JP7404233B2 - Crystalline starch decomposition products, food and drink compositions, food and drink products, pharmaceuticals, cosmetics, industrial products, feeds, culture media, fertilizers, and modifiers thereof, and the crystalline starch decomposition products using the crystalline starch decomposition products. Methods for producing products, food and drink compositions, food and drink products, pharmaceuticals, cosmetics, industrial products, feeds, culture media, and fertilizers - Google Patents
Crystalline starch decomposition products, food and drink compositions, food and drink products, pharmaceuticals, cosmetics, industrial products, feeds, culture media, fertilizers, and modifiers thereof, and the crystalline starch decomposition products using the crystalline starch decomposition products. Methods for producing products, food and drink compositions, food and drink products, pharmaceuticals, cosmetics, industrial products, feeds, culture media, and fertilizers Download PDFInfo
- Publication number
- JP7404233B2 JP7404233B2 JP2020523584A JP2020523584A JP7404233B2 JP 7404233 B2 JP7404233 B2 JP 7404233B2 JP 2020523584 A JP2020523584 A JP 2020523584A JP 2020523584 A JP2020523584 A JP 2020523584A JP 7404233 B2 JP7404233 B2 JP 7404233B2
- Authority
- JP
- Japan
- Prior art keywords
- starch decomposition
- decomposition product
- food
- products
- crystalline
- 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.)
- Active
Links
Classifications
-
- A—HUMAN NECESSITIES
- A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
- A23K—FODDER
- A23K20/00—Accessory food factors for animal feeding-stuffs
- A23K20/10—Organic substances
- A23K20/163—Sugars; Polysaccharides
-
- A—HUMAN NECESSITIES
- A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
- A23L—FOODS, FOODSTUFFS OR NON-ALCOHOLIC BEVERAGES, NOT OTHERWISE PROVIDED FOR; PREPARATION OR TREATMENT THEREOF
- A23L29/00—Foods or foodstuffs containing additives; Preparation or treatment thereof
- A23L29/30—Foods 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
-
- A—HUMAN NECESSITIES
- A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
- A23L—FOODS, FOODSTUFFS OR NON-ALCOHOLIC BEVERAGES, NOT OTHERWISE PROVIDED FOR; PREPARATION OR TREATMENT THEREOF
- A23L33/00—Modifying nutritive qualities of foods; Dietetic products; Preparation or treatment thereof
- A23L33/10—Modifying nutritive qualities of foods; Dietetic products; Preparation or treatment thereof using additives
- A23L33/125—Modifying nutritive qualities of foods; Dietetic products; Preparation or treatment thereof using additives containing carbohydrate syrups; containing sugars; containing sugar alcohols; containing starch hydrolysates
-
- A—HUMAN NECESSITIES
- A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
- A61K—PREPARATIONS FOR MEDICAL, DENTAL OR TOILETRY PURPOSES
- A61K47/00—Medicinal preparations characterised by the non-active ingredients used, e.g. carriers or inert additives; Targeting or modifying agents chemically bound to the active ingredient
- A61K47/30—Macromolecular organic or inorganic compounds, e.g. inorganic polyphosphates
- A61K47/36—Polysaccharides; Derivatives thereof, e.g. gums, starch, alginate, dextrin, hyaluronic acid, chitosan, inulin, agar or pectin
-
- A—HUMAN NECESSITIES
- A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
- A61K—PREPARATIONS FOR MEDICAL, DENTAL OR TOILETRY PURPOSES
- A61K8/00—Cosmetics or similar toiletry preparations
- A61K8/18—Cosmetics or similar toiletry preparations characterised by the composition
- A61K8/72—Cosmetics or similar toiletry preparations characterised by the composition containing organic macromolecular compounds
- A61K8/73—Polysaccharides
-
- C—CHEMISTRY; METALLURGY
- C05—FERTILISERS; MANUFACTURE THEREOF
- C05G—MIXTURES OF FERTILISERS COVERED INDIVIDUALLY BY DIFFERENT SUBCLASSES OF CLASS C05; MIXTURES OF ONE OR MORE FERTILISERS WITH MATERIALS NOT HAVING A SPECIFIC FERTILISING ACTIVITY, e.g. PESTICIDES, SOIL-CONDITIONERS, WETTING AGENTS; FERTILISERS CHARACTERISED BY THEIR FORM
- C05G3/00—Mixtures of one or more fertilisers with additives not having a specially fertilising activity
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08B—POLYSACCHARIDES; DERIVATIVES THEREOF
- C08B30/00—Preparation of starch, degraded or non-chemically modified starch, amylose, or amylopectin
- C08B30/12—Degraded, destructured or non-chemically modified starch, e.g. mechanically, enzymatically or by irradiation; Bleaching of starch
- C08B30/18—Dextrin, e.g. yellow canari, white dextrin, amylodextrin or maltodextrin; Methods of depolymerisation, e.g. by irradiation or mechanically
-
- C—CHEMISTRY; METALLURGY
- C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
- C12N—MICROORGANISMS OR ENZYMES; COMPOSITIONS THEREOF; PROPAGATING, PRESERVING, OR MAINTAINING MICROORGANISMS; MUTATION OR GENETIC ENGINEERING; CULTURE MEDIA
- C12N1/00—Microorganisms; Compositions thereof; Processes of propagating, maintaining or preserving microorganisms or compositions thereof; Processes of preparing or isolating a composition containing a microorganism; Culture media therefor
-
- C—CHEMISTRY; METALLURGY
- C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
- C12P—FERMENTATION OR ENZYME-USING PROCESSES TO SYNTHESISE A DESIRED CHEMICAL COMPOUND OR COMPOSITION OR TO SEPARATE OPTICAL ISOMERS FROM A RACEMIC MIXTURE
- C12P19/00—Preparation of compounds containing saccharide radicals
- C12P19/16—Preparation of compounds containing saccharide radicals produced by the action of an alpha-1, 6-glucosidase, e.g. amylose, debranched amylopectin
Landscapes
- Life Sciences & Earth Sciences (AREA)
- Chemical & Material Sciences (AREA)
- Health & Medical Sciences (AREA)
- Engineering & Computer Science (AREA)
- Organic Chemistry (AREA)
- Polymers & Plastics (AREA)
- Zoology (AREA)
- Wood Science & Technology (AREA)
- General Health & Medical Sciences (AREA)
- Biotechnology (AREA)
- Food Science & Technology (AREA)
- Genetics & Genomics (AREA)
- Molecular Biology (AREA)
- Biochemistry (AREA)
- Bioinformatics & Cheminformatics (AREA)
- Medicinal Chemistry (AREA)
- Veterinary Medicine (AREA)
- General Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Public Health (AREA)
- Animal Behavior & Ethology (AREA)
- Epidemiology (AREA)
- Nutrition Science (AREA)
- Microbiology (AREA)
- Pest Control & Pesticides (AREA)
- Pharmacology & Pharmacy (AREA)
- Materials Engineering (AREA)
- General Chemical & Material Sciences (AREA)
- Animal Husbandry (AREA)
- Birds (AREA)
- Crystallography & Structural Chemistry (AREA)
- Biomedical Technology (AREA)
- Virology (AREA)
- Tropical Medicine & Parasitology (AREA)
- Inorganic Chemistry (AREA)
- Mycology (AREA)
- Polysaccharides And Polysaccharide Derivatives (AREA)
- Cosmetics (AREA)
- Preparation Of Compounds By Using Micro-Organisms (AREA)
- Edible Oils And Fats (AREA)
Description
本技術は、結晶澱粉分解物、及び該結晶澱粉分解物を用いた飲食品用組成物、飲食品、医薬品、化粧料、工業製品、飼料、培地、肥料、及びこれらの改質剤、並びに、前記結晶澱粉分解物、飲食品用組成物、飲食品、医薬品、化粧品、工業製品、飼料、培地、及び肥料の製造方法に関する。 This technology provides crystalline starch decomposition products, food and drink compositions using the crystalline starch decomposition products, food and drink products, pharmaceuticals, cosmetics, industrial products, feeds, culture media, fertilizers, and modifiers thereof; The present invention relates to a method for producing the crystalline starch decomposition product, compositions for food and drink products, food and drink products, pharmaceuticals, cosmetics, industrial products, feeds, culture media, and fertilizers.
従来から、飲食品分野においては、甘味料、味質調整、浸透圧調整、保湿剤、粉末化基材等の用途に澱粉分解物が利用されている。また、澱粉分解物は、医薬品分野においても、経腸栄養剤の炭水化物源や薬剤の賦形剤等の用途に利用されている。更に化粧料分野において、澱粉分解物は、化粧料を固形化する際の結合剤やクリーム状の化粧料の粘度調整等の用途にも利用されている。 BACKGROUND ART Starch decomposition products have traditionally been used in the food and beverage field for applications such as sweeteners, taste adjustment, osmotic pressure adjustment, humectants, and powdered base materials. Starch decomposition products are also used in the pharmaceutical field as carbohydrate sources for enteral nutrients, excipients for drugs, and the like. Furthermore, in the field of cosmetics, starch decomposition products are used as binders for solidifying cosmetics and for adjusting the viscosity of creamy cosmetics.
このように、澱粉分解物は、その甘味度、味質、浸透圧、粘度、吸湿性等の基本的物性を調整することで、上記のような様々な用途に利用される。例えば、甘味度の高いものは甘味料として用いることに適し、逆に甘味度の低いものは味質調整剤、浸透圧調整剤、粉末化基材等に適する。また、澱粉分解物自体の吸湿性等も用途を選択する上で、重要な要素となる。例えば、澱粉分解物の吸湿性が高すぎると、保存や流通の際に固結したり、べたつきが発生したりすることがあり、粉末食品への利用や粉末化基材等の用途には適さない。 In this way, starch decomposition products can be used for the various purposes mentioned above by adjusting their basic physical properties such as sweetness, taste, osmotic pressure, viscosity, and hygroscopicity. For example, those with a high degree of sweetness are suitable for use as sweeteners, while those with a low degree of sweetness are suitable as taste regulators, osmotic pressure regulators, powdered base materials, etc. In addition, the hygroscopicity of the starch decomposition product itself is also an important factor in selecting the application. For example, if the hygroscopicity of starch decomposition products is too high, they may solidify or become sticky during storage or distribution, making them unsuitable for use in powdered foods or powdered base materials. do not have.
また、これらの澱粉分解物を結晶化させた結晶澱粉分解物も、その低吸湿性等の特徴を活かして、様々な分野で利用されている。例えば、特許文献1には、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により、食品分野、医薬品分野、化粧料分野等に用いることができるアミロース粒子の製造技術が開示されている。 Crystalline starch decomposition products obtained by crystallizing these starch decomposition products are also utilized in various fields by taking advantage of their characteristics such as low hygroscopicity. For example, Patent Document 1 discloses that cyclomaltodextrin glucanotransferase is caused to act on an aqueous solution containing cyclodextrin or starch to generate amylose particles insoluble in the aqueous solution, and the amylose particles are collected. , a technique for producing amylose particles that can be used in the pharmaceutical field, cosmetic field, etc. is disclosed.
また、特許文献2には、1,4-α-D-ポリグルカンまたはポリサッカリドを水中に融解し、その融解生成物を沈殿へ導き、その混合物を冷却し、そして形成された粒子を分離することによって、化粧品のための添加物、薬学的および他の適用における活性物質の担体、食品添加物、生分解性ポリマーまたは工業的ポリマーのための充填材等に用いることができるマイクロスフェアー状クリスタライトを製造する技術が開示されている。 Patent Document 2 also discloses melting 1,4-α-D-polyglucan or polysaccharide in water, leading the melted product to precipitation, cooling the mixture, and separating the particles formed. Microsphere-like crystals can thereby be used as additives for cosmetics, carriers of active substances in pharmaceutical and other applications, food additives, fillers for biodegradable or industrial polymers, etc. Techniques for manufacturing lights are disclosed.
食品分野や医療分野を含む幅広い分野で利用されている結晶物質としては、水に溶解する結晶ブドウ糖やトレハロース、水に不溶であるセルロースや高分子アミロースの結晶が挙げられ、水への溶解性の有無により利用される用途には一定の制限が生じる。結晶ブドウ糖やトレハロースは、低温の水にも高温の水にも溶解性があるため、例えば、懸濁化用途に用いることはできない。また、セルロースや高分子アミロースの結晶は、低温の水にも高温の水にも不溶であるため、水溶液中で均一に混合させることが困難である。そのため、飲食品用組成物、飲食品、医薬品、化粧料、工業製品、飼料、培地、肥料等の製品への加工手段に制約を受け、目的とする効果を発揮させることが困難となる場合がある。 Crystalline substances used in a wide range of fields, including the food and medical fields, include crystalline glucose and trehalose, which are soluble in water, and crystals of cellulose and high-molecular amylose, which are insoluble in water. Depending on the presence or absence, there are certain restrictions on how it can be used. Crystalline glucose and trehalose, for example, cannot be used for suspension applications because they are soluble in both low-temperature and high-temperature water. Furthermore, crystals of cellulose and high-molecular amylose are insoluble in both low-temperature water and high-temperature water, so it is difficult to mix them uniformly in an aqueous solution. As a result, there are restrictions on the processing methods for products such as food and beverage compositions, food and beverages, pharmaceuticals, cosmetics, industrial products, feed, culture media, and fertilizers, making it difficult to achieve the desired effects. be.
そこで、本技術では、温度によってその溶解性が異なる、新規の結晶澱粉分解物を提供することを主目的とする。 Therefore, the main objective of the present technology is to provide a novel crystalline starch decomposition product whose solubility varies depending on the temperature.
本願発明者らは、上記目的を解決するために、澱粉分解物の特定含有成分について鋭意研究を行った。その結果、本願発明者らは、オリゴ糖の中でもごく高分子の成分とデキストリンの低分子成分を高含有することを特徴とする新規な結晶澱粉分解物を開発し、該結晶澱粉分解物が、低温の水には不溶な部分を含む一方で、高温の水には完全に溶解する性質を示すことを突き止め、本技術を完成させるに至った。 In order to solve the above object, the inventors of the present application conducted extensive research on specific components contained in starch decomposition products. As a result, the present inventors developed a new crystalline starch decomposition product characterized by a high content of very high molecular weight components among oligosaccharides and low molecular weight components of dextrin, and the crystalline starch decomposition product has the following characteristics: They discovered that while it contains a portion that is insoluble in low-temperature water, it completely dissolves in high-temperature water, leading to the completion of this technology.
即ち、本技術では、まず、グルコース重合度(DP)8~19の含有量が40%以上、
グルコース重合度(DP)20以上の含有量が55%以下、
X線回折法の結果から算出される結晶化比率が1%以上である結晶澱粉分解物を提供する。
本技術に係る結晶澱粉分解物の前記結晶化比率は、10%以上とすることができる。
また、本技術に係る結晶澱粉分解物は、20℃の水に分散した際の上清Brix値を、2.0%以下とすることができる。That is, in the present technology, first, the content of glucose polymerization degree (DP) 8 to 19 is 40% or more;
The content of glucose polymerization degree (DP) of 20 or more is 55% or less,
A crystalline starch decomposition product having a crystallization ratio calculated from the results of X-ray diffraction of 1% or more is provided.
The crystallization ratio of the crystalline starch decomposition product according to the present technology can be 10% or more.
Furthermore, the crystalline starch decomposition product according to the present technology can have a supernatant Brix value of 2.0% or less when dispersed in water at 20°C.
本技術に係る結晶澱粉分解物は、温度によってその溶解性が異なることから、飲食品用組成物、飲食品、医薬品、化粧料、工業製品、飼料、培地、又は肥料等に好適に適用することが可能である。 Since the crystalline starch decomposition product according to the present technology has different solubility depending on the temperature, it can be suitably applied to food and drink compositions, food and drink products, pharmaceuticals, cosmetics, industrial products, feeds, culture media, fertilizers, etc. is possible.
