JP2926434B2 - Amylose particles and method for producing the same - Google Patents

Amylose particles and method for producing the same

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Publication number
JP2926434B2
JP2926434B2 JP2200052A JP20005290A JP2926434B2 JP 2926434 B2 JP2926434 B2 JP 2926434B2 JP 2200052 A JP2200052 A JP 2200052A JP 20005290 A JP20005290 A JP 20005290A JP 2926434 B2 JP2926434 B2 JP 2926434B2
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Japan
Prior art keywords
amylose
starch
molecular weight
amylose particles
average molecular
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JPH0485301A (en
Inventor
孝 渋谷
博人 茶圓
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Hayashibara Seibutsu Kagaku Kenkyujo KK
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Hayashibara Seibutsu Kagaku Kenkyujo KK
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Priority to JP2200052A priority Critical patent/JP2926434B2/en
Priority to GB9116133A priority patent/GB2247242B/en
Publication of JPH0485301A publication Critical patent/JPH0485301A/en
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Publication of JP2926434B2 publication Critical patent/JP2926434B2/en
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    • CCHEMISTRY; METALLURGY
    • C12BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
    • C12YENZYMES
    • C12Y204/00Glycosyltransferases (2.4)
    • C12Y204/01Hexosyltransferases (2.4.1)
    • C12Y204/01019Cyclomaltodextrin glucanotransferase (2.4.1.19)
    • AHUMAN NECESSITIES
    • A23FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
    • A23LFOODS, FOODSTUFFS, OR NON-ALCOHOLIC BEVERAGES, NOT COVERED BY SUBCLASSES A21D OR A23B-A23J; THEIR PREPARATION OR TREATMENT, e.g. COOKING, MODIFICATION OF NUTRITIVE QUALITIES, PHYSICAL TREATMENT; PRESERVATION OF FOODS OR FOODSTUFFS, IN GENERAL
    • A23L29/00Foods or foodstuffs containing additives; Preparation or treatment thereof
    • A23L29/30Foods or foodstuffs containing additives; Preparation or treatment thereof containing carbohydrate syrups; containing sugars; containing sugar alcohols, e.g. xylitol; containing starch hydrolysates, e.g. dextrin
    • A23L29/35Degradation products of starch, e.g. hydrolysates, dextrins; Enzymatically modified starches
    • AHUMAN NECESSITIES
    • A61MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61KPREPARATIONS FOR MEDICAL, DENTAL OR TOILETRY PURPOSES
    • A61K8/00Cosmetics or similar toiletry preparations
    • A61K8/02Cosmetics or similar toiletry preparations characterised by special physical form
    • A61K8/0241Containing particulates characterized by their shape and/or structure
    • AHUMAN NECESSITIES
    • A61MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61KPREPARATIONS FOR MEDICAL, DENTAL OR TOILETRY PURPOSES
    • A61K8/00Cosmetics or similar toiletry preparations
    • A61K8/18Cosmetics or similar toiletry preparations characterised by the composition
    • A61K8/72Cosmetics or similar toiletry preparations characterised by the composition containing organic macromolecular compounds
    • A61K8/73Polysaccharides
    • A61K8/732Starch; Amylose; Amylopectin; Derivatives thereof
    • AHUMAN NECESSITIES
    • A61MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61KPREPARATIONS FOR MEDICAL, DENTAL OR TOILETRY PURPOSES
    • A61K8/00Cosmetics or similar toiletry preparations
    • A61K8/18Cosmetics or similar toiletry preparations characterised by the composition
    • A61K8/72Cosmetics or similar toiletry preparations characterised by the composition containing organic macromolecular compounds
    • A61K8/73Polysaccharides
    • A61K8/738Cyclodextrins
    • AHUMAN NECESSITIES
    • A61MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61QSPECIFIC USE OF COSMETICS OR SIMILAR TOILETRY PREPARATIONS
    • A61Q19/00Preparations for care of the skin
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08BPOLYSACCHARIDES; DERIVATIVES THEREOF
    • C08B30/00Preparation of starch, degraded or non-chemically modified starch, amylose, or amylopectin
    • C08B30/20Amylose or amylopectin
    • CCHEMISTRY; METALLURGY
    • C12BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
    • C12PFERMENTATION OR ENZYME-USING PROCESSES TO SYNTHESISE A DESIRED CHEMICAL COMPOUND OR COMPOSITION OR TO SEPARATE OPTICAL ISOMERS FROM A RACEMIC MIXTURE
    • C12P19/00Preparation of compounds containing saccharide radicals
    • C12P19/16Preparation of compounds containing saccharide radicals produced by the action of an alpha-1, 6-glucosidase, e.g. amylose, debranched amylopectin
    • CCHEMISTRY; METALLURGY
    • C12BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
    • C12PFERMENTATION OR ENZYME-USING PROCESSES TO SYNTHESISE A DESIRED CHEMICAL COMPOUND OR COMPOSITION OR TO SEPARATE OPTICAL ISOMERS FROM A RACEMIC MIXTURE
    • C12P19/00Preparation of compounds containing saccharide radicals
    • C12P19/18Preparation of compounds containing saccharide radicals produced by the action of a glycosyl transferase, e.g. alpha-, beta- or gamma-cyclodextrins
    • AHUMAN NECESSITIES
    • A61MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61KPREPARATIONS FOR MEDICAL, DENTAL OR TOILETRY PURPOSES
    • A61K2800/00Properties of cosmetic compositions or active ingredients thereof or formulation aids used therein and process related aspects
    • A61K2800/40Chemical, physico-chemical or functional or structural properties of particular ingredients
    • A61K2800/41Particular ingredients further characterized by their size
    • A61K2800/412Microsized, i.e. having sizes between 0.1 and 100 microns

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  • Life Sciences & Earth Sciences (AREA)
  • Health & Medical Sciences (AREA)
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  • Wood Science & Technology (AREA)
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  • Birds (AREA)
  • General Engineering & Computer Science (AREA)
  • Polymers & Plastics (AREA)
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  • General Chemical & Material Sciences (AREA)
  • Microbiology (AREA)
  • Molecular Biology (AREA)
  • Food Science & Technology (AREA)
  • Materials Engineering (AREA)
  • Medicinal Chemistry (AREA)
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  • Preparation Of Compounds By Using Micro-Organisms (AREA)

