JPH0443624B2 - - Google Patents

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Publication number
JPH0443624B2
JPH0443624B2 JP63254540A JP25454088A JPH0443624B2 JP H0443624 B2 JPH0443624 B2 JP H0443624B2 JP 63254540 A JP63254540 A JP 63254540A JP 25454088 A JP25454088 A JP 25454088A JP H0443624 B2 JPH0443624 B2 JP H0443624B2
Authority
JP
Japan
Prior art keywords
dextrin
roasted
amylase
add
hours
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 - Lifetime
Application number
JP63254540A
Other languages
Japanese (ja)
Other versions
JPH02100695A (en
Inventor
Kazuhiro Oosumi
Takao Hanno
Kazuyuki Inada
Isao Matsuda
Yasuo Katsuta
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Matsutani Chemical Industries Co Ltd
Original Assignee
Matsutani Chemical Industries Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Matsutani Chemical Industries Co Ltd filed Critical Matsutani Chemical Industries Co Ltd
Priority to JP63254540A priority Critical patent/JPH02100695A/en
Priority to EP89309269A priority patent/EP0368451B1/en
Priority to DE68914401T priority patent/DE68914401T2/en
Priority to KR1019890013379A priority patent/KR0135075B1/en
Publication of JPH02100695A publication Critical patent/JPH02100695A/en
Publication of JPH0443624B2 publication Critical patent/JPH0443624B2/ja
Priority to US08/438,113 priority patent/US5620873A/en
Granted legal-status Critical Current

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  • Coloring Foods And Improving Nutritive Qualities (AREA)
  • Preparation Of Compounds By Using Micro-Organisms (AREA)

