after purification, unsaponifiable substances are produced during the disproportionation reaction, which adversely affects the properties of the rosin ester as a final product. The rosin ester purified as described above is then esterified with a trihydric or higher polyhydric alcohol to obtain a rosin ester as a final product. Esterification of purified disproportionated rosin and polyhydric alcohol can be carried out by a conventional method. For example, a purified disproportionated rosin and a trivalent or higher polyhydric alcohol are mixed in a closed container or an open container in the presence or absence of a catalyst and in the presence or absence of a solvent.
This can be done by heating at 80 to 300°C. As the solvent, aromatic solvents such as benzene, toluene, and xylene can be used. Catalysts include acid catalysts such as sulfuric acid, acetic acid, and paratoluenesulfonic acid, alkaline earth metal hydroxides such as calcium hydroxide, metal oxides such as magnesium oxide and calcium oxide, calcium carbonate, magnesium acetate, and calcium acetate. Any conventional esterification catalyst can be used. Examples of the trihydric or higher polyhydric alcohol used in the present invention include glycerin, diglycerin, pentaerythritol, dipentaerythritol, and the like, with glycerin and pentaerythritol being particularly preferred. Furthermore, polyhydric alcohols other than those mentioned above may be used in combination within a range that does not adversely affect the resulting rosin ester. Examples of such polyhydric alcohols include ethylene glycol, diethylene glycol, triethylene glycol, and neopentyl glycol. The rosin ester used in the present invention has a softening point of 65~
140℃, preferably 90-140℃, and further acid value
20 or less, preferably a weight average molecular weight of 700 to 1100. The pressure-sensitive adhesive of the present invention is one in which the stabilized high softening point rosin ester obtained as described above is blended with natural rubber or synthetic rubber as a tackifier. The pressure sensitive adhesive of the present invention has excellent adhesion and tack as well as heat and aging resistance. Examples of the synthetic rubber include random SBR, block SBR, polystyrene-polyisoprene-polystyrene block copolymer, nitrile rubber, polybutadiene rubber, isoprene-isobutylene rubber,
Examples include polyvinyl ether. The mixing ratio of natural rubber or synthetic rubber and tackifier may be 20 to 150 parts by weight per 100 parts by weight of natural rubber or synthetic rubber. In addition to the above-mentioned main components, the pressure-sensitive adhesive of the present invention may contain additives commonly used in pressure-sensitive adhesives. The pressure sensitive adhesive of the present invention is mixed with a mixing roll, heated and melted as it is, and applied to a base material,
Then, a pressure-sensitive adhesive film can be obtained by applying the mixture to a calender roll or using a solvent to form a solvent solution, coating the base material with a spreader, an ablator, etc., and drying by heating. Examples of the base material include cellophane, paper, and plastic film such as polyester. Next, the pressure-sensitive adhesive of the present invention will be described with reference to Reference Examples, Examples, and Comparative Examples. Reference example 1~
3 shows a method for producing a rosin ester used in the present invention, and Reference Examples 4 to 6 show a method for producing a rosin ester for reference. Reference example 1 (1) Disproportionation reaction Chinese gum rosin 100 with acid value 170 and softening point 74℃
0.03 g of 5% palladium carbon as a catalyst
g, and stirred at 280℃ for 4 hours under a nitrogen seal to perform a disproportionation reaction, resulting in an acid value of 158 and a softening point.
95 g of disproportionated rosin of color Gardner 10 was obtained at 75°C. (2) Purification The disproportionated rosin was purified to 3 mm under a nitrogen seal.
It was distilled under reduced pressure of Hg, and the obtained main distillate was used as purified disproportionated rosin.