本技術に係る結晶澱粉分解物は、その組成自体が新規であって、その収得の方法については特に限定されない。例えば、澱粉原料を、一般的な酸や酵素を用いた処理や、各種クロマトグラフィー、膜分離、エタノール沈殿等の所定操作を、適宜、組み合わせて行うことによって澱粉分解物を得た後、得られた澱粉分解物を一般的な結晶化工程を施すことによって得ることができる。 The composition of the crystalline starch decomposition product according to the present technology is new, and the method for obtaining it is not particularly limited. For example, after obtaining a starch decomposition product by appropriately combining a starch raw material with a treatment using general acids or enzymes, various chromatography, membrane separation, ethanol precipitation, etc., A starch decomposition product can be obtained by subjecting it to a general crystallization process.
即ち、本技術では、結晶澱粉分解物を製造する方法であって、澱粉または澱粉を軽度に分解して得られる澱粉分解中間物(例えば、液化液等)に、枝切り酵素及び枝作り酵素を、同時又は枝作り酵素作用後に枝切り酵素を作用させて、
グルコース重合度(DP)8~19の含有量が32%以上、
グルコース重合度(DP)20以上の含有量が30%以下、である澱粉分解物を得る酵素反応工程と、
前記澱粉分解物を、結晶化する結晶化工程と、
を行う、結晶澱粉分解物の製造方法を提供する。
また、本技術では、澱粉又は澱粉分解中間物に酸を加えて液化した後、枝切り酵素を作用させて、
グルコース重合度(DP)8~19の含有量が32%以上、
グルコース重合度(DP)20以上の含有量が30%以下、である澱粉分解物を得る酵素反応工程と、
前記澱粉分解物を、結晶化する結晶化工程と、
を行う、結晶澱粉分解物の製造方法を提供する。
本技術に係る製造方法における前記結晶化工程では、前記澱粉分解物の溶液を、所定の濃度以上で保持及び/又は所定の温度以下にすることで、前記澱粉分解物を結晶化することができる。
本技術に係る製造方法では、前記結晶化工程後に、前記結晶澱粉分解物を分離する分離工程を行うこともできる。That is, the present technology is a method for producing a crystalline starch decomposition product, in which a debranching enzyme and a debranching enzyme are added to starch or a starch decomposition intermediate (for example, a liquefied liquid) obtained by mildly decomposing starch. , by acting a branching enzyme simultaneously or after the action of a branching enzyme,
The content of glucose polymerization degree (DP) 8 to 19 is 32% or more,
an enzymatic reaction step for obtaining a starch decomposition product having a glucose polymerization degree (DP) of 20 or more and a content of 30% or less;
a crystallization step of crystallizing the starch decomposition product;
Provided is a method for producing a crystalline starch decomposition product.
In addition, in this technology, after adding acid to starch or starch decomposition intermediates and liquefying them, debranching enzymes are applied to
The content of glucose polymerization degree (DP) 8 to 19 is 32% or more,
an enzymatic reaction step for obtaining a starch decomposition product having a glucose polymerization degree (DP) of 20 or more and a content of 30% or less;
a crystallization step of crystallizing the starch decomposition product;
Provided is a method for producing a crystalline starch decomposition product.
In the crystallization step in the production method according to the present technology, the starch decomposition product can be crystallized by maintaining the solution of the starch decomposition product at a predetermined concentration or higher and/or by lowering the temperature to a predetermined temperature or less. .
In the production method according to the present technology, a separation step of separating the crystalline starch decomposition product can also be performed after the crystallization step.
本技術に係る結晶澱粉分解物は、飲食品用組成物、飲食品、医薬品、化粧料、工業製品、飼料、培地、又は肥料に含有させることにより、その品質を改質することができる。
即ち、本技術では、本技術に係る結晶澱粉分解物を含有する、飲食品用組成物、飲食品、医薬品、化粧料、工業製品、飼料、培地、又は肥料用の改質剤を提供する。The quality of the crystalline starch decomposition product according to the present technology can be improved by including it in a composition for food and drink, food and drink, medicine, cosmetics, industrial product, feed, culture medium, or fertilizer.
That is, the present technology provides a modifier for food and drink compositions, food and drink products, pharmaceuticals, cosmetics, industrial products, feeds, culture media, or fertilizers, which contains the crystalline starch decomposition product according to the present technology.
本技術では、また、グルコース重合度(DP)8~19の含有量が32%以上、
グルコース重合度(DP)20以上の含有量が30%以下、である澱粉分解物の結晶化物を含有する、飲食品用組成物、飲食品、医薬品、化粧料、工業製品、飼料、培地、又は肥料を提供する。
これらの飲食品用組成物、飲食品、医薬品、化粧料、工業製品、飼料、培地、又は肥料は、
グルコース重合度(DP)8~19の含有量が32%以上、
グルコース重合度(DP)20以上の含有量が30%以下、である澱粉分解物の一部又は全部を結晶化する結晶化工程、を行うことで製造することができる。In this technology, the content of glucose polymerization degree (DP) 8 to 19 is 32% or more,
A composition for food or drink, a food or drink, a pharmaceutical, a cosmetic, an industrial product, a feed, a culture medium, or Provide fertilizer.
These food and drink compositions, food and drink products, pharmaceuticals, cosmetics, industrial products, feeds, culture media, or fertilizers are
The content of glucose polymerization degree (DP) 8 to 19 is 32% or more,
It can be produced by performing a crystallization step of crystallizing part or all of a starch decomposition product having a glucose polymerization degree (DP) of 20 or more and 30% or less.
ここで、本技術で使用する技術用語を説明する。「枝切り酵素(debranching enzyme)」とは、澱粉の分岐点であるα-1,6-グルコシド結合を加水分解する反応を触媒する酵素の総称である。例えば、「イソアミラーゼ(Isoamylase, glycogen 6-glucanohydrolase)」、「プルラナーゼ(Pullulanase, pullulan 6-glucan hydrolase)」「アミロ-1,6-グルコシダーゼ/4-αグルカノトランスフェラーゼ(amylo-1,6-glucosidase/4-α glucanotransferase)」が知られている。なお、これらの枝切り酵素を、目的に応じて組み合わせて用いてもよい。 Here, technical terms used in this technology will be explained. “Debranching enzyme” is a general term for enzymes that catalyze a reaction that hydrolyzes α-1,6-glucoside bonds, which are branching points in starch. For example, "Isoamylase, glycogen 6-glucanohydrolase", "Pullulanase, pullulan 6-glucan hydrolase", "amylo-1,6-glucosidase/4-α glucanotransferase" /4-α glucanotransferase)” is known. Note that these debranching enzymes may be used in combination depending on the purpose.
「枝作り酵素(branching enzyme)」とは、α-1,4-グルコシド結合でつながった直鎖グルカンに作用して、α-1,6-グルコシド結合を作る働きを持った酵素の総称である。動物や細菌等に存在しているが、馬鈴薯、イネ種実、トウモロコシ種実等の植物から精製することも可能である。 "Branching enzyme" is a general term for enzymes that act on linear glucans connected by α-1,4-glucosidic bonds to form α-1,6-glucosidic bonds. . Although it exists in animals and bacteria, it can also be purified from plants such as potatoes, rice seeds, and corn seeds.
本技術に係る結晶澱粉分解物は、オリゴ糖の高分子成分とデキストリンの低分子成分(グルコース重合度;DP8~19)を多く含有するため、低分子のオリゴ糖では起こらない直鎖状糖分子同士の相互作用が生じて結晶性が高くなり、冷水には不溶な部分を含む性質を示す。また、本技術に係る結晶澱粉分解物は、DP20以上の含有量が55%以下であるため、適度な結晶性が発揮され、熱水に溶解する性質を示す。そのため、加熱溶液状態での精製が容易であり、幅広い製品の加工の際、加熱することで溶解させて利用することができる。 The crystalline starch decomposition product according to this technology contains a large amount of high molecular weight components of oligosaccharides and low molecular weight components of dextrin (glucose polymerization degree; DP8-19), so linear sugar molecules that do not occur with low molecular weight oligosaccharides As a result of interactions between the two, crystallinity increases, and it exhibits properties that include a portion that is insoluble in cold water. Further, since the crystalline starch decomposition product according to the present technology has a content of DP20 or higher of 55% or less, it exhibits appropriate crystallinity and exhibits the property of dissolving in hot water. Therefore, it is easy to purify it in a heated solution state, and it can be used by dissolving it by heating when processing a wide range of products.
以下、本技術を実施するための好適な形態について説明する。なお、以下に説明する実施形態は、本技術の代表的な実施形態の一例を示したものであり、これにより本技術の範囲が狭く解釈されることはない。 Hereinafter, a preferred form for implementing the present technology will be described. Note that the embodiment described below shows an example of a typical embodiment of the present technology, and therefore the scope of the present technology should not be interpreted narrowly.
<結晶澱粉分解物について>
本技術に係る結晶澱粉分解物は、澱粉原料、例えば、コーンスターチ、ワキシーコーンスターチ、米澱粉、小麦澱粉等の澱粉(地上系澱粉)、馬鈴薯澱粉、タピオカ澱粉、甘藷澱粉等のような地下茎または根由来の澱粉(地下系澱粉)、あるいはこれらの加工澱粉等を分解(糖化)することによって得られた澱粉分解物を、結晶化することによって得られるものである。使用する澱粉原料は、特に限定されず、あらゆる澱粉原料を用いることができる。<About crystalline starch decomposition products>
The crystalline starch decomposition product according to the present technology is derived from starch raw materials, such as starch (terrestrial starch) such as corn starch, waxy corn starch, rice starch, and wheat starch, underground stems or roots such as potato starch, tapioca starch, sweet potato starch, etc. It is obtained by crystallizing a starch decomposition product obtained by decomposing (saccharifying) starch (underground starch) or these processed starches. The starch raw material used is not particularly limited, and any starch raw material can be used.
本技術に係る結晶澱粉分解物の組成特性としては、グルコース重合度(以下「DP」と称する)8~19の含有量が40%以上、かつ、DP20以上の含有量が55%以下であり、X線回折法の結果から算出される結晶化比率が1%以上である。本技術に係る結晶澱粉分解物は、DP20未満の含有量が45%以上存在するため、沸騰浴程度での再溶解、溶液状態での精製が容易である。 The compositional characteristics of the crystalline starch decomposition product according to the present technology are that the content of glucose polymerization degree (hereinafter referred to as "DP") 8 to 19 is 40% or more, and the content of DP 20 or more is 55% or less, The crystallization ratio calculated from the results of X-ray diffraction is 1% or more. Since the crystalline starch decomposition product according to the present technology has a content of 45% or more with a DP of less than 20, it is easy to redissolve in a boiling bath or purify in a solution state.
また、本技術に係る結晶澱粉分解物は、結晶ブドウ糖、砂糖やトレハロース等とは異なり、冷水に不溶な部分を含む。具体的には、40℃程度の水で解け始め、20℃以下の冷水には不溶な部分がある。そのため、飲食品用組成物、飲食品、医薬品、化粧料、工業製品、飼料、培地、肥料等の製品の懸濁化に使用することも可能である。 Further, the crystalline starch decomposition product according to the present technology includes a portion that is insoluble in cold water, unlike crystalline glucose, sugar, trehalose, and the like. Specifically, it begins to dissolve in water at about 40°C, and some parts are insoluble in cold water at 20°C or lower. Therefore, it can also be used to suspend products such as food and drink compositions, food and drink products, pharmaceuticals, cosmetics, industrial products, feeds, culture media, and fertilizers.
更に、本技術に係る結晶澱粉分解物は、結晶セルロースや高分子のアミロース等とは異なり、熱水には溶解性を示す。具体的には、60~80℃の水でほぼ溶解し、100℃の熱水には全てが溶解する性質を示す。そのため、様々な製品への加工の際、加熱することで溶解させて利用することができる。 Furthermore, the crystalline starch decomposition product according to the present technology is soluble in hot water, unlike crystalline cellulose or polymeric amylose. Specifically, it exhibits the property that it is almost soluble in water at 60 to 80°C, and completely soluble in hot water at 100°C. Therefore, it can be melted and used by heating when processing into various products.
加えて、本技術に係る結晶澱粉分解物は、難消化性の結晶セルロースや高分子のアミロース等とは異なり、消化性を有する。そのため、消化・吸収可能な炭水化物源(カロリー源)としても利用することができる。 In addition, the crystalline starch decomposition product according to the present technology is digestible, unlike crystalline cellulose, polymer amylose, etc., which are indigestible. Therefore, it can also be used as a source of carbohydrates (calories) that can be digested and absorbed.
本技術に係る結晶澱粉分解物の前記結晶化比率は、100%を上限とし、80%以下でも60%以下でもよい。本技術に係る結晶澱粉分解物中の結晶画分は、粉末X線回折分析において、2-θが「5°-6.5°」,「8.5°-12.5°」,「13°-16°」,「16°-19°」,「19°-21°」,「21°-25.5°」,「25.5°-27.5°」,「27.5°-32°」,「32°-35.5°」,「37°-40°」の各区間に正のピークとして測定されるので、当該各区間の面積値を基に算出することで結晶澱粉分解物の結晶化比率を特定することができる。 The crystallization ratio of the crystalline starch decomposition product according to the present technology may have an upper limit of 100%, and may be 80% or less or 60% or less. In powder X-ray diffraction analysis, the crystal fraction in the crystalline starch decomposition product according to the present technology has a 2-θ of "5°-6.5°", "8.5°-12.5°", and "13 °-16°", "16°-19°", "19°-21°", "21°-25.5°", "25.5°-27.5°", "27.5°- Since positive peaks are measured in each section of 32°, 32°-35.5°, and 37°-40°, crystal starch decomposition can be calculated based on the area values of each section. It is possible to determine the crystallization ratio of a substance.
より具体的には、粉末X線回折測定結果のY軸:回折強度/X軸:2-θのチャートにおいて以下の基準により、「全体面積」及び「結晶面積」を算出し、下記(3)の計算式により、結晶化比率を求めることができる。
(1)全体面積(2-θが「3°-40°」の区間における面積);
2-θが3°と40°の測定値を結んだ直線を基準線とし、基準線と回折強度の曲線で囲まれる範囲のうち、基準線よりも回折強度が強い領域の面積を「全体面積」として算出する。
(2)結晶面積;
2-θが「5°-6.5°」,「8.5°-12.5°」,「13°-16°」,「16°-19°」,「19°-21°」,「21°-25.5°」,「25.5°-27.5°」,「27.5°-32°」,「32°-35.5°」,「37°-40°」の各区間における面積を(1)全体面積と同様にして算出し、前記全区間の面積の合計値を「結晶面積」として算出する。
(3)計算式;結晶化比率=(結晶面積/全体面積)×100More specifically, the "total area" and "crystal area" are calculated according to the following criteria in the Y axis: diffraction intensity/X axis: 2-θ chart of the powder X-ray diffraction measurement results, and the following (3) The crystallization ratio can be determined by the calculation formula.
(1) Total area (area in the section where 2-θ is "3°-40°");
The straight line connecting the measured values when 2-θ is 3° and 40° is used as the reference line, and the area of the region surrounded by the reference line and the diffraction intensity curve, where the diffraction intensity is stronger than the reference line, is defined as the "total area." ” is calculated as
(2) Crystal area;
2-θ is "5°-6.5°", "8.5°-12.5°", "13°-16°", "16°-19°", "19°-21°", "21°-25.5°", "25.5°-27.5°", "27.5°-32°", "32°-35.5°", "37°-40°" The area in each section is calculated in the same manner as (1) overall area, and the total value of the areas of all the sections is calculated as the "crystal area."
(3) Calculation formula: Crystallization ratio = (crystal area/total area) x 100
なお、本技術における「結晶化比率」は、MiniFlex600(株式会社リガク製)を用い、X線波長はCu Kα、X線出力は40kV、15mAで分析した粉末X線回折測定結果を用いて算出した値である。 The "crystallization ratio" in this technology was calculated using powder X-ray diffraction measurement results analyzed using MiniFlex 600 (manufactured by Rigaku Co., Ltd.) with an X-ray wavelength of Cu Kα and an X-ray output of 40 kV and 15 mA. It is a value.