Description

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

〔産業上の利用分野〕 本発明は焙焼デキストリンを酸素処理すること
により、食品用の難消化性デキストリンを製造す
る方法に関する。 〔従来技術〕 焙焼デキストリンは周知の通り澱粉を高熱処理
したものであつて、その処理により澱粉分子は加
水分解及び再重合が起こり、複雑な構造を呈して
いると言われ、水溶性になると共に、難消化性の
ものがかなりの割合をしめている。 一方近時日本人の食生活が変化し、多様化した
結果、繊維分の摂取量が目立つて減少しており、
この繊維分の欠乏は成人病の起因の一つにも上げ
られており、食物繊維の必要性が注目を集め、蛋
白質、糖類、脂質、ビタミン、ミネラルに次ぐ六
番目の栄養素と言われる様になつて来た。 現在食物繊維としては植物性のものや、動物性
のもので、水溶性、不溶性と色々挙げられてお
り、又合成品としてポリデキストロースが挙げら
れている。これらはぶどう糖或いはその誘導体、
又ぶどう糖以外の糖類が多数結合した形の繊維状
をなしたもの、或いは蛋白質多糖と言つたもので
形作られている。その構造は複雑でアミラーゼに
よる消化が困難で、体外に排出されるため繊維の
効果があるとされる。 〔発明が解決しようとする課題〕 本発明者は従来から食物繊維について研究を続
けて来たが、この研究に於いて、従来そり激しい
刺激臭や望ましくない味覚のために全く食物繊維
として考えても見られなかつた焙焼デキストリン
を、新しい食物繊維として利用することが出来な
いであろうかという全く新しい着想に至つた。こ
の新しい着想に基づきこれを実現するために引き
続き鋭意研究し、焙焼デキストリンの上記食物繊
維としての難点を解消すると共に、食物繊維とし
て本来具有する難消化性を少なくともそのまま維
持出来る手段の開発に着手した。 従つて本発明が解決しようとする課題は、上記
新しい着想を実現し、食物繊維として充分に使用
しうる難消化性物質を焙焼デキストリンから製造
しうる方法を開発することである。 〔課題を解決するための手段〕 この課題は、焙焼デキストリンを水に溶解し、
これにα−アミラーゼを作用させ、次いでトラン
スグルコシダーゼを必要に応じβ−アミラーゼを
共存させつつ作用させることにより解決される。 〔発明の構成並びに作用〕 本発明に於いては焙焼デキストリンを先ずα−
アミラーゼで処理してデキストリンをα−リミツ
トデキストリンまで進行せしめて、焙焼デキスト
リンの有する刺激臭や好ましくない味覚を解消す
る。次いでトランスグルコシダーゼを作用させて
低下した難消化性を復元乃至更に一段と向上させ
るものである。 以下に本発明をその製造法に従つて順に説明す
る。 先ず焙焼デキストリンを原料とするが、この焙
焼デキストリンとしては、従来から知られている
ものが使用できるが、特に本発明に於いては、そ
の刺激臭や好ましくない味覚を効率良く除去する
には、次のような方法で製造された焙焼デキスト
リンを使用するのが好ましい。即ち原料澱粉に鉱
酸好ましくは塩酸の水溶液を加え、次いで水分量
が5%前後になるまで予備乾燥し、続いて焙焼し
て製造したものが好ましい。この際の原料澱粉と
しては、広く各種のものがいずれも使用出来、た
とえば馬鈴薯、トーモロコシ、キヤツサバなど何
れでもよく、又食品用加工澱粉として市販されて
いるものでよい。これらの原料澱粉に硫酸、塩
酸、硝酸などの鉱酸好ましくは塩酸を好ましくは
その濃度を1重量%程度となして原料に対して数
重量%の量を添加好ましくは噴霧して均一になる
様良く混合し、100〜120℃程度で予備乾燥する。
この予備乾燥では澱粉の水分を5%前後まで乾燥
する。続いて150℃〜220℃に温度を上げて、1時
間〜5時間程度焙焼して焙焼デキストリンとす
る。ここで出来た焙焼デキストリンはDE(デキス
トロース当量)1〜10位のものが好ましい。 この際本発明に於いては澱粉に単糖類やオリゴ
糖を添加することが出来る。これ等糖類の添加は
難消化性デキストリンを増加させる目的でなさ
れ、通常その糖含有量が40〜60重量%の糖液を、
澱粉に対し10重量%以下程度添加する。 次にこの焙焼デキストリンを水に溶かし30〜50
重量%の液となし、中和してPH5.5〜6.5好ましく
は5.8となし、市販のα−アミラーゼ(カビ由来
のもの、細菌由来のもの等何れでもよい)を焙焼
デキストリンに対して0.05〜0.2重量%添加して
該アミラーゼの作用温度85℃〜100℃前後となし、
30分〜2時間保持する。これにより酵素によるデ
キストリンの分解がα−リミツトデキストリンま
で進む。次いで、温度を120℃まで上げα−アミ
ラーゼの酵素作用を終了させる。この後液温を下
げ、PHを調整し、トランスグルコシダーゼ(市販
品)を元の焙焼デキストリンに対して0.05〜0.2
重量%添加し、24時間〜48時間作用させる。この
反応は液中に存在することがあるぶどう糖やオリ
ゴ糖の様な小さい分子を大きい分子の方へ再重合
させと共に、焙焼デキストリンの複雑な構造を更
に増加させるものである。かくして所定の時間後
一旦温度を上げて(たとえば80℃前後に)トラン
スグルコシダーゼの酵素作用を終了させる。尚こ
のトランスグルコシダーゼの添加のβ−アミラー
ゼ(市販品)を同時に作用させてもよい。これに
より反応が促進される。 以上の操作により得られた液を活性炭脱色、イ
オン交換樹脂脱塩等の通常の澱粉糖の精製工程を
通し、濃縮、噴霧乾燥して異臭、刺激味のない食
品用に利用出来る難消化性デキストリン粉末を得
ることが出来る。 〔実施例〕 以下実施例により本発明を説明する。 但し、難消化性デキストリン含有の測定は次の
方法で行つた。 難消化性デキストリンの含有の測定方法 サンプル1gを精秤し、水50mlを加えPH5.8とな
した後、α−アミラーゼ(ターマミル120、ノ
ボ社製)0.1mlを添加し、9.5℃、30分間反応させ
る。つぎに冷却後、PH4.5に調整しアミログルコ
シダーゼ(シグマ社製)0.1mlを添加し60℃、30
分間反応させた後、90℃まで昇温し反応を終了さ
せた。終了液は濾過後、5%まで濃縮してHPLC
に供し、糖組成より生成したグルコース量を測定
した。そして、次の式より難消化デキストリンの
含量を求めた。 難消化性デキストリン含量% =100−生成グルコース% 実施例 1 市販の馬鈴薯澱粉100gに1.0%塩酸溶液5mlを
加圧空気を用いてスプレーし、更にミキサーにて
均一に混合後、アルミバツトに入れ、乾燥器で
110℃で1時間予備乾燥し、次いで、150℃で3時
間焙焼した。得られた焙焼デキストリンのDEは
6.8、粘度160cps(濃度50%、30℃)、難消化性デ
キストリン含量57%であつた。 上記の方法で調製した焙焼デキストリン100g
に100gの熱水を加え溶解し、IN水酸化ナトリウ
ム中和PH5.8、更にα−アミラーゼ(ターマミル
120)0.1%を添加し95℃で反応、1時間後115
℃まで昇温して反応を終了させた。次にPH5.5、
温度55℃に糖液を調製し、β−アミラーゼ(天野
製薬製)0.05%、トランスグルコシダーゼ(天野
製薬製)0.1%を添加し、24時間反応させ次のよ
うなデキストリンを得た。 糖組成DP1 15.8%、DP2 10.7%(マルトース
0.6、コージビオース0.3、イソマルトース9.8%)、
DP3 5.8% DP4以上68.2%粘度 75cps(濃度50
%、30℃)、難消化性デキストリン含量72% 実施例 2 タピオカ澱粉100gに1.2%塩酸4ml、50%グル
コース水溶液15gを加圧空気を用いてスプレー
し、実施例1と同様の条件で予備乾燥を行い、次
に170℃で2時間焙焼した。得られた焙焼デキス
トリンのDEは2.0、粘度250cps(50%、30℃)、難
消化性デキストリン含量 45%であつた。 上記の方法で調製した焙焼デキストリン100g
に200c.c.の熱水を加え溶解し、炭酸カルシウム粉
末で中和、更にα−アミラーゼ(ビオザイムC、
天野製薬製) 0.2%を添加し60℃で反応、3時
間後 85℃まで昇温して反応を終了させた。次に
濃縮して55%濃度に調製し、トランスグルコシダ
ーゼ(天野製薬製)0.1%を添加し、48時間反応
させ次のようなデキストリンを得た。糖組成DP1
22.5%、DP2 9.4%(マルトース1.3%、コージビ
オース0.7%、イソマルトース7.4%)、DP3 3.9%
(マルトトリオース0.3%、パノース1.7%、イソ