Abstract

Novel amylose granules advantageously used in the fields of food products, pharmaceuticals and cosmetics exist in an approximately globular-shape of amylose granule or in a conjugation form consisting of two or more of the amylose granules linked together, and having about 2.10 mu m in diameter or major axis, B type form of starch on powder X-ray diffraction analysis, the number-average molecular weight of about 4,000-7,000 on gel permeation chromatography, and the weight- average molecular weight per the number-average molecular weight of about 1.4-1.7. The granules may be prepared by allowing cyclomaltodextrin glucanotransferase (EC 2.4.1.19) to act on an aqueous solution containing a cyclodextrin or starch. In examples the enzyme is derived from Bacillus stearothermophilas or Bacillus macerans; other sources are mentioned. <IMAGE>

Description

【発明の詳細な説明】 [産業上の利用分野] 本発明はアミロース粒子とその製造方法に関し、更に
詳細には、特定の形状、X線回折図形、分子量を有する
アミロース粒子と、シクロデキストリンまたは澱粉を含
有する水溶液にシクロマルトデキストリン・グルカノト
ランスフェラーゼを作用させて該水溶液に不溶性のアミ
ロース粒子を生成せしめ、このアミロース粒子を採取す
ることを特徴とするアミロース粒子の製造方法に関す
る。
Description: FIELD OF THE INVENTION The present invention relates to amylose particles and a method for producing the same, and more particularly, to amylose particles having a specific shape, X-ray diffraction pattern, and molecular weight, and cyclodextrin or starch. The present invention relates to a method for producing amylose particles, characterized in that cyclomaltodextrin glucanotransferase is allowed to act on an aqueous solution containing to produce amylose particles insoluble in the aqueous solution, and the amylose particles are collected.

[従来の技術] アミロースの製造方法は、次に示すごとく種々の方法
が知られている。
[Prior Art] As a method for producing amylose, various methods are known as follows.

(1)ティー・ゼイ・ショック(T.J.Schoch)がジャー
ナル・オブ・アメリカン・ケミカル・ソサイエティー
(Journal of American Chemical Society)Vol.64、29
57(1942年)で報告しているブタノールによる複合体沈
澱法。
(1) TJ Schoch has published the Journal of American Chemical Society, Vol. 64, 29
57 (1942), a complex precipitation method using butanol.

(2)ケイ・エイチ・マイヤー(K.H.Meyer)等が、ヘ
ルベティカ・キミカ・アクタ(Helvetica Chimica Act
a)Vol.24、378(1951年)で報告している温水による抽
出法。
(2) KHMeyer and others have joined the Helvetica Chimica Act
a) Extraction method using warm water reported in Vol. 24, 378 (1951).

(3)バス(Bus)等が、特公昭32−8675号公報、米国
特許2,822,305および米国特許2,829,990で開示している
硫酸マグネシウムによる塩析法。
(3) A salting-out method using magnesium sulfate disclosed in Japanese Patent Publication No. 32-8675, U.S. Pat. No. 2,822,305 and U.S. Pat.

(4)杉本等が特公昭54−21420号公報で開示している
プルラナーゼ、イソアミラーゼなどの澱粉枝切酵素によ
る加水分解法。
(4) A hydrolysis method using a starch debranching enzyme such as pullulanase and isoamylase disclosed by Sugimoto et al. In Japanese Patent Publication No. 54-21420.

(5)ハンス・ベンダー(Hans Bender)が、カーボハ
イドレイト・リサーチ(Carbohydrate Research)Vol.6
5、85〜97(1978年)で報告しているシクロマルトデキ
ストリン・グルカノトランスフェラーゼによる受容体へ
の糖転移反応法。
(5) Hans Bender, Carbohydrate Research Vol.6
5, 85-97 (1978), a method of transglycosylation to a receptor by cyclomaltodextrin glucanotransferase reported in 1978.

しかしながら、(1)、(2)および、(3)の方法
では澱粉からの収率が、通常25W/W%未満と低いだけで
なく、原料澱粉の種類やロットによって、アミロースの
品質、収率が安定せず、また、アミロペクチンの混入の
恐れもある。
However, in the methods (1), (2) and (3), not only the yield from starch is as low as less than 25 W / W%, but also the quality and yield of amylose depending on the type and lot of raw starch. Is not stable, and there is a risk of contamination with amylopectin.

(4)の方法では、澱粉からの収率が80W/W%以上と
高いものの、長鎖アミロースと短鎖アミロースとの混合
物でしか得られず、通常、この長鎖、短鎖アミロースの
煩雑な分別工程を必要とする。また、澱粉枝切酵素によ
る未分解物の混入の恐れもある。
In the method (4), although the yield from starch is as high as 80 W / W% or more, it can be obtained only with a mixture of long-chain amylose and short-chain amylose. Requires a separation step. Further, there is a possibility that undegraded products may be mixed in with the starch debranching enzyme.

(5)の方法では、アミロースの生成濃度が低く、そ
の回収にメタノールなどの有機沈澱剤を必要とするにも
かかわらず、その収率は30W/W%未満と低い。
In the method (5), the yield is as low as less than 30 W / W%, although the concentration of amylose produced is low and an organic precipitant such as methanol is required for its recovery.

[発明が解決しようとする課題] 従来のアミロース製造方法の欠点を解消し、分子量の
比較的そろった高品質のアミロース粒子とそれを安定し
て容易に高収率に製造する方法の確率が強く望まれてい
る。
[Problems to be Solved by the Invention] The disadvantages of the conventional method for producing amylose are solved, and there is a strong probability that high-quality amylose particles having a relatively uniform molecular weight and a method for stably and easily producing them at a high yield. Is desired.

[課題を解決するための手段] 本発明は、上記欠点を解消するためになされたもので
あって、とりわけシクロマルトデキストリン・グルカノ
トランスフェラーゼ(EC 2.4.1.19)を使用して、新規
アミロース粒子とその製造方法の確立を目差して鋭意研
究した。
[Means for Solving the Problems] The present invention has been made in order to solve the above-mentioned drawbacks. In particular, the present invention provides a novel amylose particle using cyclomaltodextrin glucanotransferase (EC 2.4.1.19). We studied hard to establish the manufacturing method.

