JP2002201220A - Polyvinyl acetate resin for chewing gum - Google Patents
Polyvinyl acetate resin for chewing gumInfo
- Publication number
- JP2002201220A JP2002201220A JP2001000489A JP2001000489A JP2002201220A JP 2002201220 A JP2002201220 A JP 2002201220A JP 2001000489 A JP2001000489 A JP 2001000489A JP 2001000489 A JP2001000489 A JP 2001000489A JP 2002201220 A JP2002201220 A JP 2002201220A
- Authority
- JP
- Japan
- Prior art keywords
- polyvinyl acetate
- polymerization
- acetate resin
- vinyl acetate
- 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.)
- Granted
Links
Landscapes
- Confectionery (AREA)
- Addition Polymer Or Copolymer, Post-Treatments, Or Chemical Modifications (AREA)
Abstract
(57)【要約】
【課題】 ガムベース製造時のハンドリング性に優れ、
かつ極めて残存酢酸ビニルモノマーが少ない安全性、及
び衛生性に優れるポリ酢酸ビニル樹脂を提供すること。
【解決手段】(A)平均粒子径50〜1000μm、
(B)重合度300〜1500、及び(C)残存酢酸ビ
ニルモノマー5ppm以下の特性を有するポリ酢酸ビニ
ル樹脂を構成とする。(57) [Summary] [PROBLEMS] Excellent handling properties in the production of gum base,
To provide a polyvinyl acetate resin excellent in safety and hygiene in which the amount of residual vinyl acetate monomer is extremely small. (A) an average particle diameter of 50 to 1000 μm;
A polyvinyl acetate resin having (B) a degree of polymerization of 300 to 1500 and (C) a residual vinyl acetate monomer of 5 ppm or less is constituted.
Description
【0001】[0001]
【発明の属する技術分野】本発明は、ポリ酢酸ビニル樹
脂に関するものである。特にチューインガムを製造する
時に用いるポリ酢酸ビニル樹脂に関するものであり、ハ
ンドリング性、安全性、及び衛生性に優れる。[0001] The present invention relates to a polyvinyl acetate resin. Particularly, the present invention relates to a polyvinyl acetate resin used when producing chewing gum, and is excellent in handling properties, safety and hygiene.
【0002】[0002]
【従来の技術】従来、チューインガムベース樹脂として
天然チクルが好適であるが、高価であるため、一般的に
は天然チクルに代わりポリ酢酸ビニル樹脂が使用され
る。しかし、ポリ酢酸ビニル樹脂は酢酸ビニルモノマー
を重合して製造されるため、当該樹脂中に未反応酢酸ビ
ニルモノマーが残り、安全性、衛生面から好ましくな
い。その為、昨今は、未反応酢酸ビニルモノマーの残存
量が少ないポリ酢酸ビニル樹脂が使用されてはいるが、
チューインガム用ポリ酢酸ビニル樹脂のほとんどは酢酸
ビニルモノマーの塊状重合(特公昭39−24714
号)あるいはアルコール系溶剤を溶媒とした溶液重合
(食品添加物公定書解説書 廣川書店 昭和54年9月
10日 第1版発行 B−358〜B−359)で製造
されている。2. Description of the Related Art Conventionally, natural tickle is preferable as a chewing gum base resin, but polyvinyl acetate resin is generally used instead of natural tickle due to its high cost. However, since the polyvinyl acetate resin is produced by polymerizing a vinyl acetate monomer, unreacted vinyl acetate monomer remains in the resin, which is not preferable in terms of safety and hygiene. For this reason, recently, polyvinyl acetate resin with a small residual amount of unreacted vinyl acetate monomer has been used,
Most of the polyvinyl acetate resin for chewing gum is a bulk polymerization of a vinyl acetate monomer (JP-B-39-24714).
No.) or solution polymerization using an alcohol-based solvent as a solvent (Food Additive Official Manual, Hirokawa Shoten, 1st edition, September 10, 1979, B-358 to B-359).