マルトトリオース1.9%)DP4以上64.2% 粘度53.5cps(濃度50%、30℃)、難消化性デキ
ストリン含量65% 参考例 1 タピオカ澱粉10000Kgを硫酸ナトリウム1500Kg
含む水12000に懸濁せしめ、撹はん下、3%水
酸化ナトリウム水溶液3000を滴下し、更にプロ
ピレンオキサイド800を加え、43℃で20時間反
応後、硫酸で中和し、水洗、遠心分離機で脱水、
フラツシユドライヤーで乾燥してヒドロキシプロ
ピル澱粉を得た。ここで得たヒドロキシプロピル
澱粉は水分12.5%、DS.0.145であつた。 実施例 3 参考例1で得たヒドロキシプロピール澱粉5000
Kgをリボン式ミキサーに入れ、攪はんしながら
1.2%塩酸200、50%に濃度調整した市販ハイマ
ルトースシラツプ(MC−75、日本食品化工製)
500Kgを加圧空気を用いてスプレーし、1時間混
合、粉砕機を通して均一にした後、更にリボン式
ミキサー中で12時間熟成した。この混合物をフラ
ツシユドライヤーで水分3.5%に予備乾燥した後、
ロータリーキルン式焙焼機に連続的に投入し、
175%で1.5時間 焙焼機中に滞留せしめ焙焼し
た。得られた焙焼デキストリンのDEは9.0で粘度
200cps(50%、30℃)、難消化性デキストリン含量
45%であつた。 上記の方法で調製した焙焼デキストリン2000Kg
に4000の熱水を加え溶解し20%水酸化ナトリウ
ムで、PH6.0に調整し、α−アミラーゼ(ターマ
ミル60 ノボ社製)0.3%を添加し95℃で反応、
1時間後115℃まで昇温して反応を終了させて55
%濃度に調製し、β−アミラーゼ(天野製薬製)
0.2%、トランスグルコシダーゼ(天野製薬製)
48時間反応させ次のような糖組成のデキストリ
ンを得た。 DP1 7.4%、 DP2 8.7%(マルトース1.1、コ
ージビオース0.6%、イソマルトース7.0%)、DP3
6.3% (マルトトリオース0.7% パノース2.7
%、イソマルトトリオース2.9%)DP4以上77.6%
粘度70cps (50%、30℃)、難消化性デキスト
リン 60% 実施例 4 市販の馬鈴薯澱粉5000Kgをリボン式ミキサーに
入れ、攪はんいながら1.0%塩酸200をスプレ
ー、続いて粉砕機を通し均一にした後、更にリボ
ン式ミキサー中で10時間熟成した。この混合物を
フラツシユドライヤーで水分3%に予備乾燥した
後、ロータリーキルン式焙焼機に連続的に投入
し、185℃で2時間焙焼した。得られた焙焼デキ
ストリンのDEは7.8、粘度120cps(50%、30℃)、
難消化性デキストリン含量は56% 上記方法で調製した焙焼デキストリン2000Kgに
4000の熱水を加え溶解し20%水酸化ナトリウム
でPH6.0に調整し、α−アミラーゼ(ターマミル
60、ノボ社製)0.2%を添加し95℃で1時間加
水分解。次に50%まで濃縮して、0.2%トランス
グルコシダーゼを添加し、48時間反応。反応終了
後、脱色、脱塩等の精製を行い次のようなデキス
トリンを得た。 DP1 10.6%、DP2 9.4%(マルトース0.3%、
コージビオース0.7%、イソマルトース7.7%)、
DP3 5.2%(マルトトリオース0.6%、パノース
2.0%、イソマルトトリオース2.6%)DP4以上
74.8% 粘度55cps(50%、30℃)、難消化性デキストリン
67% 実施例 5 実施例4で得た難消化性デキストリンを使用し
て次の処方の炭酸飲料を製造し、官能検査、及び
食物繊維としての効果を調査した結果、味も良好
で便秘改善効果も認めた。 難消化性デキストリン 50g グラニユー糖 125g クエン酸 1.5g クエン酸Na 0.1g ビタミンC 0.15g 炭酸水 520g 水 385g 便秘改善効果テスト 便秘傾向の10名の男女(各5名)に上記飲料
200c.c./日与えテストを行つた結果、2日後には
8名が正常な便性状に改善された。
[Industrial Application Field] The present invention relates to a method for producing indigestible dextrin for food by treating roasted dextrin with oxygen. [Prior art] As is well known, roasted dextrin is starch treated with high heat.As a result of this treatment, starch molecules are hydrolyzed and repolymerized, and are said to have a complex structure, making them water-soluble. In addition, a large proportion of the food is indigestible. On the other hand, as the Japanese diet has changed and become more diverse in recent years, the intake of fiber has decreased noticeably.
This lack of fiber has been cited as one of the causes of adult diseases, and the necessity of dietary fiber has attracted attention, and it has come to be called the sixth nutrient after protein, sugars, lipids, vitamins, and minerals. I'm getting used to it. Currently, there are a variety of dietary fibers, including plant-based and animal-based fibers, water-soluble and insoluble, and polydextrose as a synthetic product. These are glucose or its derivatives,
It is also made of a fibrous material in which many sugars other than glucose are bonded together, or a protein polysaccharide. Its structure is complex, making it difficult to digest with amylase, and it is excreted from the body, so it is said to have the effect of fiber. [Problems to be Solved by the Invention] The present inventor has been conducting research on dietary fiber for a long time, and in this research, he discovered that fibers have been considered as dietary fibers at all due to their strong irritating odor and undesirable taste. This led to a completely new idea that it might be possible to use roasted dextrin, which had never been seen before, as a new dietary fiber. Based on this new idea, we continued to conduct intensive research to realize this goal, and we began to develop a means to solve the above-mentioned difficulties of roasted dextrin as a dietary fiber, and to at least maintain its inherent indigestibility as a dietary fiber. did. Therefore, the problem to be solved by the present invention is to realize the above-mentioned new idea and develop a method for producing an indigestible substance from roasted dextrin that can be sufficiently used as dietary fiber. [Means for solving the problem] This problem is solved by dissolving roasted dextrin in water,