本技術に係る結晶澱粉分解物は、換言すると、DP8~19の含有量が32%以上、DP20以上の含有量が30%以下、である澱粉分解物の結晶化物である。即ち、本技術に係る結晶澱粉分解物の結晶化前の澱粉分解物は、DP8~19の含有量が32%以上、DP20以上の含有量が30%以下、という特徴を有する。 In other words, the crystalline starch decomposition product according to the present technology is a crystallized starch decomposition product in which the content of DP8 to 19 is 32% or more and the content of DP20 or more is 30% or less. That is, the starch decomposition product before crystallization of the crystalline starch decomposition product according to the present technology is characterized in that the content of DP 8 to 19 is 32% or more, and the content of DP 20 or more is 30% or less.
本技術に係る結晶澱粉分解物は、分離工程を行うことで、甘味性を低下させることができる。低甘味性とすることで、甘味を必要としない用途へ、好適に適用することができる。そのため、例えば、甘味性の高い結晶糖質が使用できない食品添加物や飲食物、及び薬剤にも用いることができる。 The sweetness of the crystalline starch decomposition product according to the present technology can be reduced by performing a separation step. By having low sweetness, it can be suitably applied to applications that do not require sweetness. Therefore, it can be used, for example, in food additives, drinks, and drugs where crystalline carbohydrates with high sweetness cannot be used.
また、本技術に係る結晶澱粉分解物は、20℃以下の冷水に不溶な部分も含んでいるため、不溶部分を分離し、溶解性を有する糖質成分を除去する分離工程を行うことで、低吸湿性を示す結晶澱粉分解物を得ることができる。低吸湿性とすることで、本技術に係る結晶澱粉分解物を用いた飲食品用組成物、飲食品、医薬品、化粧料、工業製品、飼料、培地、肥料等の製品が吸湿してしまう可能性が低く、また、製品からの溶け出しを防止することができる。 In addition, since the crystalline starch decomposition product according to the present technology also contains a portion that is insoluble in cold water below 20°C, by performing a separation step to separate the insoluble portion and remove soluble carbohydrate components, A crystalline starch decomposition product exhibiting low hygroscopicity can be obtained. By having low hygroscopicity, products such as food and drink compositions, food and drink products, pharmaceuticals, cosmetics, industrial products, feeds, culture media, and fertilizers that use the crystalline starch decomposition products related to this technology may absorb moisture. It has low properties and can prevent it from leaching out of the product.
本技術に係る結晶澱粉分解物の中でも、低甘味性かつ低吸湿性である結晶澱粉分解物は、具体的には、結晶化比率が10%以上であり、かつ、20℃の水に分散した際の上清Brix値が2.0%以下である。ここで、本技術において、「20℃の水に分散した際の上清Brix値」とは、具体的には、20℃の水に結晶澱粉分解物を10質量%分散させ、よく撹拌させた際の上清のBrix値をいう。 Among the crystalline starch decomposition products according to the present technology, the crystalline starch decomposition products with low sweetness and low hygroscopicity have a crystallization ratio of 10% or more and are dispersed in water at 20°C. The actual supernatant Brix value is 2.0% or less. Here, in this technology, "supernatant Brix value when dispersed in 20°C water" specifically means that 10% by mass of crystalline starch decomposition product is dispersed in 20°C water and stirred well. This refers to the Brix value of the supernatant.
本技術に係る結晶澱粉分解物の中でも、低甘味性かつ低吸湿性である結晶澱粉分解物は、換言すると、本技術に係る結晶澱粉分解物を沈殿させた後、分離工程(例えば、20℃以下の水を用いて水洗)を行うことで、容易に取り出すことができる。 Among the crystalline starch decomposition products according to the present technology, the crystalline starch decomposition products having low sweetness and low hygroscopicity can be obtained by precipitating the crystalline starch decomposition products according to the present technology, followed by a separation process (for example, at 20 °C It can be easily taken out by washing with the following water.
一般的に澱粉の結晶構造は、粉末X線回折法の結果から、二重らせん間に含まれる水が単位胞に4分子含まれるA型と、36分子含まれるB型に分けられるが、本技術に係る結晶澱粉分解物の結晶構造については、本技術の効果を損なわない限り限定されず、A型であってもB型であっても良い。 In general, the crystal structure of starch can be divided into type A, in which a unit cell contains 4 molecules of water between the double helices, and type B, in which 36 molecules of water are contained between the double helices, based on the results of powder X-ray diffraction. The crystal structure of the crystalline starch decomposition product according to the technique is not limited as long as it does not impair the effects of the present technique, and may be type A or type B.
本技術に係る結晶澱粉分解物は、DP8~19の含有量が40%以上であれば、その含有量は特に限定されないが、好ましくは50%以上、より好ましくは55%以上である。DP8~19の含有量が増加するほど、結晶澱粉分解物の溶解性や結晶の大きさ等の品質が安定する。 In the crystalline starch decomposition product according to the present technology, the content is not particularly limited as long as the content of DP8 to 19 is 40% or more, but the content is preferably 50% or more, more preferably 55% or more. As the content of DP8 to 19 increases, the quality of the crystalline starch decomposition product, such as solubility and crystal size, becomes more stable.
また、本技術に係る結晶澱粉分解物は、DP20以上の含有量が55%以下であれば、その含有量は特に限定されないが、好ましくは50%以下、より好ましくは45%以下である。DP20以上の含有量が少なくなるほど、結晶澱粉分解物が60~80℃の水により溶解しやすくなる。 Further, the content of the crystalline starch decomposition product according to the present technology is not particularly limited as long as the content of DP20 or higher is 55% or less, but it is preferably 50% or less, more preferably 45% or less. The lower the content of DP20 or more, the easier the crystalline starch decomposition product will dissolve in water at 60 to 80°C.
本技術に係る結晶澱粉分解物は、粉砕して微粉末品として用いることができる。 The crystalline starch decomposition product according to the present technology can be pulverized and used as a fine powder product.
<結晶澱粉分解物を含む飲食品用組成物及び飲食品について>
本技術に係る結晶澱粉分解物は、温度によってその溶解性が異なる性質や、消化性等を利用して、飲食品の濃厚感の付与、白色の付与(白さの強調等)、炭水化物源(カロリー源)としての用途に好適に用いることができる。<About food and drink compositions and food and drink compositions containing crystalline starch decomposition products>
The crystalline starch decomposition product according to this technology takes advantage of its solubility that varies depending on temperature and its digestibility, etc. to impart richness to foods and drinks, impart whiteness (emphasizing whiteness, etc.), and provide carbohydrate sources ( It can be suitably used as a calorie source).
また、本技術に係る結晶澱粉分解物は、飲食品用組成物又は飲食品に含有させることで、その品質を改質することができる。具体的には、飲食品用組成物又は飲食品の吸湿性、固化性、ゲル化性、保形性、白色性、離水性等の品質を改質することができる。 In addition, the crystalline starch decomposition product according to the present technology can improve the quality of the composition or the food or drink by including it in the composition or the food or drink. Specifically, qualities such as hygroscopicity, solidification, gelation, shape retention, whiteness, and water repellency of the composition for food and drink products or food and drink products can be modified.
本技術に係る結晶澱粉分解物を含有することができる飲食品としては、特に限定されず、例えば、ジュース、スポーツ飲料、お茶、コーヒー、紅茶等の飲料、醤油、ソース等の調味料、スープ類、クリーム類、各種乳製品類、アイスクリーム等の冷菓、各種粉末食品(飲料を含む)、保存用食品、冷凍食品、パン類、菓子類、米飯、麺類、水練り製品、畜肉製品等の加工食品等を挙げることができる。また、保健機能飲食品(特定保健機能食品、機能性表示食品、栄養機能食品を含む)や、いわゆる健康食品(飲料を含む)、流動食、乳児・幼児食、ダイエット食品、糖尿病用食品等にも本技術に係る結晶澱粉分解物を含有することができる。 Foods and drinks that can contain the crystalline starch decomposition product according to the present technology are not particularly limited, and include, for example, juices, sports drinks, beverages such as tea, coffee, and black tea, seasonings such as soy sauce and sauces, and soups. , creams, various dairy products, frozen desserts such as ice cream, various powdered foods (including beverages), preserved foods, frozen foods, breads, sweets, processed foods such as cooked rice, noodles, water paste products, meat products, etc. etc. can be mentioned. In addition, it is used in foods and beverages with health claims (including foods with specified health claims, foods with functional claims, and foods with nutritional claims), so-called health foods (including beverages), liquid foods, infant and toddler foods, diet foods, and diabetic foods. It is also possible to contain the crystalline starch decomposition product according to the present technology.
本技術に係る結晶澱粉分解物の飲食品用組成物又は飲食品への含有方法は、特に限定されない。例えば、本技術に係る結晶澱粉分解物を飲食品用組成物又は飲食品へそのまま含有させる方法、本技術に係る結晶澱粉分解物を任意の溶媒に溶解又は分散させた状態で飲食品用組成物又は飲食品へ含有させた後、必要に応じて再結晶化させる方法、本技術に係る結晶澱粉分解物の結晶化前の状態の澱粉分解物を飲食品用組成物又は飲食品へ含有させた後、澱粉分解物を結晶化させる方法、等を挙げることができる。 There are no particular limitations on the method of incorporating the crystalline starch decomposition product according to the present technology into a food or drink composition or a food or drink composition. For example, a method of incorporating the crystalline starch decomposition product according to the present technology into a food/drink composition or a food/beverage composition, or a method of incorporating the crystalline starch decomposition product according to the present technology into a food/beverage composition in a state in which it is dissolved or dispersed in an arbitrary solvent. or a method in which the crystalline starch decomposition product according to the present technology is included in a food or drink composition and then recrystallized as necessary; After that, a method of crystallizing the starch decomposition product, etc. can be mentioned.
本技術に係る結晶澱粉分解物を飲食品に用いる場合、飲食品用組成物として流通させる形態を採用することもできる。具体的には、例えば、各種食品用ミックス(ホットケーキミックス、ベーカリー用ミックス、菓子用ミックス、麺皮類用ミックス等)、各種食品用粉(天ぷら粉、から揚げ粉、お好み焼粉、たこ焼粉等)、各種飲食品のもと(菓子のもと、ドーナツのもと、ケーキのもと、アイスクリームのもと、スープのもと、飲料のもと等)等が挙げられる。 When the crystalline starch decomposition product according to the present technology is used in food and drink products, a form in which it is distributed as a composition for food and drink products can also be adopted. Specifically, for example, various food mixes (pancake mix, bakery mix, confectionery mix, noodle wrapper mix, etc.), various food flours (tempura flour, karaage flour, okonomiyaki flour, takoyaki flour, etc.) (roasted flour, etc.), various food and drink sources (confectionery sources, donut sources, cake sources, ice cream sources, soup sources, beverage sources, etc.).
また、本技術に係る結晶澱粉分解物は、濃厚栄養剤、畜肉等の食品の増量剤、粉末化基材、味質調整剤、懸濁化剤、浸透圧調整剤等の食品添加剤として用いることも可能である。 In addition, the crystalline starch decomposition products according to this technology can be used as food additives such as concentrated nutrients, bulking agents for foods such as livestock meat, powdered base materials, taste regulators, suspending agents, and osmotic pressure regulators. It is also possible.
<結晶澱粉分解物を含む医薬品について>
本技術に係る結晶澱粉分解物は、温度によってその溶解性が異なる性質や、消化性等を利用して、あらゆる医薬品に好適に適用することが可能である。<About medicines containing crystalline starch decomposition products>
The crystalline starch decomposition product according to the present technology can be suitably applied to all kinds of pharmaceuticals by taking advantage of its solubility that varies depending on temperature, digestibility, etc.
また、本技術に係る結晶澱粉分解物は、医薬品に含有させることで、その品質を改質することができる。具体的には、医薬品の吸湿性、固化性、ゲル化性、保形性、白色性、離水性等の品質を改質することができる。 Moreover, the quality of the crystalline starch decomposition product according to the present technology can be improved by incorporating it into a pharmaceutical product. Specifically, it is possible to modify the qualities of pharmaceuticals, such as hygroscopicity, solidification, gelation, shape retention, whiteness, and water repellency.
医薬品への適用方法は、特に限定されないが、例えば、散剤、顆粒剤等の粉末化基材、錠剤等のための賦形剤、液状製剤、半固形製剤、軟膏製剤等のための懸濁化剤、浸透圧調整剤、着色(白色)料、経腸栄養剤等の炭水化物源(カロリー源)等に適用することが可能である。 Application methods for pharmaceuticals are not particularly limited, but include, for example, powdered base materials for powders and granules, excipients for tablets, suspensions for liquid preparations, semi-solid preparations, ointment preparations, etc. It can be applied to carbohydrate sources (calorie sources) such as agents, osmotic pressure regulators, colorants (white), and enteral nutrients.
本技術に係る結晶澱粉分解物の医薬品への含有方法は、特に限定されず、前述した飲食品用組成物又は飲食品への含有方法と同一であるため、ここでは説明を割愛する。 The method of incorporating the crystalline starch decomposition product according to the present technology into a pharmaceutical product is not particularly limited, and is the same as the method of incorporating it into the food/beverage composition or food/beverage product described above, so a description thereof will be omitted here.
<結晶澱粉分解物を含む化粧料について>
本技術に係る結晶澱粉分解物は、温度によってその溶解性が異なる性質等を利用して、あらゆる化粧料に好適に適用することが可能である。また、本技術に係る結晶澱粉分解物は、その粒子の形や大きさが比較的揃っており、生分解性であるため、これらの性質を利用して、様々な化粧料に好適に適用することができる。<About cosmetics containing crystalline starch decomposition products>
The crystalline starch decomposition product according to the present technology can be suitably applied to all kinds of cosmetics by taking advantage of the property that its solubility varies depending on the temperature. In addition, the crystalline starch decomposition product according to this technology has relatively uniform particle shapes and sizes and is biodegradable, so these properties can be utilized to suitably apply it to various cosmetics. be able to.
また、本技術に係る結晶澱粉分解物は、化粧料に含有させることで、その品質を改質することができる。具体的には、化粧料の吸湿性、固化性、ゲル化性、保形性、白色性、離水性等の品質を改質することができる。 Moreover, the quality of the crystalline starch decomposition product according to the present technology can be improved by incorporating it into a cosmetic. Specifically, it is possible to modify the qualities of cosmetics, such as hygroscopicity, solidification, gelation, shape retention, whiteness, and water repellency.
化粧料への適用方法は、特に限定されないが、例えば、粉状化粧料、固形状化粧料等の粉末化基材や賦形剤等、液状、乳状、ゲル状、クリーム状等の化粧料のための懸濁化剤、浸透圧調整剤、着色(白色)料等に適用することが可能である。 The method of application to cosmetics is not particularly limited, but for example, powdered base materials and excipients for powdered cosmetics, solid cosmetics, etc., liquid, milky, gel-like, cream-like cosmetics, etc. It can be applied as a suspending agent, an osmotic pressure adjusting agent, a coloring (whitening) agent, etc.
本技術に係る結晶澱粉分解物の化粧料への含有方法は、特に限定されず、前述した飲食品用組成物又は飲食品への含有方法と同一であるため、ここでは説明を割愛する。 The method of incorporating the crystalline starch decomposition product according to the present technology into cosmetics is not particularly limited, and is the same as the method of incorporating it into the food/beverage composition or food/beverage product described above, so a description thereof will be omitted here.