【0003】[0003]
【発明が解決しようとする課題】しかしながら、塊状重
合あるいは溶液重合で製造されるポリ酢酸ビニル樹脂
は、未反応酢酸ビニルモノマーを除去するには多大な熱
エネルギーを必要とするばかりでなく、製造工程も複雑
という課題があった。また、塊状重合あるいは溶液重合
で製造されるポリ酢酸ビニル樹脂は、製品形態はブロッ
ク状の固まりとなり、これをチューインガム用酢酸ビニ
ル樹脂に使用する場合、エステルガム等他の素材とのニ
ーダー初期練成が容易でなく、特に重合度の高いポリ酢
酸ビニル樹脂では、予め細かく裁断しておくか、ニーダ
ー練成前にポリ酢酸ビニル樹脂を温めて粘度を下げてお
く等の工夫がなされているが、操作が煩雑でハンドリン
グ性に劣るという課題があった。However, the polyvinyl acetate resin produced by bulk polymerization or solution polymerization not only requires a large amount of heat energy to remove unreacted vinyl acetate monomer, but also requires a large amount of heat. Was also complicated. In addition, the polyvinyl acetate resin produced by bulk polymerization or solution polymerization has a product form of block-like lump. It is not easy, especially in the case of polyvinyl acetate resin with a high degree of polymerization, it has been devised such as cutting in advance or warming the polyvinyl acetate resin before kneading to reduce the viscosity, There is a problem that the operation is complicated and the handling is inferior.
【0004】本発明者は、前記課題を解決すべく鋭意研
究を重ねた結果、ガムベース製造時のニーダー初期練成
に優れ、残存酢酸ビニルモノマーが極めて少ないため、
安全性及び衛生性に優れたポリ酢酸ビニル樹脂を得て本
発明を完成するに至った。The inventor of the present invention has conducted intensive studies in order to solve the above-mentioned problems.
The present invention has been completed by obtaining a polyvinyl acetate resin excellent in safety and hygiene.
【0005】[0005]
【課題を解決するための手段】すなわち、本発明は、
(1)(A)平均粒子径50〜1000μm、(B)重
合度300〜1500、及び(C)残存酢酸ビニルモノ
マー5ppm以下の特性を有するポリ酢酸ビニル樹脂、
(2)チューインガムを製造する時に用いることを特徴
とする(1)記載のポリ酢酸ビニル樹脂である。That is, the present invention provides:
(1) (A) a polyvinyl acetate resin having an average particle diameter of 50 to 1000 μm, (B) a degree of polymerization of 300 to 1500, and (C) a residual vinyl acetate monomer having a characteristic of 5 ppm or less,
(2) The polyvinyl acetate resin according to (1), which is used when producing chewing gum.
【0006】[0006]
【発明の実施の形態】以下、本発明について詳しく説明
する。本発明のポリ酢酸ビニル樹脂の平均粒子径は50
〜1000μmが好ましく、さらに好ましくは200〜
400μmである。50μm未満ではガムベース製造の
ニーダー練成時に粒子が飛散されやすく、均一練成が劣
り最終製品中に異物として残るので好ましくない。ま
た、1000μm以上ではガムベース製造の練成に時間
がかかるので好ましくない。重合度は、300〜150
0が好ましく、さらに好ましくは600〜1200であ
る。300未満では粒子が融着し易く本発明の平均粒子
形態を維持し難くなる。重合度1500以上では、チュ
ーインガムが硬くなりすぎチューインガムの製造に用い
るポリ酢酸ビニル樹脂として適さないものである。残存
酢酸ビニルモノマーは、安全性、及び衛生性から5pp
m以下が必要である。BEST MODE FOR CARRYING OUT THE INVENTION Hereinafter, the present invention will be described in detail. The average particle size of the polyvinyl acetate resin of the present invention is 50.