This problem can be solved by allowing α-amylase to act on this, and then using transglucosidase in the presence of β-amylase if necessary. [Structure and operation of the invention] In the present invention, roasted dextrin is first converted into α-
The dextrin is treated with amylase to progress to α-limit dextrin, thereby eliminating the pungent odor and unpleasant taste of roasted dextrin. Next, transglucosidase is applied to restore or even further improve the reduced indigestibility. The present invention will be explained below in order according to its manufacturing method. First, roasted dextrin is used as a raw material. As this roasted dextrin, conventionally known ones can be used, but especially in the present invention, in order to efficiently remove the irritating odor and unpleasant taste, It is preferable to use roasted dextrin produced by the following method. That is, it is preferable to add an aqueous solution of a mineral acid, preferably hydrochloric acid, to the raw material starch, then pre-dry it until the moisture content becomes around 5%, and then roast it. As the raw material starch in this case, any of a wide variety of starches can be used, such as potato, corn, or mackerel, or any one commercially available as processed starch for food. A mineral acid such as sulfuric acid, hydrochloric acid, or nitric acid, preferably hydrochloric acid, is added to these raw starches in an amount of several weight percent based on the raw material, preferably at a concentration of about 1 weight percent, preferably by spraying to make it uniform. Mix well and pre-dry at about 100-120℃.
In this pre-drying, the water content of starch is dried to around 5%. Subsequently, the temperature is raised to 150°C to 220°C and roasted for about 1 to 5 hours to obtain roasted dextrin. The roasted dextrin produced here preferably has a DE (dextrose equivalent) of 1 to 10. At this time, in the present invention, monosaccharides and oligosaccharides can be added to the starch. These sugars are added for the purpose of increasing indigestible dextrin, and usually the sugar solution with a sugar content of 40 to 60% by weight is
Add about 10% by weight or less to starch. Next, dissolve this roasted dextrin in water and add 30 to 50%
% by weight, neutralize to pH 5.5 to 6.5, preferably 5.8, and add commercially available α-amylase (either mold-derived, bacterial-derived, etc.) to roasted dextrin at a concentration of 0.05% by weight. By adding ~0.2% by weight, the action temperature of the amylase is around 85°C to 100°C,
Hold for 30 minutes to 2 hours. This causes the enzymatic decomposition of dextrin to progress to α-limit dextrin. Next, the temperature is raised to 120°C to terminate the enzymatic action of α-amylase. After this, lower the liquid temperature, adjust the pH, and add transglucosidase (commercially available) to 0.05 to 0.2 of the original roasted dextrin.