その結果、シクロデキストリンまたは澱粉の比較的高
濃度水溶液にシクロマルトデキストリン・グルカノトラ
ンスフェラーゼ(以下、CGT−aseと略称する。)を比較
的低温で作用させることにより、該水溶液中に新規アミ
ロース粒子が沈澱生成することを見い出し、これを採取
することによって容易に高品質のアミロース粒子が高収
率に製造しうることを見い出し、本発明を完成した。
As a result, by applying cyclomaltodextrin / glucanotransferase (hereinafter abbreviated as CGT-ase) to a relatively high concentration aqueous solution of cyclodextrin or starch at a relatively low temperature, new amylose particles are formed in the aqueous solution. It was found that a precipitate was formed, and it was found that high-quality amylose particles could be easily produced in high yield by collecting the precipitate, thereby completing the present invention.

また、本発明は、下記の特長を有していることも判明
した。
It has also been found that the present invention has the following features.

(1)反応溶液中に不溶性のアミロース粒子を沈澱生成
することから、その分離、回収が容易であり、高価なメ
タノール、ブタノールなどの有機沈澱剤が不要である。
(1) Since insoluble amylose particles are precipitated in the reaction solution, their separation and recovery are easy, and expensive organic precipitants such as methanol and butanol are not required.

(2)原料からの収率を50W/W%以上の高収率にするこ
とも容易である。
(2) It is easy to increase the yield from raw materials to a high yield of 50 W / W% or more.

(3)原料の違い、CGT−aseの起源の違い、作用温度、
作用量、作用時間などの条件を変えることにより、生成
するアミロース粒子の分子量を調整することもできる。
(3) Difference in raw materials, difference in origin of CGT-ase, working temperature,
The molecular weight of the produced amylose particles can be adjusted by changing conditions such as the amount of action and the time of action.

本発明に用いる原料シクロデキストリンは、α−シク
ロデキストリン、β−シクロデキストリン、γ−シクロ
デキストリンのいずれか一種または二種以上の混合物で
あってもよい。また、シクロデキシトリンは、市販品を
用いることも、澱粉にCGT−aseを作用させて生成したも
のを用いることも随意である。この際、シクロデキスト
リンにグルコースや低分子のオリゴ糖などが共存するな
らば、できるだけ除去して作用させるのが望ましい。
The raw material cyclodextrin used in the present invention may be any one or a mixture of two or more of α-cyclodextrin, β-cyclodextrin, and γ-cyclodextrin. In addition, as the cyclodextrin, a commercially available product or a product produced by allowing CGT-ase to act on starch is optional. At this time, if glucose, low molecular weight oligosaccharides and the like coexist in the cyclodextrin, it is desirable to remove as much as possible to act.

また、澱粉にCGT−aseと澱粉枝切酵素とを作用させて
シクロデキストリンを生成させるとともにアミロース粒
子を生成させることも有利に実施できる。
In addition, it is also possible to advantageously carry out the action of CGT-ase and starch debranching enzyme on starch to produce cyclodextrin and amylose particles.

また、本発明に用いる澱粉は、馬鈴薯澱粉、甘薯澱
粉、タピオカ澱粉などの地下澱粉であっても、とうもろ
こし澱粉、小麦澱粉、米澱粉などの地上澱粉であっても
よい。澱粉にCGT−aseを作用させるには、澱粉乳にCGT
−aseを添加して加熱し、澱粉を糊化液化させてもよ
く、また、必要ならば、予め、澱粉を酸またはα−アミ
ラーゼで低DE、望ましくは、DE1未満に液化した後にCGT
−aseを作用させてもよい。
Further, the starch used in the present invention may be an underground starch such as potato starch, sweet potato starch, tapioca starch, or a ground starch such as corn starch, wheat starch, rice starch. In order for CGT-ase to act on starch, CGT must be added to starch milk.
-The starch may be gelatinized and liquefied by adding the ase and heating, and if necessary, liquefying the starch with an acid or α-amylase to a low DE, preferably less than DE1, followed by CGT
-Ase may act.

本発明に使用するCGT−aseは、公知のバチルス・ステ
アロサーモフィラス(Bacillus stearothermophilu
s)、バチルス・サーキュランス(Bacillus circulan
s)、バチルス・マセランス(Bacillus macerans)など
のバチルス属、クレブシーラ・ニューモニアエ(Klebsi
ella pneumoniae)などのクレブシーラ属などに属する
微生物由来の酵素が用いられる。とりわけ、澱粉を加熱
糊化する際にしても使用できるバチルス・ステアロサー
モフィラス由来の好熱性のCGT−aseが有利に利用でき
る。また、澱粉枝切酵素は、プルラナーゼ(EC 3.2.1.4
1)として公知のアエロバクター(Aerobacter)属、バ
チルス属などに属する微生物由来の酵素が、イソアミラ
ーゼ(EC3.2.1.68)として、公知のシュードモナス(Ps
eudomonas)属、フラボバクテリウム(Flavobacteriu
m)属、チトファーガ(Cytophaga)属に属する微生物由
来の酵素が有利に利用できる。これらの酵素は、本発明
の目的を達成しさえすればよく、必ずしも精製して使用
する必要はなく、通常は、培養上清や、これの部分精製
酵素が用いられる。また、必要に応じて、固定化して用
いることも随意である。
CGT-ase used in the present invention is a known Bacillus stearothermophilus.
s), Bacillus circulan
s), Bacillus such as Bacillus macerans, Klebsi pneumoniae (Klebsi)
An enzyme derived from a microorganism belonging to the genus Klebsiella such as ella pneumoniae is used. In particular, a thermophilic CGT-ase derived from Bacillus stearothermophilus, which can be used even when heating and gelatinizing starch, can be advantageously used. The starch debranching enzyme is pullulanase (EC 3.2.1.4).
An enzyme derived from a microorganism belonging to the genus Aerobacter or Bacillus known as 1) is known as Pseudomonas (Ps) as an isoamylase (EC3.2.1.68).
eudomonas, Flavobacteriu
m) Enzymes derived from microorganisms belonging to the genus Cytophaga can be advantageously used. These enzymes only need to achieve the object of the present invention and need not necessarily be used after purification. Usually, a culture supernatant or a partially purified enzyme thereof is used. In addition, if necessary, it is optionally used by immobilization.

