JPS6121979B2 - - Google Patents
Info
- Publication number
- JPS6121979B2 JPS6121979B2 JP19247583A JP19247583A JPS6121979B2 JP S6121979 B2 JPS6121979 B2 JP S6121979B2 JP 19247583 A JP19247583 A JP 19247583A JP 19247583 A JP19247583 A JP 19247583A JP S6121979 B2 JPS6121979 B2 JP S6121979B2
- Authority
- JP
- Japan
- Prior art keywords
- starch
- adhesive
- weight
- viscosity
- acid
- 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
- 230000001070 adhesive effect Effects 0.000 claims description 63
- 239000000853 adhesive Substances 0.000 claims description 62
- 229920002472 Starch Polymers 0.000 claims description 58
- 235000019698 starch Nutrition 0.000 claims description 58
- 239000008107 starch Substances 0.000 claims description 56
- 229920000856 Amylose Polymers 0.000 claims description 27
- 229920002261 Corn starch Polymers 0.000 claims description 21
- 239000008120 corn starch Substances 0.000 claims description 21
- 238000004519 manufacturing process Methods 0.000 claims description 17
- 239000002253 acid Substances 0.000 claims description 14
- 238000006467 substitution reaction Methods 0.000 claims description 5
- 230000032050 esterification Effects 0.000 claims description 3
- 238000005886 esterification reaction Methods 0.000 claims description 3
- 239000004480 active ingredient Substances 0.000 claims description 2
- 239000007900 aqueous suspension Substances 0.000 claims description 2
- 238000006266 etherification reaction Methods 0.000 claims description 2
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 27
- 238000010438 heat treatment Methods 0.000 description 20
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 14
- 238000003475 lamination Methods 0.000 description 12
- 238000000034 method Methods 0.000 description 11
- 239000011111 cardboard Substances 0.000 description 10
- 235000011121 sodium hydroxide Nutrition 0.000 description 9
- QTBSBXVTEAMEQO-UHFFFAOYSA-N Acetic acid Chemical compound CC(O)=O QTBSBXVTEAMEQO-UHFFFAOYSA-N 0.000 description 8
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 description 8
- 239000000123 paper Substances 0.000 description 8
- 239000000725 suspension Substances 0.000 description 8
- 230000032683 aging Effects 0.000 description 7
- 239000002585 base Substances 0.000 description 7
- 239000003292 glue Substances 0.000 description 6
- 239000007788 liquid Substances 0.000 description 6
- 239000007787 solid Substances 0.000 description 6
- RTZKZFJDLAIYFH-UHFFFAOYSA-N Diethyl ether Chemical compound CCOCC RTZKZFJDLAIYFH-UHFFFAOYSA-N 0.000 description 5
- 239000007864 aqueous solution Substances 0.000 description 4
- 239000001341 hydroxy propyl starch Substances 0.000 description 4
- -1 hydroxypropyl Chemical group 0.000 description 4
- 235000013828 hydroxypropyl starch Nutrition 0.000 description 4
- 239000000243 solution Substances 0.000 description 4
- WFDIJRYMOXRFFG-UHFFFAOYSA-N Acetic anhydride Chemical compound CC(=O)OC(C)=O WFDIJRYMOXRFFG-UHFFFAOYSA-N 0.000 description 3
- MUBZPKHOEPUJKR-UHFFFAOYSA-N Oxalic acid Chemical compound OC(=O)C(O)=O MUBZPKHOEPUJKR-UHFFFAOYSA-N 0.000 description 3
- 229910021538 borax Inorganic materials 0.000 description 3
- 238000001816 cooling Methods 0.000 description 3
- 238000010030 laminating Methods 0.000 description 3
- 239000000203 mixture Substances 0.000 description 3
- 239000002994 raw material Substances 0.000 description 3
- 239000004328 sodium tetraborate Substances 0.000 description 3
- 235000010339 sodium tetraborate Nutrition 0.000 description 3
- 238000007711 solidification Methods 0.000 description 3
- 230000008023 solidification Effects 0.000 description 3
- FERIUCNNQQJTOY-UHFFFAOYSA-N Butyric acid Chemical compound CCCC(O)=O FERIUCNNQQJTOY-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
- FAPWRFPIFSIZLT-UHFFFAOYSA-M Sodium chloride Chemical compound [Na+].[Cl-] FAPWRFPIFSIZLT-UHFFFAOYSA-M 0.000 description 2
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 description 2