% by weight and allowed to act for 24 to 48 hours. This reaction repolymerizes small molecules such as glucose and oligosaccharides that may be present in the liquid into larger molecules and further increases the complex structure of the torrefied dextrin. After a predetermined period of time, the temperature is raised once (eg, to around 80°C) to terminate the enzymatic action of transglucosidase. Note that β-amylase (commercially available) may be added to this transglucosidase at the same time. This accelerates the reaction. The liquid obtained by the above procedure is concentrated and spray-dried through normal starch sugar purification processes such as activated carbon decolorization and ion exchange resin desalination to produce an indigestible dextrin that can be used for food products without off-odor or pungent taste. You can get powder. [Example] The present invention will be explained below with reference to Examples. However, the content of indigestible dextrin was measured by the following method. Method for measuring the content of indigestible dextrin: Accurately weigh 1 g of sample, add 50 ml of water to adjust the pH to 5.8, add 0.1 ml of α-amylase (Termamyl 120, manufactured by Novo), and heat at 9.5°C for 30 minutes. Make it react. Next, after cooling, adjust the pH to 4.5, add 0.1 ml of amyloglucosidase (manufactured by Sigma), and heat at 60℃ for 30 minutes.
After reacting for a minute, the temperature was raised to 90°C to terminate the reaction. After filtration, the finished liquid was concentrated to 5% and subjected to HPLC.
The amount of glucose produced was measured based on the sugar composition. Then, the content of indigestible dextrin was determined from the following formula. Indigestible dextrin content % = 100 - produced glucose % Example 1 100 g of commercially available potato starch was sprayed with 5 ml of 1.0% hydrochloric acid solution using pressurized air, mixed uniformly with a mixer, then placed in an aluminum vat and dried. In a vessel
It was pre-dried at 110°C for 1 hour and then roasted at 150°C for 3 hours. DE of the obtained roasted dextrin is
6.8, viscosity 160 cps (concentration 50%, 30°C), and indigestible dextrin content 57%. 100g of roasted dextrin prepared by the above method
Add 100g of hot water to dissolve, IN sodium hydroxide neutralization pH 5.8, and α-amylase (Termamil).
120) Add 0.1% and react at 95℃, after 1 hour 115
The reaction was terminated by raising the temperature to ℃. Next, PH5.5,
A sugar solution was prepared at a temperature of 55° C., 0.05% of β-amylase (manufactured by Amano Pharmaceuticals) and 0.1% of transglucosidase (manufactured by Amano Pharmaceuticals) were added, and the mixture was reacted for 24 hours to obtain the following dextrin. Sugar composition DP1 15.8%, DP2 10.7% (maltose
0.6, cordibiose 0.3, isomaltose 9.8%),
DP3 5.8% DP4 or higher 68.2% Viscosity 75 cps (concentration 50
%, 30℃), indigestible dextrin content 72% Example 2 100 g of tapioca starch was sprayed with 4 ml of 1.2% hydrochloric acid and 15 g of a 50% glucose aqueous solution using pressurized air, and pre-dried under the same conditions as Example 1. and then roasted at 170°C for 2 hours. The obtained roasted dextrin had a DE of 2.0, a viscosity of 250 cps (50%, 30°C), and an indigestible dextrin content of 45%. 100g of roasted dextrin prepared by the above method
Add 200c.c. of hot water to dissolve, neutralize with calcium carbonate powder, and add α-amylase (Biozyme C,
Amano Pharmaceutical Co., Ltd.) 0.2% was added and reacted at 60°C. After 3 hours, the temperature was raised to 85°C to terminate the reaction. Next, the mixture was concentrated to a concentration of 55%, 0.1% of transglucosidase (manufactured by Amano Pharmaceutical) was added, and the mixture was allowed to react for 48 hours to obtain the following dextrin. Sugar composition DP1
22.5%, DP2 9.4% (maltose 1.3%, cordibiose 0.7%, isomaltose 7.4%), DP3 3.9%
(Maltotriose 0.3%, Panose 1.7%, Isomaltotriose 1.9%) DP4 or higher 64.2% Viscosity 53.5 cps (concentration 50%, 30℃) Indigestible dextrin content 65% Reference example 1 10000 kg of tapioca starch was added to sodium sulfate 1500Kg