より具体的に述べると、本発明においては、シクロデ
キストリンまたは澱粉を約10〜50W/W%含有する水溶液
にCGT−aseを、固形物グラム当り1〜1,000単位、温度
約5〜100℃、pH3〜9から選ばれる条件で適宜の時間作
用させることにより、アミロース粒子を該水溶性に析
出、沈澱生成させる。澱粉乳を使用する場合には、例え
ば、澱粉にCGT−ase、または、CGT−aseと澱粉枝切酵素
とを加え、温度70〜100℃に加熱して、澱粉を糊化、液
化させた後、60℃以下、望ましくは、5〜50℃に冷却
し、必要に応じて、CGT−aseを追加し、5〜500時間反
応を進め、アミロース粒子を沈澱生成させる。このアミ
ロース粒子は、濾過または遠心分離により容易に回収で
きる。
More specifically, in the present invention, CGT-ase is added to an aqueous solution containing about 10 to 50 W / W% of cyclodextrin or starch by adding 1 to 1,000 units per gram of solid matter, at a temperature of about 5 to 100 ° C., and at pH 3 By acting for an appropriate time under the conditions selected from 99 to 99, the amylose particles are precipitated and precipitated in the water-soluble manner. When using starch milk, for example, after adding CGT-ase, or CGT-ase and starch debranching enzyme to starch, heating to a temperature of 70 to 100 ° C. to gelatinize and liquefy the starch The temperature is lowered to 60 ° C. or lower, preferably 5 to 50 ° C., and if necessary, CGT-ase is added, and the reaction is allowed to proceed for 5 to 500 hours to precipitate and form amylose particles. The amylose particles can be easily recovered by filtration or centrifugation.

このようにして得られたアミロース粒子の理化学的性
質を調べたところ、(1)ほぼ球形の粒子が単一状態
で、または複数結合した状態で存在し、それらの直径ま
たは長径が約2〜10μmであり、(2)粉末X線回折に
より澱粉のB形図形を与え、(3)ゲル浸透クロマトグ
ラフィーにより、数平均分子量(Mn)が約4,000〜7,000
(グルコースの平均重合度として約25〜43個)、重量平
均分子量(Mw)/数平均分子量(Mn)が約1.4〜1.7を与
え、(4)沃素呈色が青紫〜青色となり、(5)βーア
ミラーゼの作用により理論量のマルトースを生成するこ
とが判明した。
The physicochemical properties of the amylose particles thus obtained were examined. (1) Almost spherical particles exist in a single state or in a state of a plurality of particles, and their diameter or major axis is about 2 to 10 μm. (2) X-ray powder diffraction gives a B-shaped figure of the starch, and (3) gel permeation chromatography has a number average molecular weight (Mn) of about 4,000 to 7,000.
(Average degree of polymerization of glucose is about 25 to 43), weight average molecular weight (Mw) / number average molecular weight (Mn) is about 1.4 to 1.7, (4) iodine color changes from bluish purple to blue, and (5) It was found that β-amylase produced a theoretical amount of maltose.

CGT−aseによる反応で得られたアミロース粒子を、更
に、溶解、沈澱を繰り返すなどの方法で精製することも
随意である。例えば、アミロース粒子を水に加熱溶解
し、これを冷却、沈澱させ、濾過または遠心分離し、乾
燥して白色粉末状のアミロース粒子を採取する。また、
得られるアミロース粒子を公知の方法により、更に、微
粉末化したり、顆粒化したりすることも随意である。
The amylose particles obtained by the reaction with CGT-ase may be further purified by a method such as repeated dissolution and precipitation. For example, amylose particles are dissolved in water by heating, cooled, precipitated, filtered or centrifuged, and dried to collect white powdery amylose particles. Also,
The obtained amylose particles may be further pulverized or granulated by a known method.

このようにして得られるアミロース粒子は、粉末品で
は流動性良好、難吸湿性であり、水に加熱溶解したもの
は、アミラーゼの作用を受け易く、冷却により固化し易
い性質を有する。
The amylose particles obtained in this manner have good fluidity and poor hygroscopicity in powder form, and have the property of being easily dissolved by heating in water, easily affected by amylase, and easily solidified by cooling.

これらの性質を利用して、本発明のアミロース粒子
は、例えば、ゼリー菓子、餅菓子、米菓、パン、クッキ
ー、錠菓、打粉などとして食品分野、粉剤、錠剤、ペー
スト剤などとして医薬品分野、化粧品分野などに、更に
は、離型剤、付着防止剤、増量剤、賦形剤、フィルム素
材などとして各種分野に広く利用される。
Utilizing these properties, the amylose particles of the present invention can be used, for example, in the food field as jelly confectionery, rice cake, rice confectionery, bread, cookies, tablet confectionery, powdering, etc., in the pharmaceutical field as powders, tablets, pastes, etc. It is widely used in various fields such as a cosmetics field, and further as a release agent, an antiadhesive, a bulking agent, an excipient, a film material, and the like.

また、高品質のアミロース粒子が安定して生産できる
ことから、アミラーゼ測定用基質として臨床検査、液体
クロマトグラフィー用充填剤として光学異性体の分割な
どに有利に利用できる。
Further, since high-quality amylose particles can be stably produced, it can be advantageously used for clinical tests as a substrate for amylase measurement and resolution of optical isomers as a filler for liquid chromatography.

以下、実験を用いて、本発明を詳細に説明する。 Hereinafter, the present invention will be described in detail using experiments.

実験1 アミロース粒子の生成に及ぼす基質濃度の影響 α−シクロデキストリンを各種濃度に溶解した基質溶
液に、バチルス・ステアロサーモフィラス由来のCGT−a
se((株)林原生物化学研究所販売)をシクロデキトリ
ングラム当り50単位使用し、温度30℃、pH5.5で20時間
作用させ、生成したアミロース粒子を遠心分離にて回収
して収率(W/W%)を求めた。また、このアミロース粒
子を東ソー株式会社販売のTSK−GEL G4000PWおよびG300
0PWを連結して使用し、分子量標準物質として昭和電工
株式会社販売のShodex STANDARDP−82を使用するゲル浸
透クロマトグラフィーにかけ、数平均分子量(Mn)を求
めた。結果は、表1に示した。
Experiment 1 Effect of Substrate Concentration on Formation of Amylose Particles CGT-a derived from Bacillus stearothermophilus was added to a substrate solution in which α-cyclodextrin was dissolved at various concentrations.
se (sold by Hayashibara Biochemical Laboratory) is used for 50 hours per gram of cyclodextrin, allowed to act for 20 hours at a temperature of 30 ° C and a pH of 5.5, and the produced amylose particles are collected by centrifugation to recover the yield. (W / W%) was determined. In addition, these amylose particles were transferred to TSK-GEL G4000PW and G300
Using 0PW connected, gel permeation chromatography using Shodex STANDARDP-82 sold by Showa Denko KK as a molecular weight standard substance was performed to determine the number average molecular weight (Mn). The results are shown in Table 1.