<結晶澱粉分解物を含む工業製品について>
本技術に係る結晶澱粉分解物は、温度によってその溶解性が異なる性質等を利用して、あらゆる工業製品に好適に適用することが可能である。また、本技術に係る結晶澱粉分解物は、直鎖状の分子構造を持ち、その粒子の形や大きさが比較的揃っており、生分解性であるため、これらの性質を利用して、様々な工業製品に好適に適用することができる。<About industrial products containing crystalline starch decomposition products>
The crystalline starch decomposition product according to the present technology can be suitably applied to all kinds of industrial products by taking advantage of the property that its solubility varies depending on the temperature. In addition, the crystalline starch decomposition product according to this technology has a linear molecular structure, the shape and size of its particles are relatively uniform, and it is biodegradable, so by utilizing these properties, It can be suitably applied to various industrial products.
また、本技術に係る結晶澱粉分解物は、工業製品に含有させることで、その品質を改質することができる。具体的には、工業製品の吸湿性、固化性、ゲル化性、保形性、白色性、離水性等の品質を改質することができる。 Furthermore, the crystalline starch decomposition product according to the present technology can improve the quality of industrial products by incorporating them into the products. Specifically, it is possible to modify the qualities of industrial products such as hygroscopicity, solidification, gelation, shape retention, whiteness, and water repellency.
本技術に係る結晶澱粉分解物が適用可能な工業製品としては、例えば、担体、各種フィルム、繊維、カプセル、接着剤、離型剤、付着防止剤、増量剤、研磨剤、賦形剤等を挙げることができる。 Industrial products to which the crystalline starch decomposition product according to the present technology can be applied include, for example, carriers, various films, fibers, capsules, adhesives, mold release agents, anti-adhesion agents, fillers, abrasives, excipients, etc. can be mentioned.
本技術に係る結晶澱粉分解物の工業製品への含有方法は、特に限定されず、前述した飲食品用組成物又は飲食品への含有方法と同一であるため、ここでは説明を割愛する。 The method of incorporating the crystalline starch decomposition product according to the present technology into an industrial product is not particularly limited, and is the same as the method of incorporating it into the food/beverage composition or food/beverage product described above, so a description thereof will be omitted here.
<結晶澱粉分解物を含む飼料、培地、肥料について>
本技術に係る結晶澱粉分解物は、温度によってその溶解性が異なる性質等を利用して、牛、馬、豚等の家畜用哺乳類、鶏、ウズラ等の家禽類、爬虫類、鳥類あるいは小型哺乳類等のペット類、養殖魚類、昆虫等の飼料にも含有させることが可能である。また、微生物培養用等の培地や肥料に含有させることも可能である。<About feed, culture medium, and fertilizer containing crystalline starch decomposition products>
The crystalline starch decomposition product according to this technology can be used for livestock mammals such as cows, horses, and pigs, poultry such as chickens and quail, reptiles, birds, and small mammals by taking advantage of the property that its solubility varies depending on temperature. It can also be included in feed for pets, farmed fish, insects, etc. Moreover, it is also possible to include it in a medium or fertilizer for culturing microorganisms.
また、本技術に係る結晶澱粉分解物は、飼料や培地、肥料に含有させることで、その品質を改質することができる。具体的には、飼料や培地、肥料の吸湿性、固化性、ゲル化性、保形性、白色性、離水性等の品質を改質することができる。 Furthermore, the quality of the crystalline starch decomposition product according to the present technology can be improved by including it in feed, culture medium, or fertilizer. Specifically, it is possible to modify the qualities of feed, culture medium, fertilizer, such as hygroscopicity, solidification, gelation, shape retention, whiteness, and water repellency.
本技術に係る結晶澱粉分解物の飼料や培地、肥料への含有方法は、特に限定されず、前述した飲食品用組成物又は飲食品への含有方法と同一であるため、ここでは説明を割愛する。 The method of incorporating the crystalline starch decomposition product according to this technology into feed, culture medium, and fertilizer is not particularly limited, and is the same as the method of incorporating it into the food and drink compositions or food and drink products described above, so the explanation is omitted here. do.
<結晶澱粉分解物を含む改質剤について>
本技術に係る結晶澱粉分解物は、前述の通り、飲食品用組成物、飲食品、医薬品、化粧料、工業製品、飼料、培地、又は肥料に配合することにより、その品質を改質することができるため、各製品の改質剤として用いることができる。<About modifiers containing crystalline starch decomposition products>
As mentioned above, the crystalline starch decomposition product according to this technology can be incorporated into food and drink compositions, food and drink products, pharmaceuticals, cosmetics, industrial products, feeds, culture media, or fertilizers to improve their quality. It can be used as a modifier for various products.
本発明に係る改質剤は、有効成分として本技術に係る結晶澱粉分解物を含んでいれば、前述した結晶澱粉分解物のみで構成されていてもよいし、本発明の効果を損なわない限り、他の成分を1種又は2種以上、自由に選択して含有させることもできる。他の成分としては、例えば、通常製剤化に用いられている賦形剤、pH調整剤、着色剤、矯味剤、崩壊剤、滑沢剤、安定剤、乳化剤等の成分を用いることができる。更に、公知の又は将来的に見出される機能を有する成分を、適宜目的に応じて併用することも可能である。前述した結晶澱粉分解物は、食品に分類されるため、当該結晶澱粉分解物以外の成分の選択次第では、本発明に係る改質剤を食品として取り扱うことも可能である。 The modifier according to the present invention may be composed only of the crystalline starch decomposition product described above, as long as it contains the crystalline starch decomposition product according to the present technology as an active ingredient, and as long as the effects of the present invention are not impaired. , one or more other components may be freely selected and included. Other components that can be used include, for example, excipients, pH adjusters, coloring agents, flavoring agents, disintegrants, lubricants, stabilizers, and emulsifiers that are commonly used in formulations. Furthermore, components having functions that are known or that will be discovered in the future may be used in combination depending on the purpose. Since the crystalline starch decomposition product described above is classified as a food, the modifier according to the present invention can be treated as a food depending on the selection of components other than the crystalline starch decomposition product.
本技術に係る改質剤の各製品への配合方法は、特に限定されない。例えば、本技術に係る改質剤を各製品へそのまま配合する方法、本技術に係る改質剤を任意の溶媒に溶解又は分散させた状態で各製品へ含有させた後、必要に応じて再結晶化させる方法、等を挙げることができる。 The method of blending the modifier according to the present technology into each product is not particularly limited. For example, the modifier according to the present technology may be blended into each product as is, or the modifier according to the present technology may be dissolved or dispersed in any solvent and then added to each product, and then reused as necessary. A method of crystallization, etc. can be mentioned.
<結晶澱粉分解物の製造方法について>
本技術に係る結晶澱粉分解物は、その組成自体が新規であって、その収得の方法については特に限定されることはない。例えば、澱粉原料を、一般的な酸や酵素を用いた処理や、各種クロマトグラフィー、膜分離、エタノール沈殿等の所定操作を、適宜組み合わせて行うことによって澱粉分解物を得た後、得られた澱粉分解物を一般的な結晶化工程を施すことによって得ることができる。また、澱粉分解物製造時、溶解性に合わせて60~100℃の水を用いることで、製造中の糖化液等での沈殿を防止することができ、質の良い結晶を得ることができる。<About the manufacturing method of crystalline starch decomposition product>
The composition of the crystalline starch decomposition product according to the present technology is new, and the method for obtaining it is not particularly limited. For example, after obtaining a starch decomposition product by appropriately combining a starch raw material with a treatment using general acids or enzymes, various chromatography, membrane separation, ethanol precipitation, etc., A starch decomposition product can be obtained by subjecting it to a general crystallization process. Furthermore, when producing the starch decomposition product, by using water at a temperature of 60 to 100°C depending on the solubility, precipitation in the saccharification solution, etc. during production can be prevented, and high-quality crystals can be obtained.
本技術に係る結晶澱粉分解物の結晶化前の澱粉分解物を効率的に得る方法として、澱粉または澱粉分解中間物に、少なくとも枝切り酵素と枝作り酵素を作用させる方法がある。枝切り酵素は、澱粉の分岐鎖の分解に関与する酵素であり、枝作り酵素は、澱粉の分岐鎖の合成に用いる酵素である。従って、両者は通常、一緒に用いられることはない。しかし、全く逆の作用を示す両酵素を組み合わせて用いることにより、本技術に係る澱粉分解物を確実に製造することができる。 As a method for efficiently obtaining a starch decomposition product before crystallization of a crystalline starch decomposition product according to the present technology, there is a method in which at least a debranching enzyme and a branching enzyme are allowed to act on starch or a starch decomposition intermediate. Branching enzymes are enzymes involved in decomposing branched chains of starch, and branching enzymes are enzymes used to synthesize branched chains of starch. Therefore, the two are usually not used together. However, by using a combination of both enzymes that have completely opposite effects, it is possible to reliably produce the starch decomposition product according to the present technology.
この場合、両酵素の作用順序としては、同時又は枝作り酵素作用後に枝切り酵素を作用させる。 In this case, the order of action of both enzymes is either simultaneously or after the action of the branching enzyme, the debranching enzyme is brought into action.
前記枝切り酵素は、特に限定されない。例えば、プルラナーゼ(Pullulanase, pullulan 6-glucan hydrolase)、アミロ-1,6-グルコシダーゼ/4-αグルカノトランスフェラーゼ(amylo-1,6-glucosidase/4-α glucanotransferase)を挙げることができ、より好適な一例としては、イソアミラーゼ(Isoamylase, glycogen 6-glucanohydrolase)を用いることができる。 The debranching enzyme is not particularly limited. For example, pullulanase (pullulanase, pullulan 6-glucan hydrolase), amylo-1,6-glucosidase/4-α glucanotransferase (amylo-1,6-glucosidase/4-α glucanotransferase) can be mentioned, and more preferred As an example, isoamylase (glycogen 6-glucanohydrolase) can be used.
また、前記枝作り酵素も特に限定されない。例えば、動物や細菌等から精製したもの、又は、馬鈴薯、イネ種実、トウモロコシ種実等の植物から精製したもの、市販された酵素製剤等を用いることができる。 Furthermore, the branching enzyme is not particularly limited. For example, enzymes purified from animals, bacteria, etc., those purified from plants such as potatoes, rice seeds, and corn seeds, and commercially available enzyme preparations can be used.
また、本技術に係る結晶澱粉分解物の結晶化前の澱粉分解物を得る別の方法としては、澱粉または澱粉分解中間物に酸を加えて液化した後、枝切り酵素を作用させる方法がある。この際、用いることができる酸は、澱粉または澱粉分解中間物を液化可能な酸であって、本技術の効果を損なわない酸であれば、一般的な酸を1種または2種以上、自由に選択して用いることができる。例えば、塩酸、シュウ酸、硫酸等を挙げることができる。 Another method of obtaining a starch decomposition product before crystallization of the crystalline starch decomposition product according to the present technology is to add an acid to starch or a starch decomposition intermediate to liquefy it, and then apply a debranching enzyme to the starch decomposition product. . At this time, the acids that can be used are those that can liquefy starch or starch decomposition intermediates, and one or more general acids can be freely used as long as they do not impair the effects of the present technology. It can be selected and used. Examples include hydrochloric acid, oxalic acid, and sulfuric acid.
本技術に係る結晶澱粉分解物の製造方法における結晶化工程では、前記澱粉分解物が結晶化される。結晶化工程は、前記酵素反応工程後に行うこともできるし、前記酵素反応工程と同時に行うことも可能である。 In the crystallization step in the method for producing a crystalline starch decomposition product according to the present technology, the starch decomposition product is crystallized. The crystallization step can be performed after the enzyme reaction step, or can be performed simultaneously with the enzyme reaction step.
結晶化工程における結晶化の方法は特に限定されず、公知の結晶化方法を1種又は2種以上、自由に選択して用いることができる。本技術では、例えば、前記澱粉分解物の溶液を、所定の濃度以上に保持及び/又は所定の温度以下にすることで、前記澱粉分解物を結晶化することができる。 The crystallization method in the crystallization step is not particularly limited, and one or more known crystallization methods can be freely selected and used. In the present technology, for example, the starch decomposition product can be crystallized by maintaining the solution of the starch decomposition product at a predetermined concentration or higher and/or by lowering the temperature to a predetermined temperature or lower.
この場合の前記澱粉分解物の溶液の濃度は特に限定されず、本技術の効果を損なわない限り自由に設定することができ、例えば、10質量%以上で保持することで、前記澱粉分解物を結晶化することができる。また、この場合の前記澱粉分解物の温度も特に限定されず、本技術の効果を損なわない限り自由に設定することができ、例えば、60℃以下で保持することで、前記澱粉分解物を結晶化することができる。更に、保持時間も、特に限定されず、本技術の効果を損なわない限り自由に設定することができる。 In this case, the concentration of the solution of the starch decomposition product is not particularly limited and can be set freely as long as it does not impair the effects of the present technology. For example, by maintaining the concentration of the starch decomposition product at 10% by mass or more, Can be crystallized. In addition, the temperature of the starch decomposition product in this case is not particularly limited and can be set freely as long as it does not impair the effects of the present technology. can be converted into Furthermore, the holding time is not particularly limited, and can be freely set as long as it does not impair the effects of the present technology.
本技術に係る結晶澱粉分解物の製造方法では、前記結晶化工程後の沈殿、又は脱水乾燥後の粉末品に対して前記結晶澱粉分解物を分離する分離工程を行うことができる。分離工程とは、結晶澱粉分解物から水への溶解性の低い成分を分離する工程であり、例えば、水やアルコール等の有機溶媒での洗浄やろ過、遠心分離、またはそれらの組み合わせによって行うことができる。分離工程を行うことで、結晶化比率が10%以上であり、かつ、20℃の水に分散した際の上清Brix値が2.0%以下である、低甘味性かつ低吸湿性の結晶澱粉分解物を得ることが可能である。 In the method for producing a crystalline starch decomposition product according to the present technology, a separation step of separating the crystalline starch decomposition product can be performed on the precipitate after the crystallization step or the powder product after dehydration and drying. The separation process is a process of separating components with low solubility in water from the crystalline starch decomposition product, and may be performed, for example, by washing with an organic solvent such as water or alcohol, filtration, centrifugation, or a combination thereof. Can be done. By performing the separation process, low sweetness and low hygroscopic crystals with a crystallization ratio of 10% or more and a supernatant Brix value of 2.0% or less when dispersed in water at 20°C are obtained. It is possible to obtain starch decomposition products.
本技術に係る結晶澱粉分解物の製造方法では、前記酵素反応工程の後、前記結晶化工程の後、又は分離工程の後に、不純物を除去する工程を行うことも可能である。不純物の除去方法としては、特に限定されず、公知の方法を1種又は2種以上自由に組み合わせて用いることができる。例えば、ろ過、活性炭脱色、イオン精製等の方法を挙げることができる。 In the method for producing a crystalline starch decomposition product according to the present technology, it is also possible to perform a step of removing impurities after the enzyme reaction step, after the crystallization step, or after the separation step. The method for removing impurities is not particularly limited, and one or more known methods can be used in combination. For example, methods such as filtration, activated carbon decolorization, and ion purification can be used.
更に、本技術に係る結晶澱粉分解物は、結晶化工程後の結晶を含む液状品として用いることも可能であるが、真空乾燥、噴霧乾燥、凍結乾燥等により脱水乾燥し、粉末化することも可能である。 Furthermore, the crystalline starch decomposition product according to the present technology can be used as a liquid product containing crystals after the crystallization process, but it can also be dehydrated and powdered by vacuum drying, spray drying, freeze drying, etc. It is possible.