To 1000 μm, more preferably 200 to
400 μm. If it is less than 50 μm, particles are liable to be scattered at the time of kneading in the production of a gum base, and the uniform kneading is inferior. On the other hand, if the thickness is 1000 μm or more, it takes a long time to prepare the gum base, which is not preferable. The degree of polymerization is 300 to 150
0 is preferable, and 600 to 1200 is more preferable. When it is less than 300, the particles are easily fused and it is difficult to maintain the average particle form of the present invention. If the degree of polymerization is 1500 or more, the chewing gum becomes too hard and is not suitable as a polyvinyl acetate resin used for the production of chewing gum. Residual vinyl acetate monomer is 5 pp for safety and hygiene.
m or less is required.
【0007】本発明の(A)平均粒子径50〜1000
μm、(B)重合度300〜1500、及び(C)残存
酢酸ビニルモノマー5ppm以下の特性を有するポリ酢
酸ビニル樹脂は、例えば以下の方法で提供される。The (A) of the present invention has an average particle diameter of 50 to 1000.
The polyvinyl acetate resin having the properties of μm, (B) a degree of polymerization of 300 to 1500, and (C) a residual vinyl acetate monomer of 5 ppm or less is provided, for example, by the following method.
【0008】酢酸ビニルモノマーを重合触媒、懸濁安定
剤および重合度調節剤の存在下、水系分散媒中で重合
し、重合終了後 スラリーを減圧し未反応酢酸ビニルモ
ノマーを除去することにより製造される。[0008] A vinyl acetate monomer is polymerized in an aqueous dispersion medium in the presence of a polymerization catalyst, a suspension stabilizer and a polymerization degree regulator, and after the polymerization, the slurry is depressurized to remove unreacted vinyl acetate monomer. You.
【0009】重合に使用される重合触媒はとして、アゾ
イソブチロニトリルに代表されるアゾ系重合触媒あるい
はラウロイロパーオキサイドに代表される有機過酸化物
系重合触媒等がある。重合されたポリ酢酸ビニル樹脂の
着色等の品質面から有機過酸化物系触媒が好ましい。懸
濁安定剤は通常エチレン性ニ重結合を有するビニルモノ
マーの懸濁重合に使用される懸濁安定剤であればいずれ
も使用でき、例えばポリビニルアルコール系樹脂、ヒド
ロキシプロピルメチルセルロースに代表されるセルロー
スエーテル類、及びポリビニルピロリドン等がありこれ
らを併用することもできる。Examples of the polymerization catalyst used in the polymerization include an azo polymerization catalyst represented by azoisobutyronitrile and an organic peroxide polymerization catalyst represented by lauroyl peroxide. Organic peroxide catalysts are preferred from the viewpoint of quality such as coloring of the polymerized polyvinyl acetate resin. Any suspension stabilizer can be used as long as it is a suspension stabilizer usually used for suspension polymerization of a vinyl monomer having an ethylenic double bond, for example, a polyvinyl alcohol resin, a cellulose ether represented by hydroxypropylmethylcellulose. And polyvinylpyrrolidone, and these can be used in combination.
【0010】重合度調節剤としては、アセトアルデヒド
に代表されるアルデヒド類、アセトンに代表されるケト
ン類、2−メルカプトアルコールに代表されるメルカプ
タン類、イソプロピルアルコールに代表されるアルコー
ル類等がある。更に本発明を得るのにアルコール系溶剤
を併用してもよい。アルコール系溶剤としては、メチル
アルコール、エチルアルコール、及びイソプロピルアル
コール等である。その中でもチューインガムの製造に用
いることを考慮するとエチルアルコールが特に好まし
い。As the polymerization degree regulator, there are aldehydes represented by acetaldehyde, ketones represented by acetone, mercaptans represented by 2-mercapto alcohol, alcohols represented by isopropyl alcohol, and the like. Further, an alcohol solvent may be used in combination to obtain the present invention. Examples of the alcohol-based solvent include methyl alcohol, ethyl alcohol, and isopropyl alcohol. Among them, ethyl alcohol is particularly preferable in consideration of use in the production of chewing gum.