- 238000010306 acid treatment Methods 0.000 description 2
- 238000004026 adhesive bonding Methods 0.000 description 2
- 239000003513 alkali Substances 0.000 description 2
- 238000006243 chemical reaction Methods 0.000 description 2
- 239000004927 clay Substances 0.000 description 2
- XBDQKXXYIPTUBI-UHFFFAOYSA-N dimethylselenoniopropionate Natural products CCC(O)=O XBDQKXXYIPTUBI-UHFFFAOYSA-N 0.000 description 2
- 238000001035 drying Methods 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 239000008187 granular material Substances 0.000 description 2
- 150000007524 organic acids Chemical class 0.000 description 2
- 235000005985 organic acids Nutrition 0.000 description 2
- XNGIFLGASWRNHJ-UHFFFAOYSA-N phthalic acid Chemical compound OC(=O)C1=CC=CC=C1C(O)=O XNGIFLGASWRNHJ-UHFFFAOYSA-N 0.000 description 2
- 238000003756 stirring Methods 0.000 description 2
- 125000001424 substituent group Chemical group 0.000 description 2
- 238000005406 washing Methods 0.000 description 2
- GXVUZYLYWKWJIM-UHFFFAOYSA-N 2-(2-aminoethoxy)ethanamine Chemical compound NCCOCCN GXVUZYLYWKWJIM-UHFFFAOYSA-N 0.000 description 1
- GAWIXWVDTYZWAW-UHFFFAOYSA-N C[CH]O Chemical group C[CH]O GAWIXWVDTYZWAW-UHFFFAOYSA-N 0.000 description 1
- ZAMOUSCENKQFHK-UHFFFAOYSA-N Chlorine atom Chemical compound [Cl] ZAMOUSCENKQFHK-UHFFFAOYSA-N 0.000 description 1
- BRLQWZUYTZBJKN-UHFFFAOYSA-N Epichlorohydrin Chemical compound ClCC1CO1 BRLQWZUYTZBJKN-UHFFFAOYSA-N 0.000 description 1
- 229920000881 Modified starch Polymers 0.000 description 1
- 239000004368 Modified starch Substances 0.000 description 1
- OFOBLEOULBTSOW-UHFFFAOYSA-N Propanedioic acid Natural products OC(=O)CC(O)=O OFOBLEOULBTSOW-UHFFFAOYSA-N 0.000 description 1
- GOOHAUXETOMSMM-UHFFFAOYSA-N Propylene oxide Chemical compound CC1CO1 GOOHAUXETOMSMM-UHFFFAOYSA-N 0.000 description 1
- 239000005708 Sodium hypochlorite Substances 0.000 description 1
- MKRNVBXERAPZOP-UHFFFAOYSA-N Starch acetate Chemical compound O1C(CO)C(OC)C(O)C(O)C1OCC1C(OC2C(C(O)C(OC)C(CO)O2)OC(C)=O)C(O)C(O)C(OC2C(OC(C)C(O)C2O)CO)O1 MKRNVBXERAPZOP-UHFFFAOYSA-N 0.000 description 1
- KDYFGRWQOYBRFD-UHFFFAOYSA-N Succinic acid Natural products OC(=O)CCC(O)=O KDYFGRWQOYBRFD-UHFFFAOYSA-N 0.000 description 1
- 240000008042 Zea mays Species 0.000 description 1
- 235000005824 Zea mays ssp. parviglumis Nutrition 0.000 description 1
- 235000002017 Zea mays subsp mays Nutrition 0.000 description 1
- 150000001242 acetic acid derivatives Chemical class 0.000 description 1
- 150000007513 acids Chemical class 0.000 description 1
- 239000008186 active pharmaceutical agent Substances 0.000 description 1
- 230000010062 adhesion mechanism Effects 0.000 description 1
- GUBGYTABKSRVRQ-ASMJPISFSA-N alpha-maltose Chemical compound O[C@@H]1[C@@H](O)[C@H](O)[C@@H](CO)O[C@@H]1O[C@@H]1[C@@H](CO)O[C@H](O)[C@H](O)[C@H]1O GUBGYTABKSRVRQ-ASMJPISFSA-N 0.000 description 1
- 239000000440 bentonite Substances 0.000 description 1
- 229910000278 bentonite Inorganic materials 0.000 description 1
- SVPXDRXYRYOSEX-UHFFFAOYSA-N bentoquatam Chemical compound O.O=[Si]=O.O=[Al]O[Al]=O SVPXDRXYRYOSEX-UHFFFAOYSA-N 0.000 description 1
- 238000007664 blowing Methods 0.000 description 1
- KGBXLFKZBHKPEV-UHFFFAOYSA-N boric acid Chemical compound OB(O)O KGBXLFKZBHKPEV-UHFFFAOYSA-N 0.000 description 1
- 239000004327 boric acid Substances 0.000 description 1
- KDYFGRWQOYBRFD-NUQCWPJISA-N butanedioic acid Chemical compound O[14C](=O)CC[14C](O)=O KDYFGRWQOYBRFD-NUQCWPJISA-N 0.000 description 1
- 229910000019 calcium carbonate Inorganic materials 0.000 description 1
- 125000002057 carboxymethyl group Chemical group [H]OC(=O)C([H])([H])[*] 0.000 description 1
- 239000000460 chlorine Substances 0.000 description 1
- 229910052801 chlorine Inorganic materials 0.000 description 1
- 239000011248 coating agent Substances 0.000 description 1
- 238000000576 coating method Methods 0.000 description 1
- 230000000052 comparative effect Effects 0.000 description 1
- 230000008602 contraction Effects 0.000 description 1