<飲食品用組成物、飲食品、医薬品、化粧料、工業製品、飼料、培地、又は肥料の製造方法について>
本技術に係る結晶澱粉分解物の製造方法における前記結晶化工程を、飲食品用組成物、飲食品、医薬品、化粧料、工業製品、飼料、培地、又は肥料の製造方法の一工程で行うことで、DP8~19の含有量が32%以上、DP20以上の含有量が30%以下、である澱粉分解物の結晶化物を含有する、飲食品用組成物、飲食品、医薬品、化粧料、工業製品、飼料、培地、又は肥料を製造することができる。<About the manufacturing method of food and drink compositions, food and drink products, pharmaceuticals, cosmetics, industrial products, feeds, culture media, or fertilizers>
The crystallization step in the method for producing a crystalline starch decomposition product according to the present technology is performed as one step in a method for producing a composition for food and beverages, a food and beverage, a pharmaceutical, a cosmetic, an industrial product, a feed, a culture medium, or a fertilizer. Compositions for food and beverages, foods and beverages, pharmaceuticals, cosmetics, and industrial products containing crystallized starch decomposition products with a content of DP8 to 19 of 32% or more and a content of DP20 or higher of 30% or less. A product, feed, culture medium, or fertilizer can be manufactured.
各製品の製造方法における結晶化工程を行うタイミングは、本発明の効果を損なわない限り、各製品の製造工程に応じて、自由に設定することができる。例えば、各製品と本技術に係る結晶澱粉分解物をそれぞれ製造した上で、各製品に本技術に係る結晶澱粉分解物を配合する方法、各製品と本技術に係る結晶澱粉分解物をそれぞれ製造した上で、本技術に係る結晶澱粉分解物を任意の溶媒に溶解又は分散させた状態で各製品へ含有させた後、必要に応じて再結晶化させる方法、各製品を製造した上で、結晶化前の状態の澱粉分解物を各製品へ含有させた後、澱粉分解物を結晶化させる方法、本技術に係る結晶澱粉分解物又は/及び結晶化前の状態の澱粉分解物を各製品の原料へ配合した後、各製品の製造工程の任意のタイミングにおいて澱粉分解物を結晶化させる方法、等を挙げることができる。 The timing of performing the crystallization step in the manufacturing method of each product can be freely set according to the manufacturing process of each product, as long as the effects of the present invention are not impaired. For example, a method of manufacturing each product and a crystalline starch decomposition product according to this technology, and then blending the crystalline starch decomposition product according to this technology into each product, or manufacturing each product and a crystalline starch decomposition product according to this technology, respectively. After that, the crystalline starch decomposition product according to the present technology is dissolved or dispersed in any solvent and then incorporated into each product, and then recrystallized as necessary. After manufacturing each product, A method of crystallizing the starch decomposition product after incorporating the starch decomposition product in the state before crystallization into each product, a crystalline starch decomposition product according to the present technology and/or a starch decomposition product in the pre-crystallization state in each product Examples include a method in which the starch decomposition product is crystallized at any timing in the manufacturing process of each product after being blended with the raw material.
以下、実施例に基づいて本技術を更に詳細に説明する。なお、以下に説明する実施例は、本技術の代表的な実施例の一例を示したものであり、これにより本技術の範囲が狭く解釈されることはない。 Hereinafter, the present technology will be described in more detail based on examples. Note that the embodiment described below shows one example of a typical embodiment of the present technology, and therefore the scope of the present technology should not be interpreted narrowly.
<実験例1>
実験例1では、結晶澱粉分解物の具体的な糖組成や結晶化比率が、溶解性、甘味性及び吸湿性にどのように影響するかを検討した。<Experiment example 1>
In Experimental Example 1, we investigated how the specific sugar composition and crystallization ratio of the crystalline starch decomposition product affect solubility, sweetness, and hygroscopicity.
(1)試験方法
[枝作り酵素]
本実験例では、枝作り酵素の一例として、Eur. J. Biochem. 59, p615-625 (1975)の方法に則って、精製した馬鈴薯由来の酵素(以下「馬鈴薯由来枝作り酵素」とする)と、Branchzyme(ノボザイムズ株式会社製、以下「細菌由来枝作り酵素」とする)を用いた。(1) Test method [Branch-forming enzyme]
In this experiment, as an example of a branch-forming enzyme, a potato-derived enzyme purified according to the method of Eur. J. Biochem. 59, p615-625 (1975) (hereinafter referred to as "potato-derived branch-forming enzyme") was used. and Branchzyme (manufactured by Novozymes Co., Ltd., hereinafter referred to as "bacterial branching enzyme").
なお、枝作り酵素の活性測定は、以下の方法で行った。
基質溶液として、0.1M酢酸緩衝液(pH5.2)にアミロース(シグマ アルドリッチ社製、A0512)を0.1質量%溶解したアミロース溶液を用いた。50μLの基質液に50μLの酵素液を添加し、30℃で30分間反応させた後、ヨウ素-ヨウ化カリウム溶液(0.39mMヨウ素-6mMヨウ化カリウム-3.8mM塩酸混合用液)を2mL加え反応を停止させた。ブランク溶液として、酵素液の代わりに水を添加したものを調製した。反応停止から15分後に660nmの吸光度を測定した。枝作り酵素の酵素活性量1単位は、上記の条件で試験する時、660nmの吸光度を1分間に1%低下させる酵素活性量とした。Note that the activity of the branching enzyme was measured by the following method.
As the substrate solution, an amylose solution in which 0.1% by mass of amylose (manufactured by Sigma-Aldrich, A0512) was dissolved in 0.1M acetate buffer (pH 5.2) was used. Add 50 μL of enzyme solution to 50 μL of substrate solution, react at 30°C for 30 minutes, and then add 2 mL of iodine-potassium iodide solution (0.39 mM iodine-6 mM potassium iodide-3.8 mM hydrochloric acid mixed solution). was added to stop the reaction. A blank solution was prepared by adding water instead of the enzyme solution. Absorbance at 660 nm was measured 15 minutes after the reaction was stopped. One unit of enzyme activity of the branching enzyme was defined as the amount of enzyme activity that lowered the absorbance at 660 nm by 1% per minute when tested under the above conditions.
[DP8~19及びDP20以上の含有量]
下記の表1に示す条件で高速液体クロマトグラフィー(HPLC)にて分析を行い、検出されたピーク面積比率に基づいて、DP8~19及びDP20以上の含有量を測定した。[Content of DP8 to 19 and DP20 or higher]
Analysis was performed by high performance liquid chromatography (HPLC) under the conditions shown in Table 1 below, and the content of DP 8 to 19 and DP 20 or higher was determined based on the detected peak area ratio.
[粉末X線回折]
粉末X線回折分析は、MiniFlex600(株式会社リガク製)を用い、X線波長はCu Kα、X線出力は40kV、15mAで分析した。分析チャートより、結晶の型を調べた。[Powder X-ray diffraction]
Powder X-ray diffraction analysis was performed using MiniFlex600 (manufactured by Rigaku Co., Ltd.) at an X-ray wavelength of Cu Kα and an X-ray output of 40 kV and 15 mA. The type of crystal was determined from the analysis chart.
[結晶化比率]
粉末X線回折測定結果のY軸:回折強度/X軸:2-θのチャートにおいて以下の基準により、「全体面積」及び「結晶面積」を算出し、下記(3)の計算式により求めた。
(1)全体面積(2-θが「3°-40°」の区間における面積);
2-θが3°と40°の測定値を結んだ直線を基準線とし、基準線と回折強度の曲線で囲まれる範囲のうち、基準線よりも回折強度が強い領域の面積を「全体面積」として算出した。
(2)結晶面積;
2-θが「5°-6.5°」,「8.5°-12.5°」,「13°-16°」,「16°-19°」,「19°-21°」,「21°-25.5°」,「25.5°-27.5°」,「27.5°-32°」,「32°-35.5°」,「37°-40°」の各区間における面積を(1)全体面積と同様にして算出し、前記全区間の面積の合計値を「結晶面積」として算出した。
(3)計算式;結晶化比率(%)=(結晶面積/全体面積)×100[Crystallization ratio]
The "total area" and "crystal area" were calculated based on the following criteria in the Y axis: diffraction intensity/X axis: 2-θ chart of the powder X-ray diffraction measurement results, and were determined using the formula (3) below. .
(1) Total area (area in the section where 2-θ is "3°-40°");
The straight line connecting the measured values when 2-θ is 3° and 40° is used as the reference line, and the area of the region surrounded by the reference line and the diffraction intensity curve, where the diffraction intensity is stronger than the reference line, is defined as the "total area." ” was calculated.
(2) Crystal area;
2-θ is "5°-6.5°", "8.5°-12.5°", "13°-16°", "16°-19°", "19°-21°", "21°-25.5°", "25.5°-27.5°", "27.5°-32°", "32°-35.5°", "37°-40°" The area in each section was calculated in the same manner as (1) overall area, and the total value of the areas of all the sections was calculated as the "crystal area."
(3) Calculation formula: Crystallization ratio (%) = (crystal area/total area) x 100
[溶解性の評価]
〔20℃の溶解性〕
結晶澱粉分解物を、20℃の水に10質量%分散させてよく撹拌し、不溶物の残渣、溶液の透明性を、下記の基準に基づいて評価した。また、沈殿を除く上清について、屈折計を用いてBrix値を測定した。[Evaluation of solubility]
[Solubility at 20°C]
The crystalline starch decomposition product was dispersed in 20° C. water at 10% by mass and stirred well, and the residue of insoluble matter and the transparency of the solution were evaluated based on the following criteria. Further, the Brix value of the supernatant excluding the precipitate was measured using a refractometer.
〔100℃の溶解性〕
結晶澱粉分解物を、水に10質量%分散させて、沸騰浴中で10分よく撹拌しながら加熱し、不溶物の沈殿、溶液の透明性について、下記の基準に基づいて評価した。[Solubility at 100℃]
The crystalline starch decomposition product was dispersed in water at 10% by mass, heated in a boiling bath for 10 minutes with thorough stirring, and the precipitation of insoluble matter and the transparency of the solution were evaluated based on the following criteria.
〔評価基準〕
溶解:完全に溶解し透明な溶液となる
白濁:ある程度溶解し沈殿はほぼないが、液が白濁している
不溶:大部分が溶解せず、沈殿している〔Evaluation criteria〕
Dissolved: Completely dissolved, resulting in a transparent solution. Cloudy: Dissolved to some extent, with almost no precipitate, but the liquid is cloudy. Insoluble: Most of the solution is not dissolved and is precipitated.
[甘味性]
結晶澱粉分解物を粉末の状態で食した際の甘味性について、専門パネル5名が、下記の評価基準に従って評価し、合議にて評価を決定した。[Sweetness]
The sweetness of the crystalline starch decomposition product when eaten in powder form was evaluated by a panel of five experts according to the following evaluation criteria, and the evaluation was determined by a consensus.
〔評価基準〕
○:甘味がなく、良好
△:やや甘みが感じられる
×:甘味が強い〔Evaluation criteria〕
○: No sweetness, good △: Slightly sweetness ×: Strong sweetness
[吸湿性]
結晶澱粉分解物を、温湿度試験器HIFLEX TH401(楠本化成株式会社製)を用いて、25℃、相対湿度95%で1週間保存した後の状態について、下記の評価基準に従って評価した。[Hygroscopicity]
The state of the crystalline starch decomposition product after being stored for one week at 25° C. and 95% relative humidity was evaluated using a temperature/humidity tester HIFLEX TH401 (manufactured by Kusumoto Kasei Co., Ltd.) according to the following evaluation criteria.
〔評価基準〕
○:粉末状態を維持
△:粉末の一部又は全部が固結
×:粉末が飴状になった〔Evaluation criteria〕
○: Maintained powder state △: Part or all of the powder solidified ×: Powder became candy-like
(2)実施例・比較例の製法
[実施例1]
10%水酸化カルシウムにてpH5.8に調整した30質量%のコーンスターチスラリーに、αアミラーゼ(リコザイムスープラ、ノボザイムズ株式会社製)を、固形分(g)当たり0.2質量%添加し、ジェットクッカー(温度110℃)で液化した。この液化液を95℃で保温し、継時的にDEを測定し、DE8になった時点で、10%塩酸でpH4.0に調整し、煮沸により反応を停止した。反応を停止した糖液のpHを5.8に調整した後、細菌由来枝作り酵素を固形分(g)当たり1000ユニット添加し、50℃で24時間反応させた。その後枝切り酵素(GODO-FIA、合同酒精株式会社製)を固形分(g)当たり1.5質量%添加し、50℃で24時間反応させた。この澱粉分解物の溶液を、活性炭脱色、イオン精製し、固形分濃度60質量%に濃縮した。該濃縮液を、60℃で7日間保持し、得られた沈殿を、固形分が溶け出さなくなるまで水洗と遠心分離を繰り返して分離した後、凍結乾燥して粉末化した実施例1の結晶澱粉分解物を得た。(2) Manufacturing method of Examples and Comparative Examples [Example 1]
To a 30% by mass cornstarch slurry adjusted to pH 5.8 with 10% calcium hydroxide, 0.2% by mass per solid content (g) of α-amylase (Ricozyme Supra, manufactured by Novozymes Co., Ltd.) was added and It was liquefied in a cooker (temperature 110°C). This liquefied liquid was kept at 95° C., DE was measured over time, and when DE reached 8, the pH was adjusted to 4.0 with 10% hydrochloric acid and the reaction was stopped by boiling. After the reaction was stopped, the pH of the sugar solution was adjusted to 5.8, and then 1000 units of bacterial branching enzyme was added per solid content (g), and the reaction was carried out at 50° C. for 24 hours. Thereafter, 1.5% by mass of a branch cutting enzyme (GODO-FIA, manufactured by Godo Shusei Co., Ltd.) was added based on the solid content (g), and the mixture was reacted at 50°C for 24 hours. This starch decomposition product solution was subjected to activated carbon decolorization, ion purification, and concentrated to a solid content concentration of 60% by mass. The concentrated solution was maintained at 60° C. for 7 days, and the resulting precipitate was separated by repeated washing with water and centrifugation until no solid content was dissolved out, and then lyophilized to powder the crystalline starch of Example 1. A decomposition product was obtained.
[実施例2]
10%水酸化カルシウムにてpH5.8に調整した30質量%のコーンスターチスラリーに、αアミラーゼ(クライスターゼT10S、天野エンザイム株式会社製)を、固形分(g)当たり0.2質量%添加し、ジェットクッカー(温度110℃)で液化した。この液化液を95℃で保温し、継時的にDEを測定し、DE9になった時点で、10%塩酸でpH4.0に調整し、煮沸により反応を停止した。反応を停止した糖液のpHを5.8に調整した後、細菌由来枝作り酵素を固形分(g)当たり800ユニット、枝切り酵素(GODO-FIA、合同酒精株式会社製)を固形分(g)当たり1.0質量%添加し、50℃で60時間反応させた。この澱粉分解物の溶液を、活性炭脱色、イオン精製し、固形分濃度50質量%に濃縮した。該濃縮液を、4℃で3日間保持し、得られた沈殿を、固形分が溶け出さなくなるまで水洗と遠心分離を繰り返して分離した後、凍結乾燥して粉末化した実施例2の結晶澱粉分解物を得た。[Example 2]
To a 30% by mass corn starch slurry adjusted to pH 5.8 with 10% calcium hydroxide, 0.2% by mass of α-amylase (Clistase T10S, manufactured by Amano Enzyme Co., Ltd.) was added per solid content (g), It was liquefied in a jet cooker (temperature 110°C). This liquefied liquid was kept at 95° C., DE was measured over time, and when DE reached 9, the pH was adjusted to 4.0 with 10% hydrochloric acid and the reaction was stopped by boiling. After adjusting the pH of the sugar solution after stopping the reaction to 5.8, the bacterial branching enzyme was added to 800 units per solid content (g), and the branching enzyme (GODO-FIA, manufactured by Godo Shusei Co., Ltd.) was added to the solid content (g). 1.0% by mass per g) was added and reacted at 50°C for 60 hours. This starch decomposition product solution was decolorized with activated carbon, ion-purified, and concentrated to a solid content concentration of 50% by mass. The concentrated solution was kept at 4°C for 3 days, and the resulting precipitate was separated by repeating water washing and centrifugation until no solid content was dissolved out, and then freeze-dried and powdered to obtain the crystalline starch of Example 2. A decomposition product was obtained.