【0011】[0011]
【実施例】以下、実施例をあげて本発明を説明するが、
本発明はこれら実施例には限定されないものである。
尚、以下「部」とあるのは重量部である。Hereinafter, the present invention will be described with reference to examples.
The present invention is not limited to these examples.
Hereinafter, “parts” means parts by weight.
【0012】実施例1 撹拌機付き200リットルのオートクレーブに、純水2
70部、酢酸ビニルモノマー100部、部分ケン化ポリ
ビニルアルコール0.1部、ラウロイルパーオキサイド
0.3部、ノルマルブチルアルデヒド1.2部を仕込
み、重合温度62℃で7時間重合した。次にスラリーを
撹拌しながら温度65℃で減圧し、未反応酢酸ビニルモ
ノマーを除去した。次いで、スラリーを脱水乾燥し、粒
子状のポリ酢酸ビニル樹脂を得た。得られたポリ酢酸ビ
ニル樹脂の平均粒子径245μm、重合度820、残存
酢酸ビニルモノマーは3ppm未満であった。このポリ
酢酸ビニル樹脂100部に、マイクロクリスタリンワッ
クス30部、ポリイソブチレン30部、炭酸カルシウム
8部をパドル式10リットルのニーダーに投入し、ジャ
ケット温度110℃、回転数100rpmの条件下で練
成した。ガムベースとしての評価法及びその結果を表1
に示す。Example 1 Pure water 2 was placed in a 200-liter autoclave equipped with a stirrer.
70 parts, 100 parts of vinyl acetate monomer, 0.1 part of partially saponified polyvinyl alcohol, 0.3 part of lauroyl peroxide, and 1.2 parts of normal butyraldehyde were charged and polymerized at a polymerization temperature of 62 ° C. for 7 hours. Next, the pressure was reduced at a temperature of 65 ° C. while stirring the slurry to remove unreacted vinyl acetate monomer. Next, the slurry was dehydrated and dried to obtain a particulate polyvinyl acetate resin. The resulting polyvinyl acetate resin had an average particle size of 245 μm, a degree of polymerization of 820, and a residual vinyl acetate monomer of less than 3 ppm. To 100 parts of this polyvinyl acetate resin, 30 parts of microcrystalline wax, 30 parts of polyisobutylene, and 8 parts of calcium carbonate were put into a paddle type 10 liter kneader, and kneaded under the conditions of a jacket temperature of 110 ° C. and a rotation speed of 100 rpm. . Table 1 shows the evaluation method as a gum base and the results.
Shown in
【0013】[0013]
【表1】 [Table 1]
【0014】また、分析方法及び評価方法は、以下のと
おりである。 1.分析方法 重合度 JIS K6725「ポリ酢酸ビニル
の試験方法」に準ずる 平均粒子径 標準篩を用いてロータップ篩振とう機
で分級し、篩下量50重量%の粒子径を用いる。 残存酢ビモノマー量 食品添加物公定書 第七版に準
ずる。 2.チューインガムベースの評価方法 配合 酢酸ビニル樹脂 100部 マイクロクリスタンワックス 30部 ポリイソブテン 30部 炭酸カルシウム 8部 練成 10リットルニーダーでジャケット温度110℃、回転数100 rpmで練成する。 評価項目と評価方法:詳細は表2に示す。The analysis method and the evaluation method are as follows. 1. Analysis method Degree of polymerization Average particle diameter according to JIS K6725 "Testing method for polyvinyl acetate" Classify using a standard tap sieve with a low tap sieve shaker, and use a particle diameter of 50% by weight under the sieve. Residual vinegar bimonomer amount Same as the official edition of Food Additives, Seventh Edition. 2. Evaluation method of chewing gum base Compounding 100 parts of vinyl acetate resin 30 parts of microcrystalline wax 30 parts of polyisobutene 8 parts of kneading 8 parts of kneading Kneading at a jacket temperature of 110 ° C. and a rotation speed of 100 rpm with a 10 liter kneader. Evaluation items and evaluation methods: Details are shown in Table 2.