(a) 粘着性(ローリングボール法に準ずる)
PSTC−6の装置を使用して角度21.5゜の傾
斜板上の底辺より10cmの位置から直径15mmの鋼
球をころがし、底辺に設置したポリエステルフ
イルムの接着面上での鋼球のころがり距離を測
定した。
(b) 凝集力(剪断破壊テスト)
接着フイルムと、研摩紙で処理し充分に清浄
にしたステンレス板とを25mm×25mmの面積でラ
ツプ付けし、重さ1Kgのローラーで2回圧着さ
せ、40℃で500gの荷重をかけ、30分後のずれ
を測定した(値が小さいほどよい)。
(c) 接着力
幅1インチの接着フイルムを、研摩紙で処理
し充分に清浄にしたステンレス板に重さ1Kgの
ローラを用いて2回圧着させ、20℃、65%RH
中で12時間調温、調湿後テンシロン型万能引張
試験機を用いて引調速度300mm/分で180゜剥離
強度を測定した(値が大きいほどよい)。
(d) 耐老化試験
接着フイルムを70℃の循風乾燥機中に24時間
放置して接着剤を温風により劣化させ、前記の
試験方法と同様にして粘着性および凝集力を測
定した。ただし、凝集力測定に際し、荷重は
200gとした。
前記試験結果を第2表に示す。
(a) Adhesiveness (similar to rolling ball method) Using a PSTC-6 device, roll a steel ball with a diameter of 15 mm from a position 10 cm from the bottom of an inclined plate at an angle of 21.5°, and then The rolling distance of the steel ball on the adhesive surface was measured. (b) Cohesive force (shear failure test) The adhesive film and a stainless steel plate treated with abrasive paper and thoroughly cleaned were wrapped in an area of 25 mm x 25 mm, and pressed twice with a roller weighing 1 kg, A load of 500 g was applied at °C, and the deviation was measured after 30 minutes (the smaller the value, the better). (c) Adhesive strength A 1 inch wide adhesive film was pressed twice onto a stainless steel plate treated with abrasive paper and thoroughly cleaned using a roller weighing 1 kg, at 20°C and 65% RH.
After adjusting the temperature and humidity for 12 hours in the chamber, the 180° peel strength was measured using a Tensilon type universal tensile tester at a adjusting speed of 300 mm/min (the larger the value, the better). (d) Aging resistance test The adhesive film was left in a circulating air dryer at 70° C. for 24 hours to deteriorate the adhesive with hot air, and the tackiness and cohesive force were measured in the same manner as the test method described above. However, when measuring cohesion, the load is
The weight was 200g. The test results are shown in Table 2.
【表】
第2表から明らかなごとく、精製不均化ロジン
からえられたロジンエステル(参考例1〜3)を
用いる実施例1〜3の感圧性接着剤は未精製の不
均化ロジンからえられたロジンエステル(参考例
4〜5)および精製ロジンから不均化工程を省略
してえられたロジンエステル(参考例6)を使用
した比較例1〜3の感圧性接着剤よりも接着力が
すぐれ、かつ老化後の凝集力および粘着性もすぐ
れている。
実施例4〜6および比較例4〜5
ポリスチレン−ポリイソプレン−ポリスチレン
ブロツク共重合体(クレイトン1107、シエル化学
社製)を参考例1〜3および参考例4〜5でえた
各ロジンエステルと重量比で50:40となるように
混合し、各混合物をトルエンにそれぞれ溶解し、
固形分濃度40%の5種の溶液を調製した。ついで
これらの溶液をそれぞれ1インチ巾のサイコロ型
アプリケーターを用いてポリエステルフイルム
(厚さ38μ)に塗布し、50mmHg下にて50℃で1
時間減圧乾燥して厚さ50μの接着剤層を形成し
た。
えられた5種の接着フイルムについて実施例1
〜3と同様にして粘着性、凝集力および接着力を
測定した。なお接着力試験においてはステンレス
板に対する接着力に加えてポリエチレン板(厚さ
2mm)に対する接着力も測定した。
凝集力試験では,いずれの接着フイルムのばあ
いもずれが生じず、荷重を2倍にしても同様であ
つた。
粘着性試験および接着力試験の結果を第3表に
示す。[Table] As is clear from Table 2, the pressure sensitive adhesives of Examples 1 to 3 using rosin esters (Reference Examples 1 to 3) obtained from purified disproportionated rosin were obtained from unrefined disproportionated rosin. Adhesion was higher than that of the pressure-sensitive adhesives of Comparative Examples 1 to 3 using the obtained rosin ester (Reference Examples 4 to 5) and the rosin ester obtained by omitting the disproportionation step from purified rosin (Reference Example 6). It has excellent strength, and also has excellent cohesive strength and adhesion after aging. Examples 4 to 6 and Comparative Examples 4 to 5 Weight ratio of polystyrene-polyisoprene-polystyrene block copolymer (Krayton 1107, manufactured by Shell Chemical Co., Ltd.) to each rosin ester obtained in Reference Examples 1 to 3 and Reference Examples 4 to 5 Mix at a ratio of 50:40, dissolve each mixture in toluene,
Five types of solutions with a solid content concentration of 40% were prepared. Next, each of these solutions was applied to a polyester film (thickness: 38μ) using a 1-inch-wide dice-shaped applicator, and incubated at 50°C under 50mmHg.