- 238000010411 cooking Methods 0.000 description 1
- 235000005822 corn Nutrition 0.000 description 1
- 239000003431 cross linking reagent Substances 0.000 description 1
- AZSFNUJOCKMOGB-UHFFFAOYSA-N cyclotriphosphoric acid Chemical compound OP1(=O)OP(O)(=O)OP(O)(=O)O1 AZSFNUJOCKMOGB-UHFFFAOYSA-N 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 230000018044 dehydration Effects 0.000 description 1
- 238000006297 dehydration reaction Methods 0.000 description 1
- 230000006866 deterioration Effects 0.000 description 1
- 230000018109 developmental process Effects 0.000 description 1
- 238000004134 energy conservation Methods 0.000 description 1
- 150000002148 esters Chemical class 0.000 description 1
- 239000000945 filler Substances 0.000 description 1
- 238000001879 gelation Methods 0.000 description 1
- 125000004029 hydroxymethyl group Chemical group [H]OC([H])([H])* 0.000 description 1
- 229910052500 inorganic mineral Inorganic materials 0.000 description 1
- VZCYOOQTPOCHFL-UPHRSURJSA-N maleic acid Chemical compound OC(=O)\C=C/C(O)=O VZCYOOQTPOCHFL-UPHRSURJSA-N 0.000 description 1
- 239000011976 maleic acid Substances 0.000 description 1
- 238000005259 measurement Methods 0.000 description 1
- 238000000691 measurement method Methods 0.000 description 1
- 230000007246 mechanism Effects 0.000 description 1
- 239000011707 mineral Substances 0.000 description 1
- 235000010755 mineral Nutrition 0.000 description 1
- 235000019426 modified starch Nutrition 0.000 description 1
- 238000006386 neutralization reaction Methods 0.000 description 1
- 230000003472 neutralizing effect Effects 0.000 description 1
- 235000006408 oxalic acid Nutrition 0.000 description 1
- 239000011087 paperboard Substances 0.000 description 1
- 230000035699 permeability Effects 0.000 description 1
- 238000002360 preparation method Methods 0.000 description 1
- 238000003825 pressing Methods 0.000 description 1
- 150000003141 primary amines Chemical class 0.000 description 1
- 235000019260 propionic acid Nutrition 0.000 description 1
- IUVKMZGDUIUOCP-BTNSXGMBSA-N quinbolone Chemical compound O([C@H]1CC[C@H]2[C@H]3[C@@H]([C@]4(C=CC(=O)C=C4CC3)C)CC[C@@]21C)C1=CCCC1 IUVKMZGDUIUOCP-BTNSXGMBSA-N 0.000 description 1
- 230000008707 rearrangement Effects 0.000 description 1
- 230000035939 shock Effects 0.000 description 1
- 239000011780 sodium chloride Substances 0.000 description 1
- SUKJFIGYRHOWBL-UHFFFAOYSA-N sodium hypochlorite Chemical compound [Na+].Cl[O-] SUKJFIGYRHOWBL-UHFFFAOYSA-N 0.000 description 1
- 230000002195 synergetic effect Effects 0.000 description 1
- VZCYOOQTPOCHFL-UHFFFAOYSA-N trans-butenedioic acid Natural products OC(=O)C=CC(O)=O VZCYOOQTPOCHFL-UHFFFAOYSA-N 0.000 description 1
- 238000009736 wetting Methods 0.000 description 1
Landscapes
- Paints Or Removers (AREA)
- Adhesives Or Adhesive Processes (AREA)
Description
(産業上の利用分野)
本発明は、段ボールの製造に用いる澱粉系接着
剤に関するものであり、さらに詳しくいえば、段
ボール製造工程の省エネルギーをはかり、原紙貼
合の高速化、製品の高品質化をはかつた澱粉系接
着剤に関するものである。
(従来技術)
従来、一般に段ボールの製造に使用される澱粉
系接着剤はステインホール方式と呼ばれる製糊方
法で製造され、キヤリヤ部と呼ばれるアルカリ糊
化した澱粉糊液とメイン部と呼ばれる未糊化澱粉
の懸濁液との混合物からなつている。この接着剤
の接着機構は、基本的には貼合工程時に加熱する
ことによつてメイン部の未糊化澱粉を膨潤糊化し
て接着力を発現させ、加熱によつて水分を蒸発せ
しめ、乾燥により強固な接着を完了することにあ
る。
したがつて、このような接着剤を使用する場
合、貼合工程での熱エネルギー消費量が非常に大
きい。特にダブルフエーサーと呼ばれる段ボール
の貼合工程では、片段の段頂に塗布した糊を加熱
するにはライナーを通して行なわねばならないの
で莫大な熱量がライナーの加熱にのみ費やされ、
加えられた熱量のうちわずかな量だけメイン部澱
粉の糊化に役立つているにすぎない状態である。
また複両面段ボールを製造する場合には更に片段
を通しての加熱になるので熱損失はいつそう著し
くなる。ゆえにこのような接着剤では、媒体を通
しての間接加熱となるため熱伝導速度が低下し、
貼合速度も遅くなり、段ボールの製造速度は最高
マシン速度の1/2〜2/3が限度とされている。一
方、このような接着剤では、加えられた熱および
水に起因する紙の伸縮も避けられないので、段ボ
ールシートの反り発生等の製造上の欠点もある。
段ボール業界では、オイルシヨツク以後のエネ
ルギー危機から上記問題を解決することが切望さ
れ、加熱操作を必要とせず貼合できる省エネルギ
ー型接着剤の開発が大きな課題となつてきた。
近年、省エネルギーの観点からコールドコルゲ
ーシヨンシステムと呼ばれる方式すなわち熱を使
用しないで段ボールの波形を形成する方式および
貼合工程時に加熱を必要としない澱粉系接着剤
(米国特許第3300360号明細書参照)が開発され
た。この澱粉系接着剤の特徴は未糊化澱粉を含ま
ない均質な澱粉糊からなることである。この澱粉
系接着剤の接着機構は、高温かつ低粘度に保持し
た接着剤を常温の中芯原紙段頂に塗布し自然冷却
による接着剤の増粘と同時に進行する乾燥とによ
つてライナー原紙を貼合固着させることである。
したがつて、この澱粉系接着剤を段ボール製造用
に使用すれば段ボールの貼合工程で加熱を全く省