【0015】[0015]
【表2】 [Table 2]
【0016】<判定> ◎ 特に良い ○ 良い △ 普通 × 悪い ×× 特に悪い<Judgment> ◎ Particularly good ○ Good △ Normal × Bad ×× Particularly bad
【0017】実施例2 ノルマルブチルアルデヒドを0.7部、部分ケン化ポリ
ビニルアルコールを0.03部に変えた以外は実施例1
と同様に行った。得られたポリ酢酸ビニルの平均粒子径
は790μm、重合度1310、残存酢酸ビニルモノマ
ーは3ppm未満であった。これを実施例1と同じ方法
でガムベースとしての評価を行った。その結果を表1に
示す。Example 2 Example 1 was repeated except that 0.7 parts of normal butyraldehyde and 0.03 parts of partially saponified polyvinyl alcohol were used.
The same was done. The average particle diameter of the obtained polyvinyl acetate was 790 μm, the degree of polymerization was 1310, and the residual vinyl acetate monomer was less than 3 ppm. This was evaluated as a gum base in the same manner as in Example 1. Table 1 shows the results.
【0018】実施例3 ノルマルブチルアルデヒドを4.0部、部分ケン化ポリ
ビニルアルコールを0.15部、ラウロイルパーオキサ
イドを0.4部に変えた以外は実施例1と同様に行っ
た。得られたポリ酢酸ビニルの平均粒子径は255μ
m、重合度310、残存酢酸ビニルモノマーは3ppm
未満であった。これを実施例1と同じ方法でガムベース
としての評価を行った。その結果を表1に示す。Example 3 The procedure of Example 1 was repeated except that normal butyraldehyde was changed to 4.0 parts, partially saponified polyvinyl alcohol was changed to 0.15 parts, and lauroyl peroxide was changed to 0.4 parts. The average particle size of the obtained polyvinyl acetate is 255 μm.
m, degree of polymerization 310, residual vinyl acetate monomer 3 ppm
Was less than. This was evaluated as a gum base in the same manner as in Example 1. Table 1 shows the results.
【0019】実施例4 部分ケン化ポリビニルアルコールを0.8部に変えた以
外は、実施例1と同様に行った。得られたポリ酢酸ビニ
ルの平均粒子径は55μm、重合度810、残存酢酸ビ
ニルモノマーは3ppm未満であった。これを実施例1
と同じ方法でガムベースとしての評価を行った。その結
果を表1に示す。Example 4 The procedure of Example 1 was repeated except that the partially saponified polyvinyl alcohol was changed to 0.8 part. The average particle diameter of the obtained polyvinyl acetate was 55 μm, the degree of polymerization was 810, and the amount of residual vinyl acetate monomer was less than 3 ppm. Example 1
The evaluation as a gum base was performed in the same manner as described above. Table 1 shows the results.
【0020】比較例1 部分ケン化ポリビニルアルコールを1.5部に変えた以
外は、実施例1と同様に行った。得られたポリ酢酸ビニ
ルの平均粒子径は25μm、重合度800、残存酢酸ビ
ニルモノマーは3ppm未満であった。これを実施例1
と同じ方法でガムベースとしての評価を行った。その結
果を表1に示す。Comparative Example 1 The procedure of Example 1 was repeated, except that the partially saponified polyvinyl alcohol was changed to 1.5 parts. The average particle diameter of the obtained polyvinyl acetate was 25 μm, the degree of polymerization was 800, and the residual vinyl acetate monomer was less than 3 ppm. Example 1
The evaluation as a gum base was performed in the same manner as described above. Table 1 shows the results.