[実施例3]
10%水酸化カルシウムにてpH5.8に調整した30質量%のコーンスターチスラリーに、αアミラーゼ(クライスターゼT10S、天野エンザイム株式会社製)を、固形分(g)当たり0.2質量%添加し、ジェットクッカー(温度110℃)で液化した。この液化液を95℃で保温し、継時的にDEを測定し、DE11になった時点で、10%塩酸でpH4.0に調整し、煮沸により反応を停止した。反応を停止した糖液のpHを5.8に調整した後、細菌由来枝作り酵素を固形分(g)当たり600ユニット添加し、65℃で15時間反応させた。その後枝切り酵素(GODO-FIA、合同酒精株式会社製)を固形分(g)当たり0.5質量%添加し、50℃で40時間反応させた。この澱粉分解物の溶液を、活性炭脱色、イオン精製し、固形分濃度50質量%に濃縮した。該濃縮液を、50℃で5日間保持し、得られた沈殿を含有した糖液をスプレードライヤーで粉末化した。該粉末を固形分が溶け出さなくなるまで水洗と遠心分離を繰り返して分離した後、凍結乾燥して粉末化した実施例3の結晶澱粉分解物を得た。[Example 3]
To a 30% by mass corn starch slurry adjusted to pH 5.8 with 10% calcium hydroxide, 0.2% by mass of α-amylase (Clistase T10S, manufactured by Amano Enzyme Co., Ltd.) was added per solid content (g), It was liquefied in a jet cooker (temperature 110°C). This liquefied liquid was kept at 95° C., DE was measured over time, and when DE reached 11, the pH was adjusted to 4.0 with 10% hydrochloric acid and the reaction was stopped by boiling. After the reaction was stopped, the pH of the sugar solution was adjusted to 5.8, and then 600 units of bacterial branching enzyme was added per solid content (g), and the reaction was carried out at 65° C. for 15 hours. Thereafter, 0.5% by mass of a branch cutting enzyme (GODO-FIA, manufactured by Godo Shusei Co., Ltd.) was added based on the solid content (g), and the mixture was reacted at 50°C for 40 hours. This starch decomposition product solution was decolorized with activated carbon, ion-purified, and concentrated to a solid content concentration of 50% by mass. The concentrate was kept at 50° C. for 5 days, and the resulting sugar solution containing the precipitate was pulverized using a spray dryer. The powder was separated by repeated washing with water and centrifugation until no solid content was dissolved out, and then lyophilized to obtain a powdered crystalline starch decomposition product of Example 3.
[実施例4]
10%塩酸にてpH2.0に調整した30質量%のコーンスターチスラリーを、130℃の温度条件でDE8まで分解した。常圧に戻した後、水酸化ナトリウムを用いて反応を停止した糖液のpHを5.8に調整した後、馬鈴薯由来枝作り酵素を固形分(g)当たり300ユニット添加し、35℃で48時間反応させた後、煮沸して反応を停止した。その後pHを4.2に調整し、枝切り酵素(イソアミラーゼ、シグマアルドリッチ ジャパン株式会社製)を固形分(g)当たり1.0質量%添加し、45℃で40時間反応させた。この澱粉分解物の溶液を、4℃で3日間保持し、得られた沈殿を、固形分が溶け出さなくなるまで水洗と遠心分離を繰り返して分離した後、凍結乾燥して粉末化した実施例4の結晶澱粉分解物を得た。[Example 4]
A 30% by mass cornstarch slurry adjusted to pH 2.0 with 10% hydrochloric acid was decomposed to DE8 at a temperature of 130°C. After returning to normal pressure, the reaction was stopped using sodium hydroxide, and the pH of the sugar solution was adjusted to 5.8. After that, 300 units of potato-derived branching enzyme was added per solid content (g), and the mixture was heated at 35°C. After reacting for 48 hours, the reaction was stopped by boiling. Thereafter, the pH was adjusted to 4.2, and 1.0% by mass of a debranching enzyme (isoamylase, manufactured by Sigma-Aldrich Japan Co., Ltd.) was added based on the solid content (g), and the mixture was reacted at 45° C. for 40 hours. Example 4 This starch decomposition product solution was kept at 4°C for 3 days, and the resulting precipitate was separated by repeating water washing and centrifugation until no solid content was dissolved, and then freeze-dried and powdered. A crystalline starch decomposition product was obtained.
[実施例5]
10%水酸化カルシウムにてpH5.8に調整した30質量%のタピオカ澱粉スラリーに、αアミラーゼ(クライスターゼT10S、天野エンザイム株式会社製)を、固形分(g)当たり0.2質量%添加し、ジェットクッカー(温度110℃)で液化した。この液化液を95℃で保温し、継時的にDEを測定し、DE15になった時点で、10%塩酸でpH4.0に調整し、煮沸により反応を停止した。反応を停止した糖液のpHを5.8に調整した後、馬鈴薯由来枝作り酵素を固形分(g)当たり2000ユニット添加し、35℃で30時間反応させた。その後、枝切り酵素(GODO-FIA、合同酒精株式会社製)を固形分(g)当たり1.0質量%添加し、50℃で20時間反応させた。この澱粉分解物の溶液を、活性炭脱色、イオン精製し、固形分濃度40質量%に濃縮した。該濃縮液を、65℃で10日間保持し、得られた沈殿を、固形分が溶け出さなくなるまで水洗と遠心分離を繰り返して分離した後、凍結乾燥して粉末化した実施例5の結晶澱粉分解物を得た。[Example 5]
To a 30% by mass tapioca starch slurry adjusted to pH 5.8 with 10% calcium hydroxide, 0.2% by mass of α-amylase (Clistase T10S, manufactured by Amano Enzyme Co., Ltd.) was added per solid content (g). , and liquefied in a jet cooker (temperature 110°C). This liquefied liquid was kept at 95° C., DE was measured over time, and when DE reached 15, the pH was adjusted to 4.0 with 10% hydrochloric acid and the reaction was stopped by boiling. After the reaction was stopped, the pH of the sugar solution was adjusted to 5.8, and then 2000 units of potato-derived branch-forming enzyme per solid content (g) was added, and the mixture was reacted at 35° C. for 30 hours. Thereafter, 1.0% by mass of a branch cutting enzyme (GODO-FIA, manufactured by Godo Shusei Co., Ltd.) was added based on the solid content (g), and the mixture was reacted at 50°C for 20 hours. This starch decomposition product solution was decolorized with activated carbon, ion-purified, and concentrated to a solid content concentration of 40% by mass. The concentrated solution was maintained at 65° C. for 10 days, and the resulting precipitate was separated by repeated washing with water and centrifugation until no solid content was dissolved out, and then lyophilized to form the crystalline starch of Example 5. A decomposition product was obtained.
[実施例6]
10%塩酸にてpH2.0に調整した30質量%のワキシーコーンスターチスラリーを、130℃の温度条件でDE6まで分解した。常圧に戻した後、水酸化ナトリウムを用いて反応を停止した糖液のpHを5.8に調整した後、細菌由来枝作り酵素を固形分(g)当たり500ユニット、枝切り酵素(GODO-FIA、合同酒精株式会社製)を固形分(g)当たり0.5質量%添加し、50℃で72時間反応させた。この澱粉分解物の溶液を、活性炭脱色、イオン精製した。該精製糖液を、4℃で10日保持し、得られた沈殿を、固形分が溶け出さなくなるまで水洗と遠心分離を繰り返して分離した後、スプレードライヤーで粉末化し、実施例6の結晶澱粉分解物を得た。[Example 6]
A 30% by mass waxy cornstarch slurry adjusted to pH 2.0 with 10% hydrochloric acid was decomposed to DE6 at a temperature of 130°C. After returning to normal pressure, the pH of the sugar solution that had stopped the reaction was adjusted to 5.8 using sodium hydroxide, and then 500 units of bacterial branching enzyme per solid content (g) and branching enzyme (GODO) were added. -FIA, manufactured by Godo Shushu Co., Ltd.) was added in an amount of 0.5% by mass based on the solid content (g), and the mixture was reacted at 50°C for 72 hours. The solution of this starch decomposition product was decolorized with activated carbon and subjected to ion purification. The purified sugar solution was kept at 4°C for 10 days, and the resulting precipitate was separated by repeating water washing and centrifugation until no solid content dissolved out, and then powdered with a spray dryer to obtain the crystalline starch of Example 6. A decomposition product was obtained.
[参考例7]
実施例2の濃縮後の糖液を、4℃で3時間保持し、得られた沈殿を含有した糖液をスプレードライヤーで粉末化し、参考例7の結晶澱粉分解物を得た。
[ Reference example 7]
The concentrated sugar solution of Example 2 was held at 4° C. for 3 hours, and the resulting sugar solution containing the precipitate was pulverized using a spray dryer to obtain a crystalline starch decomposition product of Reference Example 7.
[参考例8]
参考例8の結晶澱粉分解物として、実施例3のスプレードライ後の粉末を用いた。
[ Reference example 8]
As the crystalline starch decomposition product of Reference Example 8, the spray-dried powder of Example 3 was used.
[実施例9]
10%塩酸にてpH2.0に調整した20質量%のコーンスターチスラリーを、130℃の温度条件でDE17まで分解した。常圧に戻した後、10質量%水酸化ナトリウムを用いて中和することにより反応を停止した糖液のpHを5.8に調整した後、枝切り酵素(イソアミラーゼ、シグマアルドリッチ ジャパン株式会社製)を固形分(g)当たり1.0質量%添加し、45℃で50時間反応させた。この澱粉分解物の溶液を、活性炭脱色、イオン精製し、固形分濃度45質量%に濃縮した。該濃縮液を、4℃で3日間保持し、得られた沈殿を固形分が溶け出さなくなるまで水洗い、遠心分離を繰り返し、凍結乾燥によって実施例9の結晶含有澱粉分解物を得た。[Example 9]
A 20% by mass cornstarch slurry adjusted to pH 2.0 with 10% hydrochloric acid was decomposed to DE17 at a temperature of 130°C. After returning to normal pressure, the pH of the sugar solution was adjusted to 5.8 by neutralizing the reaction with 10% by mass sodium hydroxide, and then a debranching enzyme (isoamylase, Sigma-Aldrich Japan Co., Ltd.) was added. 1.0% by mass based on the solid content (g) was added and reacted at 45°C for 50 hours. This starch decomposition product solution was decolorized with activated carbon, ion-purified, and concentrated to a solid content concentration of 45% by mass. The concentrated solution was kept at 4° C. for 3 days, and the resulting precipitate was washed with water and centrifuged repeatedly until no solid content was dissolved out, followed by freeze-drying to obtain the crystal-containing starch decomposition product of Example 9.
[比較例1]
10%水酸化ナトリウムにてpH5.8に調整した30質量%のワキシーコーンスターチスラリーに、αアミラーゼ(リコザイムスープラ、ノボザイムズ株式会社製)を、固形分(g)当たり0.2質量%添加し、ジェットクッカー(温度110℃)で液化した。この液化液を95℃で保温し、継時的にDEを測定し、DE6になった時点で、10%塩酸でpH4.0に調整し、煮沸により反応を停止した。反応を停止した糖液のpHを5.8に調整した後、枝切り酵素(GODO-FIA、合同酒精株式会社製)を固形分(g)当たり2.0質量%添加し、50℃で48時間反応させた。反応中から多量の沈殿が確認され、反応終了後はそのまま室温で1日放冷した。反応中及び放冷で得られた沈殿を、固形分が溶け出さなくなるまで水洗と遠心分離を繰り返して分離した後、凍結乾燥して粉末化した比較例1の結晶澱粉分解物を得た。[Comparative example 1]
To a 30% by mass waxy corn starch slurry adjusted to pH 5.8 with 10% sodium hydroxide, 0.2% by mass of α-amylase (Ricozyme Supra, manufactured by Novozymes Inc.) was added per solid content (g), It was liquefied in a jet cooker (temperature 110°C). This liquefied liquid was kept at 95° C., DE was measured over time, and when DE reached 6, the pH was adjusted to 4.0 with 10% hydrochloric acid and the reaction was stopped by boiling. After adjusting the pH of the sugar solution after stopping the reaction to 5.8, debranching enzyme (GODO-FIA, manufactured by Godo Shusei Co., Ltd.) was added at 2.0% by mass per solid content (g), and the pH was adjusted to 48% at 50°C. Allowed time to react. A large amount of precipitate was observed during the reaction, and after the reaction was completed, the mixture was left to cool at room temperature for one day. The precipitate obtained during the reaction and during cooling was separated by repeating water washing and centrifugation until no solid content dissolved out, and then freeze-dried to obtain a powdered crystalline starch decomposition product of Comparative Example 1.
[比較例2]
比較例2の結晶糖質として、株式会社林原の「トレハ」(登録商標)(トレハロース)を用いた。[Comparative example 2]
As the crystalline carbohydrate in Comparative Example 2, "Treha" (registered trademark) (trehalose) manufactured by Hayashibara Co., Ltd. was used.
[比較例3]
比較例3の結晶糖質として、株式会社光洋商会の「エンデュランスMCC VE-050」(結晶セルロース)を用いた。[Comparative example 3]
As the crystalline carbohydrate in Comparative Example 3, "Endurance MCC VE-050" (crystalline cellulose) manufactured by Koyo Shokai Co., Ltd. was used.
[比較例4]
実施例1の澱粉分解物の溶液を、活性炭脱色、イオン精製した後、濃縮せずにそのままスプレードライで粉末化して、比較例4の澱粉分解物を得た。[Comparative example 4]
The solution of the starch decomposition product of Example 1 was subjected to activated carbon decolorization and ion purification, and then powdered as it was by spray drying without concentrating to obtain the starch decomposition product of Comparative Example 4.
(3)測定
前記で得られた実施例1~6、参考例7、8、実施例9及び比較例1~4について、DP8~19及びDP20以上の含有量を、前述した方法で測定した。また、粉末X線回折を前述した方法で行い、その結果から結晶の型を判定し、前述した方法にて結晶化比率(%)を算出した。また、前記で得られた実施例1~6、参考例7、8、実施例9及び比較例1~4の溶解性、甘味性、及び吸湿性についても、前述した方法で評価した。結果を下記の表2に示す。また、A型結晶の例として実施例1、B型結晶の例として実施例2、非結晶の例として比較例4の粉末X線回折のチャートを図1~3にそれぞれ示す。
(3) Measurement For Examples 1 to 6, Reference Examples 7 and 8 , Example 9, and Comparative Examples 1 to 4 obtained above, the content of DP 8 to 19 and DP 20 or more was measured by the method described above. In addition, powder X-ray diffraction was performed using the method described above, the crystal type was determined from the results, and the crystallization ratio (%) was calculated using the method described above. In addition, the solubility, sweetness, and hygroscopicity of Examples 1 to 6, Reference Examples 7 and 8 , Example 9, and Comparative Examples 1 to 4 obtained above were also evaluated using the methods described above. The results are shown in Table 2 below. Further, powder X-ray diffraction charts of Example 1 as an example of A-type crystal, Example 2 as an example of B-type crystal, and Comparative Example 4 as an amorphous example are shown in FIGS. 1 to 3, respectively.
表2に示す通り、実施例1~6、参考例7、8、実施例9は、20℃の溶解性は全て不溶又は白濁であったが、100℃では、全て溶解性を示していた。 As shown in Table 2, Examples 1 to 6, Reference Examples 7 and 8, and Example 9 were all insoluble or cloudy at 20°C, but all showed solubility at 100°C.