表1の結果より、アミロース粒子の生成は基質濃度に
依存し、基質濃度が高いほどアミロース粒子の生成量は
増加し、15W/W%以上の濃度で50W/W%以上の高収率であ
った。生成したアミロース粒子の分子量は、ほとんど同
じであった。
From the results in Table 1, it can be seen that the production of amylose particles depends on the substrate concentration, and the higher the substrate concentration, the more the amount of amylose particles produced, and a high yield of 50 W / W% or more at a concentration of 15 W / W% or more. Was. The molecular weight of the produced amylose particles was almost the same.

実験2 アミロース粒子の生成に及ぼす温度の影響 α−シクロデキストリンの25W/W%溶液にバチルス・
ステアロサーモフィラス由来のCGT−aseをシクロデキス
トリングラム当り50単位、pH5.5で各種温度で20時間作
用させ、アミロース粒子を回収した。得られたアミロー
ス粒子の収率や分子量の測定結果を表2に示した。
Experiment 2 Effect of temperature on formation of amylose particles Bacillus.
Amylose particles were collected by allowing CGT-ase derived from Stearothermophilus to act at 50 units per cyclodextrin ram at pH 5.5 for 20 hours at various temperatures. Table 2 shows the measurement results of the yield and molecular weight of the obtained amylose particles.

表2の結果より、アミロース粒子の生成は温度に依存
し、温度が低いほどアミロース粒子の生成量は増大し、
50℃以下が好適であった。生成したアミロース粒子の分
子量は、温度に影響された。
From the results in Table 2, the production of amylose particles depends on the temperature, and the lower the temperature, the more the amount of amylose particles produced,
50 ° C. or less was preferred. The molecular weight of the resulting amylose particles was affected by temperature.

実験3 アミロース粒子の生成に及ぼすCGT−ase起源の
比較 α−シクロデキストリン、γ−シクロデキストリンの
25W/W%溶液にバチルス・ステアロサーモフィラス、バ
チルス・マセランス由来のCGT−aseをシクロデキストリ
ングラム当り50単位、pH5.5、温度40℃で20時間作用さ
せ、得られたアミロース粒子の収率や分子量、沃素呈色
の測定を行なった。その結果を、表3に示した。
Experiment 3 Effect of CGT-ase on the production of amylose particles Comparison of α-cyclodextrin and γ-cyclodextrin
CGT-ase derived from Bacillus stearothermophilus or Bacillus macerans was allowed to act on a 25 W / W% solution at 50 units per cyclodextrin ram at pH 5.5 at a temperature of 40 ° C. for 20 hours, and the resulting amylose particles were collected. The rate, molecular weight and iodine coloration were measured. The results are shown in Table 3.

表3に示したように、基質の種類、酵素の起源によ
り、生成するアミロース粒子の収率や分子量、沃素呈色
は異なっており、この違いを利用することにより所望の
アミロース粒子の製造が可能になる。
As shown in Table 3, the yield, molecular weight, and iodine coloration of the produced amylose particles are different depending on the type of the substrate and the origin of the enzyme, and the desired amylose particles can be produced by utilizing these differences. become.

以下、実施例を述べる。 Hereinafter, examples will be described.

実施例1 α−シクロデキストリンの25W/W%水溶液に、バチル
ス・ステアロサーモフィラス由来のCGT−aseをシクロデ
キストリングラム当り50単位の割合で加え、pH5.5、30
℃で20時間反応させた。生成したアミロース粒子を遠心
分離機にて回収した。これを水で2回遠心洗浄し、40℃
で一夜真空乾燥し、アミロース粒子を約84W/W%の収率
で得た。
Example 1 CGT-ase derived from Bacillus stearothermophilus was added to an aqueous solution of α-cyclodextrin at 25% w / w at a ratio of 50 units per cyclodextrin rum at pH 5.5, 30.
The reaction was performed at 20 ° C. for 20 hours. The produced amylose particles were collected by a centrifuge. This is centrifuged twice with water, and
Overnight to obtain amylose particles in a yield of about 84 W / W%.

本品の理化学的性質を調べたところ、次の通りであっ
た。
Examination of the physicochemical properties of this product revealed the following.

(1)粒子径 走差型電子顕微鏡にて2,000倍に拡大して調べたとこ
ろ、図1に示すように、ほぼ球形の粒子が単一状態で、
または複数結合した状態で確認され、それらの直径また
は長径は約2〜10μmであった。
(1) Particle size When examined with a scanning electron microscope at a magnification of 2,000 times, as shown in FIG. 1, almost spherical particles are in a single state.
Alternatively, it was confirmed in a state of multiple bonds, and their diameter or major axis was about 2 to 10 μm.

(2)粉末X線解析 X線回折装置(理学電機株式会社製造、商品名ガイガ
ーフレックスRAD−IIB、Cukα線使用)にて対照の澱粉
と本発明のアミロース粒子を粉末法で調べた。結果は、
図2に示した。は澱粉のA形図形であり、は澱粉の
B形図形である。は本発明のアミロース粒子のX線回
折図であり、と同じ澱粉のB形図形を与えることが判
明した。
(2) X-Ray Powder Analysis Control starch and amylose particles of the present invention were examined by an X-ray diffractometer (manufactured by Rigaku Denki Co., Ltd., trade name: Geigerflex RAD-IIB, using Cukα ray) by a powder method. Result is,
As shown in FIG. Is an A-shaped figure of starch, and is a B-shaped figure of starch. Is an X-ray diffraction pattern of the amylose particles of the present invention, and was found to give the same B-form of starch.

(3)分子量 ゲル濾過クロマトグラフィーにより、分子量(数平均
分子量(Mn)および重量平均分子量(Mw)を調べたとこ
ろ、それらの値は、それぞれ5,300および8,000であっ
た。従って、そのMw/Mnは約1.5で、このことは、分子量
分布幅の狭い高品質のアミロースであることを意味す
る。
(3) Molecular weight When the molecular weight (number average molecular weight (Mn) and weight average molecular weight (Mw) were examined by gel filtration chromatography, the values were 5,300 and 8,000, respectively. At about 1.5, this means a high quality amylose with a narrow molecular weight distribution.

(4)比旋光度 ▲[α]20 D▼163°(l=1、c=0.9、0.5N−NaO
H) (5)赤外線吸収スペクトル KBr錠剤法で測定し、結果は、図3に示した。
(4) Specific rotation ▲ [α] 20 D ▼ 163 ° (l = 1, c = 0.9, 0.5N-NaO
H) (5) Infrared absorption spectrum Measured by the KBr tablet method, and the results are shown in FIG.