Suspend in water containing 12,000 ml, drop 3,000 ml of 3% sodium hydroxide aqueous solution under stirring, further add propylene oxide 800 ml, react at 43°C for 20 hours, neutralize with sulfuric acid, wash with water, and centrifuge. Dehydrate with
Hydroxypropyl starch was obtained by drying with a flash dryer. The hydroxypropyl starch obtained here had a moisture content of 12.5% and a DS.0.145. Example 3 Hydroxypropyl starch 5000 obtained in Reference Example 1
Kg into a ribbon mixer and while stirring.
Commercially available high maltose syrup (MC-75, manufactured by Nihon Shokuhin Kako) adjusted to 1.2% hydrochloric acid 200% and 50%.
500 kg was sprayed using pressurized air, mixed for 1 hour, homogenized through a grinder, and further aged in a ribbon mixer for 12 hours. After pre-drying this mixture with a flash dryer to a moisture content of 3.5%,
Continuously fed into a rotary kiln roaster,
It was allowed to stay in the roaster for 1.5 hours at 175% and roasted. The obtained roasted dextrin has a DE of 9.0 and a viscosity of
200cps (50%, 30℃), indigestible dextrin content
It was 45%. 2000Kg of roasted dextrin prepared by the above method
Add 4,000 ml of hot water to dissolve, adjust the pH to 6.0 with 20% sodium hydroxide, add 0.3% of α-amylase (Termamyl 60 manufactured by Novo), and react at 95°C.
After 1 hour, raise the temperature to 115℃ to complete the reaction.
% concentration and β-amylase (manufactured by Amano Pharmaceutical)
0.2%, transglucosidase (manufactured by Amano Pharmaceutical)
The reaction was carried out for 48 hours to obtain dextrin with the following sugar composition. DP1 7.4%, DP2 8.7% (maltose 1.1, cordibiose 0.6%, isomaltose 7.0%), DP3
6.3% (maltotriose 0.7% panose 2.7
%, isomaltotriose 2.9%) DP4 or higher 77.6%
Viscosity 70cps (50%, 30℃), indigestible dextrin 60% Example 4 Put 5000kg of commercially available potato starch into a ribbon mixer, spray with 1.0% hydrochloric acid 200% while stirring, and then pass through a pulverizer to homogenize. After that, it was further aged in a ribbon mixer for 10 hours. After pre-drying this mixture to a moisture content of 3% using a flash dryer, it was continuously charged into a rotary kiln roaster and roasted at 185°C for 2 hours. The DE of the obtained roasted dextrin was 7.8, the viscosity was 120 cps (50%, 30℃),
Indigestible dextrin content is 56% 2000 kg of roasted dextrin prepared by the above method
Add 4,000 ml of hot water to dissolve, adjust to PH6.0 with 20% sodium hydroxide, and add α-amylase (Termamyl).
60 (manufactured by Novo) was added at 0.2% and hydrolyzed at 95℃ for 1 hour. Next, concentrate to 50%, add 0.2% transglucosidase, and react for 48 hours. After the reaction was completed, purification such as decolorization and desalting was performed to obtain the following dextrin. DP1 10.6%, DP2 9.4% (maltose 0.3%,
cordibiose 0.7%, isomaltose 7.7%),
DP3 5.2% (maltotriose 0.6%, panose
2.0%, isomaltotriose 2.6%) DP4 or higher
74.8% viscosity 55cps (50%, 30℃), indigestible dextrin
67% Example 5 A carbonated drink with the following formulation was manufactured using the indigestible dextrin obtained in Example 4, and a sensory test and investigation of its effect as dietary fiber revealed that it had a good taste and was effective in improving constipation. also admitted. Indigestible dextrin 50g Granulated sugar 125g Citric acid 1.5g Sodium citrate 0.1g Vitamin C 0.15g Carbonated water 520g Water 385g Constipation improvement effect test The above drink was administered to 10 men and women (5 each) who tended to have constipation.
As a result of the 200c.c./day feeding test, 8 people's stools improved to normal after 2 days.