また、実施例の中で比較すると、水洗を行わなかった参考例7及び8に比べ、水洗を行った実施例1~6及び9の方が、甘味性評価及び吸湿性評価が良好であった。甘味性評価及び吸湿性評価が良好な実施例1~6及び9は、結晶化比率が10%以上であり、かつ、20℃の水に分散した際の上清Brix値が2.0%以下であった。この結果から、分離
工程を行うことで、結晶化比率が10%以上であり、かつ、20℃の水に分散した際の上清Brix値が2.0%以下である、低甘味性かつ低吸湿性の結晶澱粉分解物を得ることができることが分かった。
Furthermore, when compared among the Examples, Examples 1 to 6 and 9, which were washed with water, had better sweetness evaluation and hygroscopicity evaluation than Reference Examples 7 and 8, which were not washed with water. . Examples 1 to 6 and 9 with good sweetness evaluation and hygroscopicity evaluation have a crystallization ratio of 10% or more and a supernatant Brix value of 2.0% or less when dispersed in water at 20°C. Met. From this result, by performing the separation process, it is possible to achieve a crystallization ratio of 10% or more, a supernatant Brix value of 2.0% or less when dispersed in water at 20°C, low sweetness and low It has been found that a hygroscopic crystalline starch decomposition product can be obtained.
一方、DP8~19の含有量が40%未満であり、DP20以上の含有量が55%を超える比較例1は、結晶化比率は15%であったが、100℃でも完全に溶解しなかった。それは、高分子成分の溶け残りが影響していると考えられる。トレハロースである比較例2は、結晶ではあるが、20℃においても溶解してしまい、甘味が強く、吸湿性評価も劣っていた。結晶セルロースである比較例3は、100℃でも溶解しなかったため、DP8~19の含有量、及びDP20以上の含有量を測定することができなかった。比較例4は、DP8~19の含有量が40%以上であり、DP20以上の含有量が55%以下であったが、結晶化比率が低く、結晶ではないと考えられ、20℃でも溶解してしまい、甘味が感じられ、吸湿性が非常に劣っていた。 On the other hand, in Comparative Example 1, in which the content of DP8 to 19 was less than 40% and the content of DP20 or more exceeded 55%, the crystallization ratio was 15%, but it did not completely dissolve even at 100 ° C. . This is thought to be caused by undissolved polymer components. Although Comparative Example 2, which is trehalose, was crystalline, it dissolved even at 20°C, had a strong sweet taste, and had poor hygroscopicity evaluation. Comparative Example 3, which is crystalline cellulose, did not dissolve even at 100°C, so it was not possible to measure the content of DP 8 to 19 and the content of DP 20 or higher. In Comparative Example 4, the content of DP8 to 19 was 40% or more, and the content of DP20 or higher was 55% or less, but the crystallization ratio was low and it was considered that it was not a crystal, and it did not dissolve even at 20 ° C. It tasted sweet, and its hygroscopicity was very poor.
なお、室温より低い温度で結晶化を行った実施例2,4,6,参考例7,及び実施例9については、B型の結晶ができ、室温より高い温度で結晶化を行った実施例1,3,5,及び参考例8については、A型の結晶ができることが分かった。 In addition, in Examples 2, 4, 6, Reference Example 7, and Example 9, in which crystallization was performed at a temperature lower than room temperature, type B crystals were formed, and in Examples 2, 4, 6, Reference Example 7, and Example 9, in which crystallization was performed at a temperature higher than room temperature. Regarding Examples 1, 3, 5, and Reference Example 8, it was found that type A crystals were formed.
<実験例2>
実験例2では、前記実験例1で製造した結晶澱粉分解物又は結晶前の澱粉分解物を、飲食品用組成物、飲食品、医薬品、化粧料、及び工業製品に適用した場合について、検証した。<Experiment example 2>
In Experimental Example 2, the case where the crystalline starch decomposition product or pre-crystallization starch decomposition product produced in Experimental Example 1 was applied to food and drink compositions, food and drink products, pharmaceuticals, cosmetics, and industrial products was verified. .
(1)じゃがいもの冷製スープ
皮をむいて適当な大きさに切ったじゃがいも300質量部及び玉ねぎ50質量部を水300質量部で茹で、ミキサーで破砕した後に牛乳300質量部とともに煮立て、塩とこしょうで味を整えた。約30℃になったところで実施例1の結晶澱粉分解物80質量部を加えた後、冷蔵庫で冷やしてじゃがいもの冷製スープを得た。得られたじゃがいもの冷製スープは、結晶由来の舌触りが感じられ、濃厚感が付与された良好な品質であった。(1) Cold potato soup Boil 300 parts by mass of potatoes and 50 parts by mass of onions, peeled and cut into appropriate sizes, in 300 parts by mass of water, crush with a mixer, boil with 300 parts of milk, and add salt. Season to taste with pepper. When the temperature reached about 30°C, 80 parts by mass of the crystalline starch decomposition product of Example 1 was added, and the mixture was cooled in a refrigerator to obtain a cold potato soup. The resulting cold potato soup had a texture derived from the crystals and was of good quality with a rich texture.
(2)牛乳プリン
水19質量部に脱脂粉乳6質量部、砂糖5質量部、ゼラチン1質量部を添加し、沸騰浴で溶かし、約50℃になったところで実施例2又は実施例9の結晶澱粉分解物4質量部を添加し、型に移して4℃で固めて牛乳プリンを得た。得られた牛乳プリンは、白さがより強調された良好な品質であった。(2) Milk pudding 6 parts by mass of skim milk powder, 5 parts by mass of sugar, and 1 part by mass of gelatin were added to 19 parts by mass of water, dissolved in a boiling bath, and when the temperature reached about 50°C, the crystals of Example 2 or Example 9 were crystallized. 4 parts by mass of starch decomposition product was added, transferred to a mold, and solidified at 4°C to obtain milk pudding. The obtained milk pudding was of good quality with enhanced whiteness.
(3)錠剤
実施例3の結晶澱粉分解物80質量部にL-アスコルビン酸粉末20質量部を加え、錠剤成型器で錠剤を作製した。結着が良く、吸湿性の低いビタミンC錠剤が得られた。(3) Tablets 20 parts by mass of L-ascorbic acid powder was added to 80 parts by mass of the crystalline starch decomposition product of Example 3, and tablets were produced using a tablet molding machine. Vitamin C tablets with good binding and low hygroscopicity were obtained.
(4)粉末飲料
実施例4の結晶澱粉分解物100質量部に、濃く煮出した後に約20℃まで冷ました緑茶50質量部を加えよく混合したところ、スラリー化することなく粉末状態が維持された良好な粉末飲料が得られた。(4) Powdered beverage When 100 parts by mass of the crystalline starch decomposition product of Example 4 was added with 50 parts by mass of green tea that had been boiled to a high concentration and then cooled to approximately 20°C and mixed well, the powder state was maintained without becoming a slurry. A good powdered beverage was obtained.
(5)粉末油脂
実施例5の結晶澱粉分解物100質量部にサラダ油20質量部を加えよく混合したところ、スラリー化することなく粉末状態が維持された良好な粉末油脂が得られた。(5) Powdered fat When 20 parts by mass of salad oil was added to 100 parts by mass of the crystalline starch decomposition product of Example 5 and mixed well, a good powdered fat was obtained which maintained a powder state without becoming a slurry.
(6)化粧用クリーム
実施例1の結晶澱粉分解物2質量部、セトステアリルアルコール4質量部、スクワラン40質量部、流動パラフィン5質量部、ミツロウ3質量部、還元ラノリン5質量部、エチルパラベン0.1質量部、モノステアリン酸グリセリド2質量部、グリセリン5質量部、精製水33.9質量部を配合し、常法に従い化粧用クリームを製造した。その結果、良好なクリームが得られた。(6) Cosmetic cream 2 parts by mass of the crystalline starch decomposition product of Example 1, 4 parts by mass of cetostearyl alcohol, 40 parts by mass of squalane, 5 parts by mass of liquid paraffin, 3 parts by mass of beeswax, 5 parts by mass of reduced lanolin, 0 parts by mass of ethylparaben .1 part by mass, 2 parts by mass of glyceride monostearate, 5 parts by mass of glycerin, and 33.9 parts by mass of purified water to produce a cosmetic cream according to a conventional method. As a result, a good cream was obtained.
(7)研磨剤
実施例2の結晶澱粉分解物粉末を、そのまま研磨剤として台所シンク回りの汚れに対しスポンジを用いて研磨したところ、良好に汚れが落とされた。本技術に係る結晶澱粉分解物は、水に溶けない固形物であり、その粒子の形や大きさが比較的揃っており、また、生分解性であるという特徴を有することから、研磨剤として好適に使用することができた。(7) Abrasive When the crystalline starch decomposition product powder of Example 2 was directly used as an abrasive to polish stains around the kitchen sink using a sponge, the stains were successfully removed. The crystalline starch decomposition product according to this technology is a solid substance that is insoluble in water, has relatively uniform particle shapes and sizes, and is biodegradable, so it can be used as an abrasive. It was able to be used suitably.
(8)ドーナツのアイシング・グレーズ
実施例1又は実施例9の結晶化前の澱粉分解物20質量部に水6質量部を加えて溶解し、揚げたてのドーナツの上面にかけて室温で1時間静置し、アイシングドーナツを製造した。また、実施例1又は実施例9の結晶化前の澱粉分解物20質量部に水15質量部を加えて溶解し、揚げたてのドーナツ全体に塗布して室温で1時間静置し、グレーズドーナツを製造した。製造した各ドーナツを、25℃、相対湿度90%で、48時間保存した。(8) Donut icing/glaze Add 6 parts by mass of water to 20 parts by mass of the starch decomposition product before crystallization of Example 1 or Example 9, dissolve it, and pour it over the top of freshly fried donuts and let it stand at room temperature for 1 hour. , manufactured icing donuts. In addition, 15 parts by mass of water was added to 20 parts by mass of the starch decomposition product before crystallization of Example 1 or Example 9, dissolved, and applied to the entire freshly fried donut and allowed to stand at room temperature for 1 hour to form a glazed donut. Manufactured. Each donut produced was stored at 25° C. and 90% relative humidity for 48 hours.
比較のために、前記澱粉分解物の代わりに、DE16.5のデキストリン(商品名「L‐SPD」(昭和産業株式会社製))と、粉糖と、をそれぞれ用いて、デキストリンには水6質量部、粉糖には水4質量部を加えて溶解し、前記と同様に、アイシングドーナツを製造した。製造した各ドーナツを、25℃、相対湿度90%で、48時間保存した。 For comparison, dextrin with a DE of 16.5 (trade name "L-SPD" (manufactured by Showa Sangyo Co., Ltd.)) and powdered sugar were used instead of the starch decomposition product, and the dextrin contained 6 ml of water. 4 parts by weight of powdered sugar were added and dissolved in 4 parts by weight of water, and icing donuts were produced in the same manner as described above. Each donut produced was stored at 25° C. and 90% relative humidity for 48 hours.
製造した各ドーナツ及び保存後の各ドーナツのアイシング又はグレーズの白さ、べたつきについて、下記の評価基準に基づいて評価した。 The whiteness and stickiness of the icing or glaze of each manufactured donut and each donut after storage were evaluated based on the following evaluation criteria.
[白さの評価基準]
○:白く不透明で、良好
△:やや白く半透明
×:透明で白さがない[Whiteness evaluation criteria]
○: White and opaque, good △: Slightly white and translucent ×: Transparent, no whiteness
[べたつきの評価基準]
○:べたつかず、非常に良好
△:ややべたつくが、良好
×:べたつく[Stickness evaluation criteria]
○: Not sticky, very good △: Slightly sticky, but good ×: Sticky
結果を、下記の表3に示す。また、実施例1の結晶化前の澱粉分解物を用いたアイシングドーナツと、粉糖を用いたアイシングドーナツの、保存前・保存後の写真を図4に示す。 The results are shown in Table 3 below. Further, FIG. 4 shows photographs of the icing donut using the starch decomposition product before crystallization of Example 1 and the icing donut using powdered sugar before and after storage.
表3に示す通り、デキストリンを用いたアイシングは、水あめ状で固まらなかった。粉糖を用いたアイシングは、保存前は白く不透明で、べたつきもなく良好であったが、保存するにつれて、吸湿してしまったために潮解が起こり、透明で白さがなくなり、べたつきも生じ、評価が低下した(図4参照)。 As shown in Table 3, the icing using dextrin was syrup-like and did not harden. The icing made with powdered sugar was white, opaque, and non-sticky before storage, but as it was stored, it absorbed moisture and deliquesced, losing its transparent whiteness and becoming sticky. decreased (see Figure 4).
これに対して、実施例1又は実施例9の結晶化前の澱粉分解物を用いたアイシングは、白さ・べたつき共に、保存後も保存前の良好な状態を維持した結果であった(図4参照)。また、実施例1又は実施例9の結晶化前の澱粉分解物を用いたグレーズについても、薄い膜状のため白さは目立たない結果であったが、保存後も保存前の状態を維持し、また、べたつきについては、保存後も保存前の良好な状態を維持した結果であった。 On the other hand, the icing using the starch decomposition product before crystallization of Example 1 or Example 9 maintained its good whiteness and stickiness even after storage (Fig. (see 4). In addition, regarding the glaze using the starch decomposition product before crystallization in Example 1 or Example 9, the whiteness was not noticeable because it was a thin film, but the state before storage was maintained even after storage. Also, regarding stickiness, the good condition before storage was maintained even after storage.
この結果から、本技術を用いることで、吸湿によってべたつかず、白色を維持したアイシングやグレーズが作製できることが分かった。また、本技術に係る結晶澱粉分解物は甘味度が低いので、甘味料や他の調味料での味の調整が容易であることが分かった。 These results showed that by using this technology, it was possible to create icing and glaze that did not become sticky due to moisture absorption and maintained their white color. Furthermore, it was found that since the crystalline starch decomposition product according to the present technology has a low degree of sweetness, the taste can be easily adjusted with sweeteners or other seasonings.
(9)可食性プラスチック様物質
実施例3の結晶化前の澱粉分解物50gに、水を15g添加して袋の中でよく混錬した後、型に入れて3時間静置後に型から取り外し、可食性プラスチック様物質を製造した。(9) Edible plastic-like substance Add 15 g of water to 50 g of the starch decomposition product before crystallization of Example 3, mix well in a bag, put it in a mold, let it stand for 3 hours, and then remove it from the mold. , produced an edible plastic-like material.
比較のために、前記澱粉分解物の代わりに、DE16.5のデキストリン(商品名「L‐SPD」(昭和産業株式会社製))を用いて、前記と同様の方法にて、可食性プラスチック様物質を製造した。 For comparison, in place of the starch decomposition product, dextrin with a DE of 16.5 (trade name "L-SPD" (manufactured by Showa Sangyo Co., Ltd.)) was used, and an edible plastic-like material was prepared in the same manner as above. produced the substance.
実施例3の結晶化前の澱粉分解物を用いた場合、図5に示すような樹脂状の可食性プラスチック様物質が得られたが、DE16.5のデキストリン(商品名「L‐SPD」(昭和産業株式会社製))を用いた場合、水あめ状のものしか得られなかった。 When the starch decomposition product before crystallization of Example 3 was used, a resin-like edible plastic-like substance as shown in FIG. 5 was obtained. When using Showa Sangyo Co., Ltd.), only a starch syrup-like product was obtained.
この結果から、本技術を用いることで、可食性、生分解性の樹脂状の成型物が得られることが分かった。そして、得られた成型物は、水濡れや湿気に強く、添加する水の量を調整することで硬さをコントロールでき、可塑剤(ソルビトール、グリセリン等)等を加えることで柔軟性をコントロールできることが分かった。また、きれいな白色のため、着色料による色の映えも良いことが分かった。更に、同じ要領で、少量ずつ塗布、積層することにより、文字ペンや3Dプリンターの原液としても応用できることが分かった(図6参照)。 From this result, it was found that by using this technology, an edible, biodegradable resin-like molded product can be obtained. The resulting molded product is resistant to water and humidity, and its hardness can be controlled by adjusting the amount of water added, and its flexibility can be controlled by adding plasticizers (sorbitol, glycerin, etc.). I understand. In addition, it was found that because of its beautiful white color, the colors reflected well with the coloring agent. Furthermore, it was found that by applying and layering small amounts in the same manner, it could be applied as a stock solution for character pens and 3D printers (see Figure 6).