(6)沃素呈色 沃素−沃化カリウム溶液で青紫に呈色し、その最大吸
収波長(λmax)は、570nm付近であった。
(6) Coloration of iodine The iodine-potassium iodide solution exhibited blue-violet color, and its maximum absorption wavelength (λmax) was around 570 nm.

(7)アミラーゼ分解 サツマイモ由来のβーアミラーゼ(生化学工業株式会
社、結晶標品)によって、加水分解され、理論量のマル
トースを生成することから、本アミロース粒子は、実質
的にα−1,4グルコシド結合から成っているものと判断
される。
(7) Amylase degradation The amylose particles are substantially hydrolyzed by β-amylase derived from sweet potato (Seikagaku Corporation, crystal standard) to produce the theoretical amount of maltose. It is determined to be composed of glucosidic bonds.

実施例2 γ−シクロデキストリンの25W/W%水溶液にバチルス
・マセランス由来のCGT−aseをシクロデキストリングラ
ム当り70単位加え、pH5.7、40℃で20時間作用させた。
生成したアミロース粒子を実施例1と同様に洗浄、乾燥
してアミース粒子を収率約66W/W%で得た。
Example 2 CGT-ase derived from Bacillus macerans was added to a 25 W / W% aqueous solution of γ-cyclodextrin in an amount of 70 units per cyclodextrin gram, and allowed to act at pH 5.7 and 40 ° C for 20 hours.
The produced amylose particles were washed and dried in the same manner as in Example 1 to obtain amice particles at a yield of about 66 W / W%.

本品の数平均分子量(Mn)、重量平均分子量(Mw)
は、それぞれ4,700、6,500で、そのMw/Mnは約1.4で、比
旋光度は▲[α]20 D▼161°であった。
Number average molecular weight (Mn), weight average molecular weight (Mw) of this product
Were 4,700 and 6,500, respectively, the Mw / Mn was about 1.4, and the specific rotation was ▲ [α] 20 D ▼ 161 °.

本品の他の理化学的性質は、実施例1と同様であっ
た。
Other physicochemical properties of this product were the same as in Example 1.

実施例3 β−シクロデキストリンの20W/W%含有懸濁液にバチ
ルス・ステアロサーモフィラス由来のCGT−aseをシクロ
デキストリングラム当り200単位加え、pH5.7に維持し、
50℃で4時間作用させた後、冷却し、40℃で10時間、30
℃で10時間、計24時間作用させ、生成したアミロース粒
子を実施例1と同様に採取し、収率約60W/W%で得た。
Example 3 A CGT-ase derived from Bacillus stearothermophilus was added to a suspension containing β-cyclodextrin at 20% w / w in an amount of 200 units per cyclodextrin, and the pH was maintained at 5.7.
After acting at 50 ° C for 4 hours, cool and at 40 ° C for 10 hours,
The resulting amylose particles were allowed to act for 10 hours at 24 ° C. for a total of 24 hours.

本品の数平均分子量(Mn)、重量平均分子量(Mw)は
それぞれ5,200、7,900で、そのMw/Mnは約1.5で、比旋光
度は▲[α]20 D▼163°であった。
The number average molecular weight (Mn) and the weight average molecular weight (Mw) of this product were 5,200 and 7,900, respectively. The Mw / Mn was about 1.5, and the specific rotation was ▲ [α] 20 D ▼ 163 °.

本品の他の理化学的性質は、実施例1と同様であっ
た。
Other physicochemical properties of this product were the same as in Example 1.

実施例4 20W/W%とうもろこし澱粉乳(pH6.0に調整)にバチル
ス・ステアロサーモフィラス由来の好熱性CGT−aseを固
形物グラム当り1単位加え、90℃で20分間液化を行なっ
た。この液化液を70℃に冷却し、CGT−aseを固形物グラ
ム当り5単位加え、24時間反応させてシクロデキストリ
ンを生成させた。この反応液を100℃で20分間維持し
て、CGT−aseを失活させ、次いで、pH4.5に調整し、グ
ルコアミラーゼを固形物当り10単位加え、55℃で20時間
反応させた。この反応液を100℃10分間維持して、グル
コアミラーゼを失活させ、濾過し活性炭にて脱色し、濃
縮した。
Example 4 A thermophilic CGT-ase derived from Bacillus stearothermophilus was added to 20 W / W% corn starch milk (adjusted to pH 6.0) at a rate of 1 unit per gram of solid matter, and liquefied at 90 ° C. for 20 minutes. . This liquefied liquid was cooled to 70 ° C., and 5 units of CGT-ase was added per gram of solid substance, and reacted for 24 hours to produce cyclodextrin. This reaction solution was maintained at 100 ° C. for 20 minutes to inactivate CGT-ase, then adjusted to pH 4.5, added with 10 units of glucoamylase per solid, and reacted at 55 ° C. for 20 hours. The reaction solution was maintained at 100 ° C. for 10 minutes to inactivate glucoamylase, filtered, decolorized with activated carbon, and concentrated.

本濃縮液を、特公昭62−51120号公報に開示させてい
る方法に準じて、ナトリウム型強酸性カチオン交換樹脂
を充填したカラムクロマトグラフィーにかけ、グルコー
スを除去し、α−、β−、γ−シクロデキストリン混合
物を、溶液状で収率約25W/W%で得た。
The concentrated solution was subjected to column chromatography packed with a sodium-type strongly acidic cation exchange resin according to the method disclosed in JP-B-62-51120 to remove glucose, and to remove α-, β-, γ- The cyclodextrin mixture was obtained in solution with a yield of about 25 W / W%.

本溶液を、濃度約35W/W%にし、バチルス・ステアロ
サーモフィラス由来のCGT−aseをシクロデキストリング
ラム当り50単位加え、pH5.7に維持し、65℃で4時間、
次いで冷却し、40℃で10時間、30℃で10時間、計24時間
作用させ、生成したアミロース粒子を実施例1と同様に
採取し、シクロデキストリン混合物当り収率約85W/W%
で得た。
This solution was adjusted to a concentration of about 35 W / W%, and CGT-ase derived from Bacillus stearothermophilus was added in an amount of 50 units per cyclodextrin ram, maintained at pH 5.7, and maintained at 65 ° C for 4 hours.
Then, the mixture was cooled and allowed to act at 40 ° C. for 10 hours and at 30 ° C. for 10 hours, for a total of 24 hours. The resulting amylose particles were collected in the same manner as in Example 1, and the yield per cyclodextrin mixture was about 85 W / W%.
I got it.