略することができる。しかしながら、この接着剤
はセツト速度が非常に遅く、十分な貼合速度が得
られないばかりかダブルフエーサー側の貼合にお
いてはスリツタ−スコアラーを通るため接着力が
その衝撃に耐えきれず剥がれてしまい、いまだ実
用の段階に至つていない。
(発明の目的)
本発明者らは、前述した段ボール製造用接着剤
の現状を打開して、段ボールの製造工程における
所要熱量の大幅な節減ならびにダブルフエーサー
の貼合性向上を図ること、ならびに優れたセツト
性を有し、じゆうぶんな貼合速度と段ボールシー
ト品質を与えるような段ボール製造用澱粉系接着
剤を得ることを目的として本発明を完成した。
(発明の構成)
アミロース含量が35重量%以上であつて、澱粉
濃度が30重量%でPHが12である水懸濁液の95℃に
おける粘度が50〜2000ブラベンダー・ユニツトで
ある酸処理とうもろこし澱粉のエーテル化又はエ
ステル化した加工澱粉を蒸煮したものを有効成分
とする接着剤であつて、糊液濃度が20〜50重量
%、温度85℃において50〜2000ブラベンダー・ユ
ニツトの粘度を有し、かつ常温で固化する性質を
有し、未糊化澱粉を含まないことを特徴とする段
ボール製造用コールドセツト型接着剤である。
((デンプン))
本発明に用いる澱粉はアミロース含量35重量%
以上の高アミロースとうもろこし澱粉が使用でき
る。
高アミロースとうもろこし澱粉は、澱粉粒を構
成する直鎖状分子(アミロース)を多く含むた
め、通常のとうもろこし澱粉(アミロース含量約
25%)と比べ、極めて老化しやすく、フイルム強
度が強く、接着力が強いなどの特性を有してい
る。このような特性を有する高アミロースとうも
ろこし澱粉は、本発明の接着剤の原料として極め
て適している。
((酸処理))
本発明は、段ボール製造時に加熱を必要としな
い、優れたセツト性を有する澱粉系接着剤を提供
するものであるから、糊液は水の散失負担を少な
くするため高濃度であることが必要であり、かつ
段ボールの貼合面に塗布後、急速にセツト現象を
起こすことが要求される。また段ボール製造に於
いては、ダブルフエーサーでスリツタースコアラ
ーをかけるため、接着剤のセツト性が非常に重要
な役割を演ずる。
したがつて、高濃度化を計りかつ糊液の流動性
を保持するために低粘度化処理した酸処理高アミ
ロースとうもろこし澱粉は、急速セツトするた
め、本発明において好適原料と考えられる。
本発明において原料となる酸処理高アミロース
とうもろこし澱粉は、高アミロースとうもろこし
澱粉を塩酸、硫酸などの鉱酸あるいは蓚酸、酢酸
などの有機酸で処理して得られ、澱粉濃度30重量
%(25%苛性ソーダでPH12に調整)25℃より1.5
℃/分昇温、95℃におけるブラベンダー粘度が50
〜2000B.U.の澱粉が適する。酸処理澱粉の粘度
が2000B.U.以上になると老化が高く、流動性を
失い好ましくない。又粘度が50B.U.以下になる
と老化は低下するものの、澱粉がアミロデキスト
リン化し、白化し乾燥するともろくなり、接着強
度は弱く、耐湿性も乏しくなるという短所があ
る。
((エステル化・エーテル化))
前述したように、高アミロースとうもろこし澱
粉は、直鎖状分子のアミロースを多く含むため、
一般にいわれるようにその澱粉は、直鎖状分子の
再配列、すなわち老化が極めて生じやすい。この
老化は濃度、温度に依存するので、本発明のごと
き高濃度糊液の接着剤を目的に高アミロースとう
もろこし澱粉を酸処理低粘度化を計つても、老化
は大きく糊液ライフが非常に短いという短所があ
る。
本発明者らは、酸処理高アミロースとうもろこ
し澱粉をエステル化あるいはエーテル化処理し、
置換基を導入することにより、酸処理高アミロー
スとうもろこし澱粉の老化を適度に抑えて、糊液
ライフが長く、オープンタイムも取れる優れたセ
ツト性を有する澱粉系接着剤を製造することがで
きることを見いだした。
本発明に用いる澱粉は所定測定法で粘度が50B.
U.〜2000B.U.(B.U.はブラベンダ−ユニツトの
略)の酸処理高アミロースとうもろこし澱粉を酢
酸、プロピオン酸、酪酸、コハク酸、マレイン
酸、フタル酸等の有機酸と反応して得られるエス
テル化澱粉、リン酸エステル澱粉、あるいは、酸
処理高アミロースとうもろこし澱粉をヒドロキシ
メチル、ヒドロキシエチル、ヒドロキシプロピ
ル、カルボキシメチル、カルボキシエチル、2−
アミノエチルエーテル、第1アミンエーテル、第
3アミノアルキルエーテル、第4アンモニウムア
ルキルエーテル等のエーテル化した澱粉である。
さらに、トリメタリン酸、エピクロルヒドリン等
の架橋剤を架橋した酸処理高アミロースとうもろ
こし澱粉も使用可能である。これらの澱粉で好ま
しいのは、濃度20〜50重量%、温度85℃における
糊液粘度が50〜2000B.U.好ましくは100〜1000B.
U.置換度が0.01〜0.7のエステル化・エーテル化
澱粉である。置換度が0.01以下である場合、置換
基導入数が少なく老化抑制に十分でない。又0.7
以上になると高置換となり直鎖分子のからみあい
を阻止するためと思われるが老化を抑えすぎ、セ
ツト性が悪くなるという現象が生じる。
((接着剤の調製))
本発明の澱粉系接着剤の調製方法は、上記の酸
処理高アミロースとうもろこし澱粉のエステル化
あるいはエーテル化した澱粉を水に分散させ、澱
粉濃度20〜50重量%の懸濁液を任意の加熱方法、
例えば、ジエツトクツカーのような蒸気吹き込み
による直接加熱方式、高圧クツカーのようなジヤ
ケツトによる間接加熱方式により糊炊きを行い、
澱粉濃度20〜50重量%、温度85℃における粘度が
50B.U.〜2000B.U.好ましくは100〜1000B.U.の高
温、高濃度の糊液を調製する。
本発明においては、必要に応じて、澱粉の持つ
粘着物性を更に強固なものにするため、苛性ソー
ダのごときアルカリを加えてPH調整してもよい。
けれどもPHを11.0以上にするとアルカリによる劣
化を招く作用があり、注意を要する。さらに硼
砂、硼酸のごとき、ゲル化促進剤を併用すること
もできる。また、糊コスト低減のため、クレイ、
ベントナイト、炭酸カルシウムなどのフイラーも
添加することができる。
((接着剤の濃度および粘度))
本発明の澱粉系接着剤中の澱粉濃度は20〜50重
量%が好ましい。なぜならば、本接着剤は、蒸煮
糊化した均質な糊液を貼合面に塗布し、加熱操作
を省いて接着するものであるから、水の散失、瞬
間的固化が必須条件となるため、高濃度糊液であ
ることが要求されるからである。段ボールのシン
グルフエーサー側を接着する場合には、段ロール
とプレスロールによるニツプ圧が効果的に働くた
め、糊液濃度20重量%で十分に貼合できるが、ダ
ブルフエーサー側を接着する場合には、プレス効
果がなく澱粉濃度を高くした方が水の散失、固化
が速いために貼合速度を上げることができるので
製造上有利である。しかし濃度が50重量%を越え
て高くなると、粘度に上限がある以上、澱粉を更
に低分子化しなければならないため、乾燥すると
もろくなり、接着強度は弱く、耐湿性も乏しくな
る欠点がある。
以上のように、この発明の接着剤の澱粉濃度
は、必要に応じて20〜50重量%に調整する。
製造した接着剤の粘度は、測定温度85℃におい
て50〜2000B.U.好まくは100〜1000B.U.のブラベ
ンダー粘度になるように調整する。当然ながら接
着剤粘度は糊炊き時の澱粉濃度、酸処理、エーテ
ルエステル化とも相対関係にあり、設計した接着
剤粘度を得るためには、製造のための諸条件を適
当に選択すればよい。
(接着剤の使用方法)
この接着剤は、所定の温度を保持させた接着剤
を段ボールの貼合面に塗布し、自然冷却および糊
液の濃縮によつてライナーと中芯原紙の接着を完
了するものであり、この冷却および濃縮により澱
粉糊液は、急速に固化して強固な接着力を生じる
ものである。さらに塗布温度は、紙面に対する、
ぬれ、浸透性をよくし、使用粘度を維持するた
め、さらに作業性を考慮した場合70℃〜95℃が好
ましい。
なお、貼合にあたつては使用原紙水分も貼合適
性に影響し、貼合速度・セツト性は、原紙水分を
低く目に抑え、本発明の接着剤を用いると相乗効
果が現われ、向上し、本発明はさらに改善され
る。好ましくは、原紙水分4%以下がよい。
(実施例)
本発明をいつそう理解しやすくするために以下
に実施例および対照例を示し、具体的に説明する
が、下記の実施例はこの発明を何ら制限するもの
ではない。
実施例 1
酸処理高アミロースとうもろこし澱粉(澱粉濃
度30重量%(PH12に調整)1.5℃/分昇温95℃に
おけるブラベンダー粘度220B.U.)450Kgを25℃
の水680に分散させ、3%苛性ソーダでPH8.0に
調整しながら無水酢酸190Kgを加え、1時間撹拌
を続け、その後塩酸でPH5.0に中和した後、脱
水、水洗、乾燥して置換度(DS)0.4の酢酸澱粉
を得た。この酢酸澱粉を水に分散させ、澱粉濃度
35重量%の懸濁液を調製し、この懸濁液を間接加
熱連続糊化装置にて140℃で糊炊きを行ない、全
固形分35重量%の接着剤を得た。この接着剤の粘
度は温度85℃においてブラベンダー粘度が250B.