【0021】比較例2 ノルマルブチルアルデヒドを6.0部、部分ケン化ポリ
ビニルアルコールを0.2部、ラウロイルパーオキサイ
ドを0.5部に変えた以外は、実施例1と同様に行っ
た。スラリーを脱水乾燥する工程で粒子同士付着し塊と
なった。得られたポリ酢酸ビニル樹脂の重合度は21
0、残存酢酸ビニルモノマーは3ppm未満であった。
これを実施例1と同じ方法でガムベースとしての評価を
行った。その結果を表1に示す。Comparative Example 2 The procedure of Example 1 was repeated, except that 6.0 parts of normal butyraldehyde, 0.2 part of partially saponified polyvinyl alcohol, and 0.5 part of lauroyl peroxide were used. In the step of dehydrating and drying the slurry, the particles adhered to each other to form a lump. The polymerization degree of the obtained polyvinyl acetate resin is 21.
0, the residual vinyl acetate monomer was less than 3 ppm.
This was evaluated as a gum base in the same manner as in Example 1. Table 1 shows the results.
【0022】比較例3 ノルマルブチルアルデヒドを0.4部に変えた以外は、
実施例1と同様に行った。得られたポリ酢酸ビニルの平
均粒子径は240μm、重合度1810、残存酢酸ビニ
ルモノマーは3ppm未満であった。これを実施例1と
同じ方法でガムベースとしての評価を行った。その結果
を表1に示す。Comparative Example 3 Except that normal butyraldehyde was changed to 0.4 part,
Performed in the same manner as in Example 1. The average particle diameter of the obtained polyvinyl acetate was 240 μm, the degree of polymerization was 1810, and the amount of the residual vinyl acetate monomer was less than 3 ppm. This was evaluated as a gum base in the same manner as in Example 1. Table 1 shows the results.
【0023】比較例4 撹拌機付き200リットルのオートクレーブに、酢酸ビ
ニルモノマー370部、ラウロイルパーオキサイド0.
2部、ノルマルブチルアルデヒド2.5部を仕込み、重
合温度62℃で7時間塊状重合した。次に重合物を撹拌
しながら温度65℃で減圧し、未反応酢酸ビニルモノマ
ーを除去した。次いで塊状重合物をステンレス製容器に
取り出し、乾燥し塊状物のポリ酢酸ビニル樹脂を得た。
得られたポリ酢酸ビニル樹脂の重合度は790、残存酢
酸ビニルモノマーは108ppmであった。これを実施
例1と同じ方法でガムベースとしての評価を行った。そ
の結果を表1に示す。Comparative Example 4 In a 200-liter autoclave equipped with a stirrer, 370 parts of vinyl acetate monomer and lauroyl peroxide 0.1% were added.
2 parts and 2.5 parts of normal butyraldehyde were charged and bulk polymerization was performed at a polymerization temperature of 62 ° C. for 7 hours. Next, the pressure was reduced at a temperature of 65 ° C. while stirring the polymer to remove unreacted vinyl acetate monomer. Next, the bulk polymer was taken out into a stainless steel container and dried to obtain a bulk polyvinyl acetate resin.
The polymerization degree of the obtained polyvinyl acetate resin was 790, and the residual vinyl acetate monomer was 108 ppm. This was evaluated as a gum base in the same manner as in Example 1. Table 1 shows the results.
【0024】比較例5 撹拌機付き200リットルのオートクレーブに、酢酸ビ
ニルモノマー250部、エチルアルコール120部、ラ
ウロイルパーオキサイド0.4部を仕込み、重合温度6
2℃で7時間溶液重合した。次に重合物を撹拌しながら
温度65℃で減圧し、未反応酢酸ビニルモノマーを除去
した。次いで溶液重合物をステンレス製容器に取り出
し、乾燥し塊状物のポリ酢酸ビニル樹脂を得た。得られ
たポリ酢酸ビニル樹脂の重合度は1320、残存酢酸ビ
ニルモノマーは52ppmであった。これを実施例1と
同じ方法でガムベースとしての評価を行った。その結果
を表1に示す。Comparative Example 5 A 200-liter autoclave equipped with a stirrer was charged with 250 parts of vinyl acetate monomer, 120 parts of ethyl alcohol, and 0.4 part of lauroyl peroxide.