本品の数平均分子量(Mn)、重量平均分子量(Mw)は
それぞれ6,600、10,500で、そのMw/Mnは約1.6で、比旋
光度は▲[α]20 D▼166°であった。
The number average molecular weight (Mn) and the weight average molecular weight (Mw) of this product were 6,600 and 10,500, respectively. Its Mw / Mn was about 1.6, and the specific rotation was ▲ [α] 20 D ▼ 166 °.

本品の他の理化学的性質は、実施例1と同様であっ
た。
Other physicochemical properties of this product were the same as in Example 1.

実施例5 25W/W%馬鈴薯澱粉乳(pH6.0に調整)にバチルス・ス
テアロサーモフィラス由来の好熱性CGT−aseを固形物グ
ラム当り2単位加え、90℃で、20分間液化を行なった。
この液化液を55℃に冷却し、pH5.5に調整した後、CGT−
ase、イソアミラーゼ(株式会社林原生物化学研究所販
売)を固形物グラム当り、それぞれ100単位ずつ加え、
3時間作用させ、シクロデキストリンを生成させた後、
冷却し、40℃に6時間、30℃で17時間、計26時間作用さ
せ、生成したアミロース粒子を実施例1と同様に採取
し、澱粉当り収率約55W/W%で得た。
Example 5 Thermophilic CGT-ase derived from Bacillus stearothermophilus was added to 25 W / W% potato starch milk (adjusted to pH 6.0) at 2 units per gram of solid matter, and liquefaction was carried out at 90 ° C. for 20 minutes. Was.
After cooling this liquefied liquid to 55 ° C and adjusting the pH to 5.5, CGT-
ase, isoamylase (available from Hayashibara Biochemical Laboratory Co., Ltd.)
After acting for 3 hours to produce cyclodextrin,
The mixture was cooled and allowed to act at 40 ° C. for 6 hours and at 30 ° C. for 17 hours for a total of 26 hours, and the produced amylose particles were collected in the same manner as in Example 1 to obtain a yield per starch of about 55 W / W%.

本品の数平均分子量(Mn)、重量平均分子量(Mw)
は、それぞれ5,400、9,200で、そのMw/Mnは約1.7で、比
旋光度は▲[α]20 D▼163°であった。
Number average molecular weight (Mn), weight average molecular weight (Mw) of this product
Was 5,400 and 9,200, respectively, the Mw / Mn was about 1.7, and the specific rotation was ▲ [α] 20 D ▼ 163 °.

本品の他の理化学的性質は、実施例1と同様であっ
た。
Other physicochemical properties of this product were the same as in Example 1.

[発明の効果] 本文で述べたごとく、本発明の新規アミロース粒子
は、比較的分子量のそろった高品質の粒子で、シクロデ
キストリンまたは澱粉にシクロデキストリン・グルカノ
トランスフェラーゼを作用させた反応溶液中に沈澱生成
することから分離、回収が容易であり、高価なメタノー
ル、ブタノールなどの有機沈澱剤が不要である。
[Effects of the Invention] As described in the text, the novel amylose particles of the present invention are high-quality particles having relatively uniform molecular weights, and are prepared in a reaction solution obtained by reacting cyclodextrin or starch with cyclodextrin-glucanotransferase. Separation and recovery are easy due to precipitation, and expensive organic precipitants such as methanol and butanol are not required.

また、原料からの収率を50W/W%以上に高めることも
容易である。
It is also easy to increase the yield from raw materials to 50 W / W% or more.

更に、原料の違い、CGT−aseの起源の違い、作用濃
度、作用量などの反応条件を変えることによって、生成
するアミロース粒子の分子量を調整できることもきわめ
て好都合である。
Furthermore, it is also very convenient that the molecular weight of the produced amylose particles can be adjusted by changing the reaction conditions such as the difference in the raw materials, the difference in the origin of the CGT-ase, the action concentration and the action amount.

このようにして得られる新規アミロース粒子は、粉末
品では、流動性良好、難吸湿性であり、水に加熱溶解し
たものは、アミラーゼの作用を受け易く、冷却により固
化し易い性質を有する。これらの性質を利用して、食
品、医薬品、化粧品などの素材として有利に利用される
ことにより、これら産業における工業的意義はきわめて
大きい。
The novel amylose particles thus obtained have good fluidity and poor hygroscopicity in powder form, and have the property of being easily dissolved by heating in water and easily solidified by amylase. By utilizing these properties and being advantageously used as a material for foods, pharmaceuticals, cosmetics, and the like, the industrial significance in these industries is extremely large.

【図面の簡単な説明】[Brief description of the drawings]

図1は、本発明のアミロース粒子構造の一例を示す電子
顕微鏡による拡大写真(2,000倍)である。 図2は、澱粉と本発明のアミロース粒子の粉末X線回折
図で、は澱粉のA形図形であり、は澱粉のB形図形
であり、は本発明のアミロース粒子のX線回折図であ
る。 図3は、本発明の一例として、アミロース粒子の赤外線
吸収スペクトルである。
FIG. 1 is an enlarged photograph (2,000-fold) of an example of the amylose particle structure of the present invention, which is taken by an electron microscope. FIG. 2 is an X-ray powder diffraction pattern of starch and amylose particles of the present invention, wherein A is a form of starch, B is a form of starch B, and is an X-ray diffraction pattern of amylose particles of the present invention. . FIG. 3 is an infrared absorption spectrum of amylose particles as an example of the present invention.