U.であつた。
使用例 1
この接着剤を使用して、蒸気を全く通さない実
際のダブルフエーサーで片面段ボール(B−220
×SCP125)とライナー(B−220)を貼り合わ
せ、両面段ボールを製造したところ、130m/分
の速度で貼合できた。
実施例 2
実施例1の酸処理高アミロースとうもろこし澱
粉を水に分散させ、38重量%の懸濁液を調製す
る。この懸濁液に対澱粉4%の塩化ナトリウムお
よび対澱粉0.85%の苛性ソーダ(3%水溶液で)
を添加、さらに対澱粉12%のプロピレンオキシド
を加え、反応温度45℃にて密閉反応容器で5時間
反応し、濃塩酸でPH6.0に中和後、水洗、脱水、
乾燥して置換度0.25のヒドロキシプロピル澱粉を
得た。このヒドロキシプロピル澱粉を実施例1と
同様に間接加熱連続糊化装置で糊炊きを行い25%
苛性ソーダーでPH8.5に調整し、全固形分35重量
%、温度85℃においてブラベンダー粘度240B.U.
の接着剤を得た。
使用例 2
使用例1と同様に熱を全く通さないダブルフエ
ーサーで両面段ボールを製造したところ、130
m/分の速度で貼合できた。
対照例 1
実施例1の酸処理高アミロースとうもろこし澱
粉を間接加熱連続糊化装置で糊炊きを行い25%苛
性ソーダでPH8.8に調整し、全固形分35重量%、
温度85℃においてブラベンダー粘度280B.U.の接
着剤を得た。この接着剤を使用して、使用例1と
同様にダブルフエーサーにて両面段ボールを製造
したが、糊液はゲル化して貼合できなかつた。こ
れらの結果を表−1に示す。
対照例 2
高アミロースとうもろこし澱粉(アミロース含
量70%)450Kgを40℃の温水650に溶解し、濃度
3%の苛性ソーダ水溶液でPH11.0に調整しながら
有効塩素13%の次亜塩素酸ソーダ135を添加
し、40℃で4時間撹拌を続け、その後塩酸でPHを
5.0に中和した後、水洗、脱水、乾燥して酸化高
アミロースとうもろこし澱粉を得た。
この酸化高アミロースとうもろこし澱粉を実施
例1と同様に間接加熱連続糊化装置で糊炊きを行
い、PH8.0、固形分34重量%、ブラベンダー粘度
210B.U.の接着剤を得た。この接着剤を使用例1
と同様にダブルフエーサーで両面段ボールを製造
した。90m/分の速度で貼合でき、これ以上速度
を上げるとカツター先で剥離が生じた。これらの
結果を表−1に示す。
(Industrial Application Field) The present invention relates to a starch-based adhesive used in the manufacture of corrugated cardboard. More specifically, the present invention relates to a starch-based adhesive used in the manufacture of corrugated cardboard. More specifically, it is used to save energy in the corrugated cardboard manufacturing process, speed up the lamination of base paper, and improve the quality of the product. This invention relates to starch-based adhesives that have (Prior art) Starch-based adhesives commonly used in the manufacture of corrugated board have traditionally been manufactured using a glue manufacturing method called the stain hole method, in which an alkali-gelatinized starch paste called a carrier part and an ungelatinized starch paste called a main part are used. It consists of a mixture with a suspension of starch. The bonding mechanism of this adhesive is basically that by heating during the lamination process, the ungelatinized starch in the main part swells and becomes gelatinized to develop adhesive strength, and then the water is evaporated by heating and then dried. The goal is to achieve stronger adhesion. Therefore, when such an adhesive is used, the amount of thermal energy consumed in the bonding process is very large. In particular, in the corrugated board bonding process known as double facer, heating the glue applied to the top of one tier must be done through a liner, so a huge amount of heat is spent just heating the liner.
In this state, only a small amount of the added heat serves to gelatinize the main starch.