Solution polymerization was carried out at 2 ° C. for 7 hours. Next, the pressure of the polymer was reduced at 65 ° C. while stirring, to remove unreacted vinyl acetate monomer. Next, the solution polymer was taken out into a stainless steel container and dried to obtain a lump polyvinyl acetate resin. The polymerization degree of the obtained polyvinyl acetate resin was 1320, and the residual vinyl acetate monomer was 52 ppm. This was evaluated as a gum base in the same manner as in Example 1. Table 1 shows the results.
【0025】[0025]
【発明の効果】以上のとおり、本発明のポリ酢酸ビニル
樹脂は、ガムベース製造時のハンドリング性に優れ、か
つ極めて残存酢酸ビニルモノマーが少ない為、安全性、
及び衛生性に優れる。As described above, the polyvinyl acetate resin of the present invention has excellent handling properties in the production of a gum base, and has very little residual vinyl acetate monomer.
And excellent hygiene.
Claims (2)
(B)重合度300〜1500、及び(C)残存酢酸ビ
ニルモノマー5ppm以下の特性を有するポリ酢酸ビニ
ル樹脂。(A) an average particle diameter of 50 to 1000 μm,
(B) A polyvinyl acetate resin having a degree of polymerization of 300 to 1500 and (C) a residual vinyl acetate monomer of 5 ppm or less.
とを特徴とする請求項1記載のポリ酢酸ビニル樹脂。2. The polyvinyl acetate resin according to claim 1, which is used for producing chewing gum.
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| JP2001000489A JP4059632B2 (en) | 2001-01-05 | 2001-01-05 | Polyvinyl acetate resin for chewing gum |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2001000489A JP4059632B2 (en) | 2001-01-05 | 2001-01-05 | Polyvinyl acetate resin for chewing gum |
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| JP2002201220A true JP2002201220A (en) | 2002-07-19 |
| JP4059632B2 JP4059632B2 (en) | 2008-03-12 |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2020150957A (en) * | 2015-10-28 | 2020-09-24 | インターコンチネンタル グレート ブランズ エルエルシー | Method for preparing an encapsulated composition for use in an edible composition |
Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3826847A (en) * | 1970-10-21 | 1974-07-30 | Lotte Co Ltd | Process for preparation of flavor durable chewing gum |
| JPS56167707A (en) * | 1980-05-12 | 1981-12-23 | Tokuyama Sekisui Kogyo Kk | Production of vinyl acetate polymer |
| JPS61148209A (en) * | 1984-12-21 | 1986-07-05 | Kuraray Co Ltd | Production of polyvinyl ester based polymer having high polymerization degree and polyvinyl alcohol based polymer having high polymerization degree |
| JPH02408A (en) * | 1986-01-07 | 1990-01-05 | Warner Lambert Co | Edible solvent free seal composition |
-
2001
- 2001-01-05 JP JP2001000489A patent/JP4059632B2/en not_active Expired - Fee Related
Patent Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3826847A (en) * | 1970-10-21 | 1974-07-30 | Lotte Co Ltd | Process for preparation of flavor durable chewing gum |
| JPS56167707A (en) * | 1980-05-12 | 1981-12-23 | Tokuyama Sekisui Kogyo Kk | Production of vinyl acetate polymer |
| JPS61148209A (en) * | 1984-12-21 | 1986-07-05 | Kuraray Co Ltd | Production of polyvinyl ester based polymer having high polymerization degree and polyvinyl alcohol based polymer having high polymerization degree |
| JPH02408A (en) * | 1986-01-07 | 1990-01-05 | Warner Lambert Co | Edible solvent free seal composition |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2020150957A (en) * | 2015-10-28 | 2020-09-24 | インターコンチネンタル グレート ブランズ エルエルシー | Method for preparing an encapsulated composition for use in an edible composition |
| JP7321978B2 (en) | 2015-10-28 | 2023-08-07 | インターコンチネンタル グレート ブランズ エルエルシー | Method for preparing encapsulated compositions for use in edible compositions |
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| JP4059632B2 (en) | 2008-03-12 |
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