It was dried under reduced pressure for hours to form an adhesive layer with a thickness of 50 μm. Example 1 about the five types of adhesive films obtained
The tackiness, cohesive force and adhesive force were measured in the same manner as in 3. In the adhesion test, in addition to the adhesion force to a stainless steel plate, the adhesion force to a polyethylene plate (thickness 2 mm) was also measured. In the cohesive force test, no displacement occurred in any of the adhesive films, and the same was true even when the load was doubled. The results of the tack test and adhesion test are shown in Table 3.
Claims (1)
を主成分とする感圧性接着剤において、該タツキ
フアイヤーが、精製された不均化ロジンを3価以
上の多価アルコールでエステル化してえられた、
軟化点が65〜140℃のロジンエステルであること
を特徴とする感圧性接着剤。 2 精製された不均化ロジンが不均化ロジンを蒸
留してえられたものである特許請求の範囲第1項
記載の感圧性接着剤。 3 ロジンエステルの使用量が天然ゴムまたは合
成ゴムの100重量部に対して20〜150重量部である
特許請求の範囲第1項記載の感圧性接着剤。[Scope of Claims] 1. A pressure-sensitive adhesive whose main components are natural rubber or synthetic rubber and tackifier, in which the tackifier is made by esterifying purified disproportionated rosin with a trivalent or higher polyhydric alcohol. I was able to transform into
A pressure-sensitive adhesive characterized by being a rosin ester with a softening point of 65 to 140°C. 2. The pressure-sensitive adhesive according to claim 1, wherein the purified disproportionated rosin is obtained by distilling disproportionated rosin. 3. The pressure-sensitive adhesive according to claim 1, wherein the amount of rosin ester used is 20 to 150 parts by weight per 100 parts by weight of natural rubber or synthetic rubber.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP10832079A JPS5554373A (en) | 1979-08-25 | 1979-08-25 | Pressure-sensitive adhesive |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP10832079A JPS5554373A (en) | 1979-08-25 | 1979-08-25 | Pressure-sensitive adhesive |
Related Parent Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP7672578A Division JPS559605A (en) | 1978-06-23 | 1978-06-23 | Preparation of rosin ester having high softening point and improved stability |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS5554373A JPS5554373A (en) | 1980-04-21 |
| JPS6146024B2 true JPS6146024B2 (en) | 1986-10-11 |
Family
ID=14481714
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP10832079A Granted JPS5554373A (en) | 1979-08-25 | 1979-08-25 | Pressure-sensitive adhesive |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS5554373A (en) |
Families Citing this family (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS6084371A (en) * | 1983-10-17 | 1985-05-13 | Toagosei Chem Ind Co Ltd | Aqueous emulsion type adhesive composition |
| JPS61238877A (en) * | 1985-04-15 | 1986-10-24 | Harima Kasei Kogyo Kk | rewet adhesive |
| JPWO2006109441A1 (en) * | 2005-03-30 | 2008-10-16 | 荒川化学工業株式会社 | Tackifier and tackifier resin emulsion |
| TWI731094B (en) * | 2016-06-16 | 2021-06-21 | 日商荒川化學工業股份有限公司 | Tackifying resin, tackifying resin emulsion, water-based adhesive composition, polychloroprene latex-based adhesive composition |
-
1979
- 1979-08-25 JP JP10832079A patent/JPS5554373A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS5554373A (en) | 1980-04-21 |
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