Furthermore, when producing double-sided corrugated board, heating is required through one stage, so heat loss becomes significant. Therefore, with such adhesives, the heat conduction rate decreases due to indirect heating through the medium,
The lamination speed is also slower, and the production speed of corrugated board is limited to 1/2 to 2/3 of the maximum machine speed. On the other hand, with such adhesives, expansion and contraction of the paper due to the applied heat and water cannot be avoided, so there are manufacturing disadvantages such as warping of the corrugated paperboard sheet. In the corrugated board industry, there has been a strong desire to solve the above-mentioned problems due to the energy crisis that followed the oil shock crisis, and the development of energy-saving adhesives that can be bonded without the need for heating has become a major issue. In recent years, from the perspective of energy conservation, a method called the cold corrugation system, which forms corrugated cardboard without using heat, and a starch-based adhesive that does not require heating during the lamination process (see U.S. Pat. No. 3,300,360) have been developed. ) was developed. A feature of this starch-based adhesive is that it consists of a homogeneous starch paste that does not contain ungelatinized starch. The adhesion mechanism of this starch-based adhesive is to apply the adhesive maintained at high temperature and low viscosity to the corrugated top of the core base paper at room temperature, and to dry the liner base paper at the same time as the adhesive increases in viscosity due to natural cooling. It is to bond and fix.
Therefore, if this starch-based adhesive is used for manufacturing corrugated boards, heating can be completely omitted in the process of laminating corrugated boards. However, this adhesive has a very slow setting speed, and not only is it difficult to obtain a sufficient lamination speed, but when laminating the double facer side, it passes through a slitter and scorer, so the adhesive force cannot withstand the impact and it peels off. However, it has not yet reached the stage of practical use. (Objective of the Invention) The present inventors have overcome the current state of adhesives for manufacturing corrugated board as described above, and aim to significantly reduce the amount of heat required in the manufacturing process of corrugated board and improve the bonding properties of double facer. The present invention was completed with the aim of obtaining a starch-based adhesive for corrugated board manufacturing that has excellent setting properties, provides adequate lamination speed and corrugated sheet quality. (Structure of the Invention) Acid-treated corn having an amylose content of 35% by weight or more, a starch concentration of 30% by weight, and a pH of 12, in which the viscosity at 95°C of an aqueous suspension is 50 to 2000 Brabender units. An adhesive whose active ingredient is a steamed processed starch obtained by etherifying or esterifying starch, with a concentration of 20 to 50% by weight and a viscosity of 50 to 2000 Brabender units at a temperature of 85°C. This is a cold-set adhesive for corrugated board manufacturing, which is characterized by having the property of solidifying at room temperature and containing no ungelatinized starch. ((Starch)) The starch used in the present invention has an amylose content of 35% by weight.
The above high amylose corn starch can be used. High-amylose corn starch contains a large amount of linear molecules (amylose) that make up starch granules, so high amylose corn starch contains a lot of linear molecules (amylose) that make up starch granules.
25%), it ages extremely easily, has strong film strength, and has strong adhesive strength. High amylose corn starch having such properties is extremely suitable as a raw material for the adhesive of the present invention. ((Acid treatment)) The present invention provides a starch-based adhesive that does not require heating during corrugated board manufacturing and has excellent setting properties. In addition, it is required that the setting phenomenon occurs rapidly after being applied to the bonding surface of the corrugated board. Furthermore, in the production of corrugated board, a double facer is used to apply a slitter scorer, so the setting properties of the adhesive play a very important role. Therefore, acid-treated high amylose corn starch, which has been treated to reduce the viscosity in order to increase the concentration and maintain the fluidity of the size liquid, is considered to be a suitable raw material in the present invention because it sets rapidly. Acid-treated high amylose corn starch, which is a raw material in the present invention, is obtained by treating high amylose corn starch with mineral acids such as hydrochloric acid and sulfuric acid, or organic acids such as oxalic acid and acetic acid, and has a starch concentration of 30% by weight (25% caustic soda). (adjusted to PH12) 1.5 from 25℃
Temperature increase at °C/min, Brabender viscosity at 95 °C is 50
Starch of ~2000 B.U. is suitable. If the viscosity of the acid-treated starch exceeds 2000 B.U., aging will be high and fluidity will be lost, which is not preferable. When the viscosity is lower than 50 B.U., although aging is reduced, the starch becomes amylodextrin, whitens, becomes brittle when dried, has weak adhesive strength, and has poor moisture resistance. ((Esterification/Etherification)) As mentioned above, high amylose corn starch contains a lot of amylose, a linear molecule.
Generally speaking, starch is extremely susceptible to rearrangement of linear molecules, that is, retrogradation. This aging depends on concentration and temperature, so even if high-amylose corn starch is treated with acid to reduce its viscosity for the purpose of making a high-concentration size liquid adhesive like the one of the present invention, aging will be large and the size liquid life will be very short. There is a disadvantage. The present inventors esterified or etherified acid-treated high amylose corn starch,
We have discovered that by introducing a substituent, it is possible to moderately suppress the aging of acid-treated high amylose corn starch, and to produce a starch-based adhesive that has a long glue life and excellent setting properties that allow for long open times. Ta. The starch used in the present invention has a viscosity of 50B according to a specified measurement method.
Esters obtained by reacting acid-treated high amylose corn starch of U. to 2000 B.U. (BU stands for Brabender Unit) with organic acids such as acetic acid, propionic acid, butyric acid, succinic acid, maleic acid, and phthalic acid. Hydroxymethyl, hydroxyethyl, hydroxypropyl, carboxymethyl, carboxyethyl, 2-
These are etherified starches such as aminoethyl ether, primary amine ether, tertiary aminoalkyl ether, and quaternary ammonium alkyl ether.
Furthermore, acid-treated high amylose corn starch crosslinked with a crosslinking agent such as trimetaphosphoric acid or epichlorohydrin can also be used. These starches preferably have a concentration of 20 to 50% by weight and a paste viscosity of 50 to 2000 B.U., preferably 100 to 1000 B.U., at a temperature of 85°C.
U. Esterified/etherified starch with a degree of substitution of 0.01 to 0.7. When the degree of substitution is 0.01 or less, the number of substituents introduced is small and is not sufficient to suppress aging. Also 0.7
If the content is higher than that, the substitution becomes highly substituted, presumably to prevent entanglement of linear molecules, but aging is suppressed too much, resulting in poor setting properties. ((Preparation of Adhesive)) The method for preparing the starch-based adhesive of the present invention involves dispersing the esterified or etherified starch of the acid-treated high amylose corn starch in water to obtain a starch concentration of 20 to 50% by weight. any method of heating the suspension;
For example, glue can be cooked using a direct heating method using steam blowing, such as in a jet cooker, or an indirect heating method using a jacket, such as a high-pressure cooker.