【表】 比較例 実施例4で得られた焙焼デキストリンと同等の
DE値を持つマルトデキストリン(パインデツク
ス#1、松谷化学社製)を50%まで濃縮して0.2
%トランスグルコシダーゼを添加して48時間反応
させた結果、次の様な糖を得た。 DP1 65% DP2 10.5%(マルトース2.3%、コ
ージビオース2.5%、イソマルトース5.7%)
DP3 6.2%(マルトトリオース 1.2%、パノース
3.8%、イソマルトトリオース1.2%) DP4以上
18.3% 難消化性デキストリン含量 5.0%であ
つた。
[Table] Comparative example: Same as the roasted dextrin obtained in Example 4.
Maltodextrin (Pinedex #1, manufactured by Matsutani Chemical Co., Ltd.) with DE value is concentrated to 50% and 0.2
As a result of adding % transglucosidase and reacting for 48 hours, the following sugars were obtained. DP1 65% DP2 10.5% (maltose 2.3%, cordibiose 2.5%, isomaltose 5.7%)
DP3 6.2% (maltotriose 1.2%, panose
3.8%, isomaltotriose 1.2%) DP4 or higher
The content of indigestible dextrin was 18.3% and 5.0%.

Claims (1)

【特許請求の範囲】 1 焙焼デキストリンを水に溶解し、これにα−
アミラーゼを作用させ、次いでトランスグルコシ
ダーゼを必要に応じβ−アミラーゼを共存させて
作用させる事を特徴とする難消化性デキストリン
の製造法。 2 焙焼デキストリンとして澱粉単独、或いはこ
れに単糖類及びオリゴ糖の少なくとも1種を混合
したものを常法で焙焼して製造したものを使用す
る請求項1に記載の難消化性デキストリンの製造
法。
[Claims] 1. Dissolve roasted dextrin in water and add α-
1. A method for producing indigestible dextrin, which comprises allowing amylase to act, and then allowing transglucosidase to act, optionally in the presence of β-amylase. 2. The production of indigestible dextrin according to claim 1, wherein the roasted dextrin is produced by roasting starch alone or a mixture thereof with at least one of monosaccharides and oligosaccharides in a conventional manner. Law.
JP63254540A 1988-10-07 1988-10-07 Production of indigestible dextrin Granted JPH02100695A (en)