フロントページの続き (56)参考文献 特公 昭54−21420(JP,B1) 特公 昭51−46817(JP,B1) 特公 昭54−28457(JP,B1) 澱粉科学,40[4](1993)p.375 −381 Carbohydr.Res,65[1 ](1978)p.85−97 Carbohydr.Res,101 [2](1982)p.279−285 Carbohydr.Res,78[1 ](1980)p.147−162 (58)調査した分野(Int.Cl.6,DB名) C08B 30/20 CA(STN)Continuation of the front page (56) References JP-B-54-21420 (JP, B1) JP-B-51-46817 (JP, B1) JP-B-54-28457 (JP, B1) Starch Science, 40 [4] ( 1993) p. 375-381 Carbohydr. Res, 65 [1] (1978) p. 85-97 Carbohydr. Res, 101 [2] (1982) p. 279-285 Carbohydr. Res, 78 [1] (1980) p. 147-162 (58) Field surveyed (Int. Cl. 6 , DB name) C08B 30/20 CA (STN)

Claims (3)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】ほぼ球形の粒子が単一状態で、または複数
結合した状態で存在し、それらの直径または長径が2〜
10μmであり、粉末X線回折により澱粉のB形図形を与
え、ゲル浸透クロマトグラフィーにより数平均分子量が
4,000〜7,000、重量平均分子量/数平均分子量が1.4〜
1.7を与え、かつ実質的にα−1,4グルコシド結合から成
っていることを特徴とするアミロース粒子。
(1) A substantially spherical particle exists in a single state or a plurality of bonded states, and has a diameter or a long diameter of 2 to 2.
X-ray powder diffraction gave a starch B-shaped figure, and the number average molecular weight was determined by gel permeation chromatography.
4,000 to 7,000, weight average molecular weight / number average molecular weight is 1.4 to
Amylose particles which give 1.7 and consist essentially of α-1,4 glucosidic bonds.
【請求項2】シクロデキストリンを10〜50w/w%含有
し、他の糖類を実質的に含まない水溶液にシクロマルト
デキストリン・グルカノトランスフェラーゼを作用さ
せ、該水溶液中に不溶性のアミロース粒子を生成せし
め、これを採取して請求項1記載のアミロース粒子を得
ることを特徴とするアミロース粒子の製造方法。
2. An aqueous solution containing 10 to 50% w / w of cyclodextrin and containing substantially no other saccharides is reacted with cyclomaltodextrin / glucanotransferase to form insoluble amylose particles in the aqueous solution. A method for producing amylose particles, comprising obtaining the amylose particles according to claim 1.
【請求項3】シクロデキストリンが澱粉から調製された
ものであることを特徴とする請求項2記載のアミロース
粒子の製造方法。
3. The method for producing amylose particles according to claim 2, wherein the cyclodextrin is prepared from starch.
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Families Citing this family (24)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5395640A (en) 1990-02-20 1995-03-07 A.E. Staley Manufacturing Company Method of preparing reduced fat foods
US5378491A (en) 1990-02-20 1995-01-03 A. E. Staley Manufacturing Co. Method of preparing a starch hydrolysate, an aqueous starch hydrolysate dispersion, method of preparing a food containing a starch hydrolysate, and a food formulation containing a starch hydrolysate
US5436019A (en) 1990-02-20 1995-07-25 A. E. Staley Manufacturing Co. Method of preparing reduced fat foods
US5387426A (en) 1990-02-20 1995-02-07 A.E. Staley Manufacturing Company Method of preparing reduced fat foods
JPH05506776A (en) 1990-02-20 1993-10-07 エー.イー.ステーリー マニュファクチュアリング カンパニー Method for producing low-fat food
US5368878A (en) 1990-02-20 1994-11-29 A. E. Staley Manufacturing Company Reduced fat meat products
US5372835A (en) 1990-02-20 1994-12-13 A. E. Staley Manufacturing Company Method of preparing reduced fat foods
US5409726A (en) 1990-02-20 1995-04-25 A. E. Staley Manufacturing Co. Method of preparing reduced fat foods
US5374442A (en) 1990-02-20 1994-12-20 A. E. Staley Manufacturing Company Method of preparing reduced fat foods
US5376399A (en) 1992-05-15 1994-12-27 A.E. Staley Manufacturing Co. Reduced fat cremes
USH1394H (en) 1992-05-22 1995-01-03 A. E. Staley Manufacturing Company Method of preparing reduced fat spreads
USH1395H (en) 1992-05-22 1995-01-03 A. E. Staley Manufacturing Company Composition and method of preparing reduced fat spreads
NL9300131A (en) * 1993-01-22 1994-08-16 Avebe Coop Verkoop Prod Method for fractionating starch.
FR2716199B1 (en) * 1994-02-15 1996-04-26 Roquette Freres Process for the manufacture of a starch hydrolyzate with a low polymolecularity index, a new starch hydrolyzate thus obtained and its use in peritoneal dialysis.
DE19737481A1 (en) * 1997-08-28 1999-03-04 Hoechst Ag Microparticles containing spherical linear polysaccharides
DE19839216C1 (en) * 1998-08-28 2000-01-20 Aventis Res & Tech Gmbh & Co Preparation of biocompatible, biodegradable water-insoluble polysaccharide microparticles, used e.g. as fillers for polymers or in diagnostic tests
US6746665B1 (en) 1998-12-28 2004-06-08 Celanese Ventures Gmbh Sun protection product with microparticles on the basis of water-insoluble linear polyglucan
DE19860371A1 (en) 1998-12-28 2000-06-29 Aventis Res & Tech Gmbh & Co Cosmetic or medical preparation for topical use
DE19860373B4 (en) * 1998-12-28 2004-02-19 Celanese Ventures Gmbh Oral care products and use of spherical microparticles
DE19902917C2 (en) * 1999-01-26 2001-03-29 Aventis Res & Tech Gmbh & Co Water-insoluble linear polysaccharides for filtration
US20080286410A1 (en) * 2007-03-06 2008-11-20 Richmond Patricia A Production of Resistant Starch Product
WO2012129017A1 (en) * 2011-03-18 2012-09-27 Baxter International Inc. Peritoneal dialysis solutions comprising glucose polymers
CN113811197A (en) 2019-05-13 2021-12-17 昭和产业株式会社 Modifier, composition for modification containing the modifier, and food, drink, pharmaceutical product, cosmetic, industrial product, feed, culture medium or fertilizer using the same, and method for modifying the same
CN113678933B (en) * 2021-08-10 2023-03-28 江南大学 Method for enhancing gel property of starch soft sweets by enzyme method and application thereof

Family Cites Families (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4587332A (en) * 1984-02-28 1986-05-06 Ogilvie Mills Ltd. Modified wheat "B" starch for corrugating adhesives
US4551177A (en) * 1984-04-23 1985-11-05 National Starch And Chemical Corporation Compressible starches as binders for tablets or capsules

Non-Patent Citations (4)

* Cited by examiner, † Cited by third party
Title
Carbohydr.Res,101[2](1982)p.279−285
Carbohydr.Res,65[1](1978)p.85−97
Carbohydr.Res,78[1](1980)p.147−162
澱粉科学,40[4](1993)p.375−381

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