The viscosity at a starch concentration of 20-50% by weight and a temperature of 85℃ is
A high temperature, high concentration paste solution of 50 B.U. to 2000 B.U., preferably 100 to 1000 B.U. is prepared. In the present invention, if necessary, an alkali such as caustic soda may be added to adjust the pH in order to further strengthen the adhesive properties of starch.
However, if the pH is higher than 11.0, the alkali will cause deterioration, so care must be taken. Furthermore, gelation accelerators such as borax and boric acid can also be used together. In addition, to reduce glue costs, clay,
Fillers such as bentonite, calcium carbonate, etc. can also be added. ((Concentration and Viscosity of Adhesive)) The starch concentration in the starch adhesive of the present invention is preferably 20 to 50% by weight. This is because this adhesive applies a homogeneous paste liquid that has been steamed to a paste onto the bonding surface and adheres without heating, so water dissipation and instantaneous solidification are essential conditions. This is because a highly concentrated paste solution is required. When gluing the single facer side of corrugated board, the nip pressure from the corrugating rolls and press rolls works effectively, so a glue concentration of 20% by weight can be sufficient for bonding, but when gluing the double facer side Since there is no pressing effect and the starch concentration is increased, water dissipation and solidification are faster, so the lamination speed can be increased, which is advantageous in production. However, if the concentration exceeds 50% by weight, the viscosity has an upper limit and the starch must be further reduced in molecular weight, resulting in brittleness when dried, weak adhesive strength, and poor moisture resistance. As described above, the starch concentration of the adhesive of the present invention is adjusted to 20 to 50% by weight as necessary. The viscosity of the produced adhesive is adjusted to have a Brabender viscosity of 50 to 2000 B.U., preferably 100 to 1000 B.U., at a measurement temperature of 85°C. Naturally, the adhesive viscosity has a relative relationship with the starch concentration during cooking, acid treatment, and ether esterification, and in order to obtain the designed adhesive viscosity, various conditions for production may be appropriately selected. (How to use the adhesive) With this adhesive, the adhesive is maintained at a specified temperature and applied to the bonding surface of the cardboard, and the liner and core base paper are completely bonded by natural cooling and concentration of the size liquid. By this cooling and concentration, the starch paste solution rapidly solidifies and produces strong adhesive strength. Furthermore, the coating temperature is
In order to improve wetting and permeability and to maintain the usable viscosity, the temperature is preferably 70°C to 95°C in consideration of workability. In addition, when laminating, the moisture content of the base paper used also affects lamination suitability, and the lamination speed and setting properties can be improved by keeping the moisture content of the base paper low and using the adhesive of the present invention, as a synergistic effect appears. However, the present invention is further improved. Preferably, the moisture content of the base paper is 4% or less. (Examples) In order to make the present invention easier to understand, Examples and Comparative Examples will be shown and specifically explained below, but the following Examples do not limit the present invention in any way. Example 1 Acid-treated high amylose corn starch (starch concentration 30% by weight (adjusted to PH12) Brabender viscosity 220 B.U. at 1.5°C/min temperature increase at 95°C) 450 kg at 25°C
Dispersed in 680 g of water, adjusted to pH 8.0 with 3% caustic soda, added 190 kg of acetic anhydride, continued stirring for 1 hour, then neutralized to pH 5.0 with hydrochloric acid, dehydrated, washed with water, dried and replaced. Starch acetate with a degree (DS) of 0.4 was obtained. This acetic acid starch is dispersed in water to determine the starch concentration.
A 35% by weight suspension was prepared, and this suspension was heated at 140°C in an indirect heating continuous gelatinization device to obtain an adhesive with a total solid content of 35% by weight. The viscosity of this adhesive is Brabender viscosity of 250B at a temperature of 85℃.
It was U. Example of use 1 Use this adhesive to attach single-sided corrugated cardboard (B-220
×SCP125) and liner (B-220) were bonded together to produce double-sided corrugated board, and the bonding was possible at a speed of 130 m/min. Example 2 The acid-treated high amylose corn starch of Example 1 is dispersed in water to prepare a 38% by weight suspension. Add to this suspension 4% sodium chloride to starch and 0.85% caustic soda to starch (in a 3% aqueous solution).
was added, and propylene oxide with a ratio of 12% to starch was added, and the mixture was reacted for 5 hours in a closed reaction vessel at a reaction temperature of 45°C. After neutralization to pH 6.0 with concentrated hydrochloric acid, washing with water, dehydration,
After drying, hydroxypropyl starch with a degree of substitution of 0.25 was obtained. This hydroxypropyl starch was boiled into a paste using an indirect heating continuous gelatinization device in the same manner as in Example 1, and the percentage was reduced to 25%.
Adjusted to pH 8.5 with caustic soda, total solids content 35% by weight, Brabender viscosity 240 B.U. at 85°C.
of adhesive was obtained. Usage example 2 In the same way as usage example 1, double-sided cardboard was manufactured using a double facer that does not allow any heat to pass through.
Lamination was possible at a speed of m/min. Control Example 1 The acid-treated high amylose corn starch of Example 1 was cooked in an indirect heating continuous gelatinizer and adjusted to pH 8.8 with 25% caustic soda, and the total solid content was 35% by weight.
An adhesive with a Brabender viscosity of 280 B.U. was obtained at a temperature of 85°C. Using this adhesive, a double-sided corrugated board was produced using a double facer in the same manner as in Use Example 1, but the size solution gelled and could not be bonded. These results are shown in Table-1. Control example 2 450 kg of high amylose corn starch (amylose content 70%) was dissolved in 40°C warm water 650, and while adjusting the pH to 11.0 with a 3% aqueous solution of caustic soda, added sodium hypochlorite 135 with 13% available chlorine. and continue stirring at 40℃ for 4 hours, then adjust the pH with hydrochloric acid.
After neutralizing to 5.0, oxidized high amylose corn starch was obtained by washing with water, dehydrating, and drying. This oxidized high amylose corn starch was cooked in an indirect heating continuous gelatinization device in the same manner as in Example 1, with a pH of 8.0, a solid content of 34% by weight, and a Brabender viscosity.