Priority Applications (5)

Application Number Priority Date Filing Date Title
JP63254540A JPH02100695A (en) 1988-10-07 1988-10-07 Production of indigestible dextrin
EP89309269A EP0368451B1 (en) 1988-10-07 1989-09-12 Process for preparing dextrin containing dietary fiber
DE68914401T DE68914401T2 (en) 1988-10-07 1989-09-12 Process for the production of fibrous food products containing dextrin.
KR1019890013379A KR0135075B1 (en) 1988-10-07 1989-09-12 Preparation process of dextrin containing food fiber
US08/438,113 US5620873A (en) 1988-10-07 1995-05-08 Process for preparing dextrin containing food fiber

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP63254540A JPH02100695A (en) 1988-10-07 1988-10-07 Production of indigestible dextrin

Publications (2)

Publication Number Publication Date
JPH02100695A JPH02100695A (en) 1990-04-12
JPH0443624B2 true JPH0443624B2 (en) 1992-07-17

Family

ID=17266461

Family Applications (1)

Application Number Title Priority Date Filing Date
JP63254540A Granted JPH02100695A (en) 1988-10-07 1988-10-07 Production of indigestible dextrin

Country Status (1)

Country Link
JP (1) JPH02100695A (en)

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US5342631A (en) * 1992-12-29 1994-08-30 Wm. Wrigley Jr. Company Wax-free chewing gum including special oligosaccharide binders
JP2654529B2 (en) 1992-03-27 1997-09-17 大塚製薬株式会社 Health drink composition
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JP2015023835A (en) * 2013-07-26 2015-02-05 堤 和弘 Alcoholic beverage and production method thereof
WO2016103737A1 (en) 2014-12-26 2016-06-30 サントリーホールディングス株式会社 Dietary fiber
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