Obtained 210 B.U. of adhesive. Example of using this adhesive 1
Double-sided corrugated cardboard was produced using double facer in the same manner as above. Lamination was possible at a speed of 90 m/min, and if the speed was increased beyond this, peeling occurred at the cutter tip. These results are shown in Table-1.
【表】
実施例 3
実施例2のヒドロキシプロピル澱粉を用い、澱
粉23重量部、クレー22重量部、水55重量部、硼砂
0.46重量部組成の懸濁液を実施例1と同様に糊炊
きを行ない、30%苛性ソーダ水溶液でPHを9.9に
調整し、全固形分約45重量%、ブラベンダー粘度
620B.U.の接着剤を得た。
使用例 3
この接着剤を用い、使用例1と同様に熱を全く
通さないダブルフエーサーで両面段ボールを製造
したところ、135m/分の速度で貼合できた。
実施例 4
実施例2のヒドロキシプロピル澱粉の濃度33重
量%の懸濁液を調製し、それに対澱粉2重量%の
硼砂を添加し、実施例1と同様に糊炊きを行い、
25重量%の苛性ソーダ水溶液でPHを10.0に調整し
て全固形分約31重量%、85℃におけるブラベンダ
ー粘度340B.U.の接着剤を得た。
使用例 4
この接着剤を用いて実施例1と同様に両面段ボ
ールを製造したところ、130m/分の速度で貼合
できた。[Table] Example 3 Using the hydroxypropyl starch of Example 2, 23 parts by weight of starch, 22 parts by weight of clay, 55 parts by weight of water, borax
A suspension having a composition of 0.46 parts by weight was prepared in the same manner as in Example 1, and the pH was adjusted to 9.9 with a 30% aqueous solution of caustic soda.The total solid content was approximately 45% by weight, and the Brabender viscosity was adjusted to 9.9.
Obtained 620B.U. of adhesive. Usage Example 3 Using this adhesive, double-sided corrugated cardboard was manufactured using a double facer that does not transmit any heat in the same manner as in Usage Example 1, and the adhesive could be bonded at a speed of 135 m/min. Example 4 A suspension of the hydroxypropyl starch of Example 2 with a concentration of 33% by weight was prepared, borax was added thereto at a concentration of 2% by weight of the starch, and the paste was cooked in the same manner as in Example 1.
The pH was adjusted to 10.0 with a 25% by weight aqueous solution of caustic soda to obtain an adhesive with a total solids content of about 31% by weight and a Brabender viscosity of 340 B.U. at 85°C. Usage Example 4 When double-sided corrugated board was manufactured using this adhesive in the same manner as in Example 1, it was possible to bond the sheets together at a speed of 130 m/min.
【表】
(発明の効果)
本発明澱粉系接着剤は、加熱操作を省いて貼合
ができ、貼合速度も実用可能な速度が得られ、接
着強度も十分なものであつた。更に無加熱および
糊液の高固形分化により、熱および水に起因する
反りの問題もなく、高品質の段ボールシートを製
造することができる。[Table] (Effects of the Invention) The starch-based adhesive of the present invention could be laminated without heating operations, a lamination speed that was practical could be obtained, and adhesive strength was sufficient. Furthermore, due to no heating and high solidification of the size liquid, high quality corrugated cardboard sheets can be produced without the problem of warping caused by heat and water.
Claims (1)
粉濃度が30重量%でPHが12である水懸濁液の95℃
における粘度が50〜2000ブラベンダー・ユニツト
である酸処理とうもろこし澱粉のエーテル化又は
エステル化した加工澱粉を蒸煮したものを有効成
分とする接着剤であつて糊液濃度が20〜50重量
%、温度85℃において50〜2000ブラベンダー・ユ
ニツトの粘度を有し、かつ常温で固化する性質を
有し、未糊化澱粉を含まないことを特徴とする段
ボール製造用コールドセツト型接着剤。 2 エステル化またはエーテル化の置換度が0.01
〜0.7である特許請求の範囲第1項記載の接着
剤。[Claims] 1. An aqueous suspension having an amylose content of 35% by weight or more, a starch concentration of 30% by weight, and a pH of 12 at 95°C.
An adhesive whose active ingredient is a processed starch obtained by etherifying or esterifying acid-treated corn starch and having a viscosity of 50 to 2000 Brabender Units at a temperature of 20 to 50% by weight. A cold-set adhesive for corrugated board manufacturing, which has a viscosity of 50 to 2000 Brabender units at 85°C, solidifies at room temperature, and does not contain ungelatinized starch. 2 Degree of substitution for esterification or etherification is 0.01
The adhesive according to claim 1, which has a molecular weight of ˜0.7.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP19247583A JPS6084370A (en) | 1983-10-17 | 1983-10-17 | Adhesive for production of corrugated cardboard |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP19247583A JPS6084370A (en) | 1983-10-17 | 1983-10-17 | Adhesive for production of corrugated cardboard |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS6084370A JPS6084370A (en) | 1985-05-13 |
| JPS6121979B2 true JPS6121979B2 (en) | 1986-05-29 |
Family
ID=16291906
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP19247583A Granted JPS6084370A (en) | 1983-10-17 | 1983-10-17 | Adhesive for production of corrugated cardboard |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS6084370A (en) |
Families Citing this family (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US5085228A (en) * | 1990-05-21 | 1992-02-04 | National Starch And Chemical Investment Holding Corporation | Starch based natural adhesives used in cigarette manufacture |
| DE69925741T2 (en) * | 1998-07-23 | 2005-12-15 | Coöperatieve Verkoop- en Productievereniging van Aardappelmeel en Derivaten 'AVEBE' B.A. | ADHESIVE COMPOSITION |
| JP2002256241A (en) * | 2001-03-02 | 2002-09-11 | Yayoi Chemical Industry Co Ltd | Starch paste |
| EP1352939A1 (en) * | 2002-04-12 | 2003-10-15 | Remy Industries N.V. | Starch-based glue paste compositions |
-
1983
- 1983-10-17 JP JP19247583A patent/JPS6084370A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS6084370A (en) | 1985-05-13 |
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