Claims (12)
グルコース重合度(DP)20以上の含有量が18%以上55%以下、
X線回折法の結果から算出される結晶化比率が10%以上であり、
澱粉又は澱粉分解中間物の枝切り酵素及び枝作り酵素処理物の結晶化物、及び/又は、澱粉又は澱粉分解中間物の酸液化物の枝切り酵素処理物の結晶化物である結晶澱粉分解物。 The content of glucose polymerization degree (DP) 8 to 19 is 40% or more,
The content of glucose polymerization degree (DP) 20 or more is 18% or more and 55% or less,
The crystallization ratio calculated from the results of X-ray diffraction is 10% or more,
A crystallized product of starch or a starch decomposition intermediate treated with a debranching enzyme and a debranching enzyme , and/or a crystallized product of a debranching enzyme-treated product of an acid liquefied starch or a starch decomposition intermediate.
グルコース重合度(DP)8~19の含有量が45%以上、
グルコース重合度(DP)20以上の含有量が21%以上30%以下、である澱粉分解物を得る酵素反応工程と、
前記澱粉分解物を、結晶化して、
グルコース重合度(DP)8~19の含有量が40%以上、
グルコース重合度(DP)20以上の含有量が18%以上55%以下、
X線回折法の結果から算出される結晶化比率が10%以上である結晶澱粉分解物を得る結晶化工程と、
を行う、結晶澱粉分解物の製造方法。 A debranching enzyme and a branching enzyme are applied to starch or a starch decomposition intermediate at the same time or after the action of the branching enzyme,
The content of glucose polymerization degree (DP) 8 to 19 is 45% or more,
an enzymatic reaction step for obtaining a starch decomposition product having a glucose polymerization degree (DP) of 20 or more and a content of 21% or more and 30% or less;
Crystallizing the starch decomposition product ,
The content of glucose polymerization degree (DP) 8 to 19 is 40% or more,
The content of glucose polymerization degree (DP) 20 or more is 18% or more and 55% or less,
a crystallization step of obtaining a crystalline starch decomposition product having a crystallization ratio calculated from the results of X-ray diffraction method of 10 % or more;
A method for producing a crystalline starch decomposition product.
グルコース重合度(DP)8~19の含有量が45%以上、
グルコース重合度(DP)20以上の含有量が21%以上30%以下、である澱粉分解物を得る酵素反応工程と、
前記澱粉分解物を、結晶化して、
グルコース重合度(DP)8~19の含有量が40%以上、
グルコース重合度(DP)20以上の含有量が18%以上55%以下、
X線回折法の結果から算出される結晶化比率が10%以上である結晶澱粉分解物を得る結晶化工程と、
を行う、結晶澱粉分解物の製造方法。 After adding acid to starch or starch decomposition intermediates and liquefying them, debranching enzymes are applied,
The content of glucose polymerization degree (DP) 8 to 19 is 45% or more,
an enzymatic reaction step for obtaining a starch decomposition product having a glucose polymerization degree (DP) of 20 or more and a content of 21% or more and 30% or less;
Crystallizing the starch decomposition product ,
The content of glucose polymerization degree (DP) 8 to 19 is 40% or more,
The content of glucose polymerization degree (DP) 20 or more is 18% or more and 55% or less,
a crystallization step of obtaining a crystalline starch decomposition product having a crystallization ratio calculated from the results of X-ray diffraction method of 10 % or more;
A method for producing a crystalline starch decomposition product.
グルコース重合度(DP)20以上の含有量が21%以上30%以下、であり、
澱粉又は澱粉分解中間物の枝切り酵素及び枝作り酵素処理物、及び/又は、澱粉又は澱粉分解中間物の酸液化物の枝切り酵素処理物であり、
グルコース重合度(DP)8~19の含有量が40%以上、
グルコース重合度(DP)20以上の含有量が18%以上55%以下、
X線回折法の結果から算出される結晶化比率が10%以上の結晶澱粉分解物を含有する、飲食品用組成物、飲食品、医薬品、化粧料、工業製品、飼料、培地、又は肥料。 The content of glucose polymerization degree (DP) 8 to 19 is 45% or more,
The content of glucose polymerization degree (DP) of 20 or more is 21% or more and 30% or less,
A debranching enzyme and a debranching enzyme-treated product of starch or a starch decomposition intermediate, and/or a debranching enzyme-treated product of an acid liquefied starch or a starch decomposition intermediate ,
The content of glucose polymerization degree (DP) 8 to 19 is 40% or more,
The content of glucose polymerization degree (DP) 20 or more is 18% or more and 55% or less,
A food or drink composition, a food or drink, a pharmaceutical, a cosmetic, an industrial product, a feed, a culture medium, or a fertilizer containing a crystalline starch decomposition product with a crystallization ratio of 10% or more calculated from the results of an X-ray diffraction method.
グルコース重合度(DP)20以上の含有量が21%以上30%以下、であり、
澱粉又は澱粉分解中間物の枝切り酵素及び枝作り酵素処理物、及び/又は、澱粉又は澱粉分解中間物の酸液化物の枝切り酵素処理物である澱粉分解物の一部又は全部を結晶化して、
グルコース重合度(DP)8~19の含有量が40%以上、
グルコース重合度(DP)20以上の含有量が18%以上55%以下、
X線回折法の結果から算出される結晶化比率が10%以上である結晶澱粉分解物を得る結晶化工程、を行う飲食品用組成物、飲食品、医薬品、化粧料、工業製品、飼料、培地、又は肥料の製造方法。 The content of glucose polymerization degree (DP) 8 to 19 is 45% or more,
The content of glucose polymerization degree (DP) of 20 or more is 21% or more and 30% or less,
Crystallizing part or all of a starch decomposition product that is a debranching enzyme and a debranching enzyme-treated product of starch or a starch decomposition intermediate, and/or a debranching enzyme-treated product of an acid liquefied starch or a starch decomposition intermediate. hand ,
The content of glucose polymerization degree (DP) 8 to 19 is 40% or more,
The content of glucose polymerization degree (DP) 20 or more is 18% or more and 55% or less,
Compositions for food and drink products, food and drink products, pharmaceuticals, cosmetics, industrial products, feeds, which perform a crystallization process to obtain a crystalline starch decomposition product with a crystallization ratio calculated from the results of X-ray diffraction method of 10% or more; Method for producing culture medium or fertilizer.
及び/又は、
澱粉又は澱粉分解中間物に酸を加えて液化した後、枝切り酵素を作用させて、澱粉分解物を得る酵素反応工程と、
前記澱粉分解物を、結晶化して、
グルコース重合度(DP)8~19の含有量が40%以上、
グルコース重合度(DP)20以上の含有量が18%以上55%以下、
X線回折法の結果から算出される結晶化比率が10%以上である結晶澱粉分解物を得る結晶化工程と、
を行う、結晶澱粉分解物の製造方法。
an enzymatic reaction step in which a debranching enzyme and a debranching enzyme act on starch or a starch decomposition intermediate to obtain a starch decomposition product ;
and/or
An enzymatic reaction step of adding an acid to starch or a starch decomposition intermediate to liquefy it, and then acting on a debranching enzyme to obtain a starch decomposition product ;
Crystallizing the starch decomposition product,
The content of glucose polymerization degree (DP) 8 to 19 is 40% or more,
The content of glucose polymerization degree (DP) 20 or more is 18% or more and 55% or less,
a crystallization step of obtaining a crystalline starch decomposition product having a crystallization ratio calculated from the results of X-ray diffraction method of 10% or more;
A method for producing a crystalline starch decomposition product.
Applications Claiming Priority (3)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2018110190 | 2018-06-08 | ||
| JP2018110190 | 2018-06-08 | ||
| PCT/JP2019/018953 WO2019235142A1 (en) | 2018-06-08 | 2019-05-13 | Crystalline starch degradation product; food/beverage product composition, food/beverage product, medicinal product, cosmetic, industrial product, feed, medium, and fertilizer employing said crystalline starch degradation product, and modifier therefor; and method for manufacturing said crystalline starch degradation product, food/beverage product composition, food/beverage product, medicinal product, cosmetic, industrial product, feed, medium, and fertilizer |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPWO2019235142A1 JPWO2019235142A1 (en) | 2021-07-08 |
| JP7404233B2 true JP7404233B2 (en) | 2023-12-25 |
Family
ID=68769982
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP2020523584A Active JP7404233B2 (en) | 2018-06-08 | 2019-05-13 | Crystalline starch decomposition products, food and drink compositions, food and drink products, pharmaceuticals, cosmetics, industrial products, feeds, culture media, fertilizers, and modifiers thereof, and the crystalline starch decomposition products using the crystalline starch decomposition products. Methods for producing products, food and drink compositions, food and drink products, pharmaceuticals, cosmetics, industrial products, feeds, culture media, and fertilizers |
Country Status (4)
| Country | Link |
|---|---|
| JP (1) | JP7404233B2 (en) |
| CN (1) | CN112292042B (en) |
| TW (1) | TW202011825A (en) |
| WO (1) | WO2019235142A1 (en) |
Families Citing this family (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP7309448B2 (en) * | 2019-05-20 | 2023-07-18 | フタムラ化学株式会社 | icing material |
| JP7613869B2 (en) * | 2020-10-06 | 2025-01-15 | 昭和産業株式会社 | Texture improver, mix containing same, fried skin food or fried noodle skin using same, and fried skin food or fried noodle |
| JP7649799B2 (en) * | 2020-11-12 | 2025-03-21 | 昭和産業株式会社 | Oil-in-water emulsion composition and food product using said oil-in-water emulsion composition |
| JP2022167684A (en) * | 2021-04-23 | 2022-11-04 | 昭和産業株式会社 | Physical property stabilizer |
| JP2023061211A (en) * | 2021-10-19 | 2023-05-01 | 昭和産業株式会社 | Starch decomposition products for confectionery |
| JP2023104766A (en) * | 2022-01-18 | 2023-07-28 | 昭和産業株式会社 | Starch decomposition product for clothes |
| WO2023152823A1 (en) * | 2022-02-09 | 2023-08-17 | 昭和産業株式会社 | Oil-in-water emulsion composition and food item using oil-in-water emulsion composition |
| JP7717337B2 (en) * | 2022-02-25 | 2025-08-04 | 株式会社アルファテック | Method for producing pregelatinized starch dry powder, pregelatinized starch dry powder, pregelatinized buckwheat dry powder, and pregelatinized starch dry powder production device |
| WO2025173172A1 (en) * | 2024-02-15 | 2025-08-21 | 昭和産業株式会社 | Crystalline starch decomposition product for microbeads, microbeads, method for producing crystalline starch decomposition product for microbeads, cosmetic, method for producing cosmetic, and method for improving heat resistance of crystalline starch decomposition product |
Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2004131683A (en) | 2002-05-14 | 2004-04-30 | Natl Starch & Chem Investment Holding Corp | Resistant starch manufactured by debranching low amylose starch with isoamylase |
| JP2010226988A (en) | 2009-03-26 | 2010-10-14 | Showa Sangyo Co Ltd | Starch degradation product, food additive containing the starch degradation product, food and drink, drug, and method for producing starch degradation product |
| WO2011083438A1 (en) | 2010-01-08 | 2011-07-14 | Consejo Nacional De Investigaciones Cientificas Y Tecnicas (Conicet) | A biodegradable, biocompatible and non-toxic material, sheets consisting of said material and the use thereof in food, pharmaceutical, cosmetic and cleaning products |
| WO2014081807A1 (en) | 2012-11-20 | 2014-05-30 | Kansas State University Research Foundation | Starch spherulites having controlled enzymatic digestion |
| JP2016202106A (en) | 2015-04-24 | 2016-12-08 | 昭和産業株式会社 | Starch decomposition product, and powdery candy, syrup and food and drink prepared therewith |
Family Cites Families (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2640577B2 (en) * | 1991-02-15 | 1997-08-13 | ホクレン農業協同組合連合会 | Nistose crystal and method for producing the same |
| JP4034846B2 (en) * | 1996-12-10 | 2008-01-16 | 株式会社林原生物化学研究所 | Crystalline powdered sugar, production method and use thereof |
-
2019
- 2019-05-13 JP JP2020523584A patent/JP7404233B2/en active Active
- 2019-05-13 CN CN201980038803.7A patent/CN112292042B/en active Active
- 2019-05-13 WO PCT/JP2019/018953 patent/WO2019235142A1/en not_active Ceased
- 2019-05-17 TW TW108116999A patent/TW202011825A/en unknown
Patent Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2004131683A (en) | 2002-05-14 | 2004-04-30 | Natl Starch & Chem Investment Holding Corp | Resistant starch manufactured by debranching low amylose starch with isoamylase |
| JP2010226988A (en) | 2009-03-26 | 2010-10-14 | Showa Sangyo Co Ltd | Starch degradation product, food additive containing the starch degradation product, food and drink, drug, and method for producing starch degradation product |
| WO2011083438A1 (en) | 2010-01-08 | 2011-07-14 | Consejo Nacional De Investigaciones Cientificas Y Tecnicas (Conicet) | A biodegradable, biocompatible and non-toxic material, sheets consisting of said material and the use thereof in food, pharmaceutical, cosmetic and cleaning products |
| WO2014081807A1 (en) | 2012-11-20 | 2014-05-30 | Kansas State University Research Foundation | Starch spherulites having controlled enzymatic digestion |
| JP2016202106A (en) | 2015-04-24 | 2016-12-08 | 昭和産業株式会社 | Starch decomposition product, and powdery candy, syrup and food and drink prepared therewith |
Non-Patent Citations (5)
| Title |
|---|
| HELBERT W. et al.,Morphological and structural features of amylose spherocrystals of A-type,Int. J. Biol. Macromol., 1993, 15(3), pp.183-187 |
| MONTESANTI, Nicole et al.,A-type crystals from dilute solutions of short amylose chains,Biomacromolecules, 2010, 11(11), pp.3049-3058 |
| SHANG, Yaqian et al.,Starch Spherulites Prepared by a Combination of Enzymatic and Acid Hydrolysis of Normal Corn Starch,J. Agric. Food Chem.,2018年06月04日,vol. 66, no. 25,pp. 6357-6363 |
| SRICHUWONG, Sathaporn et al.,Structure of lintnerized starch is related to X-ray diffraction pattern and susceptibility to acid a,Int. J. Biol. Macromol., 2005, 37(3), pp.115-121 |
| VERMEYLEN, Rudi et al.,Amylopectin molecular structure reflected in macromolecular organization of granular starch,Biomacromolecules, 2004, 5(5), pp.1775-1786 |
Also Published As
| Publication number | Publication date |
|---|---|
| CN112292042B (en) | 2024-03-01 |
| CN112292042A (en) | 2021-01-29 |
| TW202011825A (en) | 2020-04-01 |
| JPWO2019235142A1 (en) | 2021-07-08 |
| WO2019235142A1 (en) | 2019-12-12 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| JP7404233B2 (en) | Crystalline starch decomposition products, food and drink compositions, food and drink products, pharmaceuticals, cosmetics, industrial products, feeds, culture media, fertilizers, and modifiers thereof, and the crystalline starch decomposition products using the crystalline starch decomposition products. Methods for producing products, food and drink compositions, food and drink products, pharmaceuticals, cosmetics, industrial products, feeds, culture media, and fertilizers | |
| JP7354237B2 (en) | Modifiers, modification compositions containing the modifiers, foods and drinks, pharmaceuticals, cosmetics, industrial products, feeds, culture media, or fertilizers using these, and methods for modifying these products | |
| CN105614894B (en) | Food products comprising a slowly digestible or digestion resistant saccharide composition | |
| US5073387A (en) | Method for preparing reduced calorie foods | |
| JP6470099B2 (en) | Starch decomposition product, and powdered rice cake, syrup and food and drink using the starch decomposition product | |
| TW589384B (en) | Crystalline powdery saccharide, and uses thereof | |
| JP5507107B2 (en) | Starch degradation product, food additive containing the starch degradation product, food and drink, drug, and method for producing starch degradation product | |
| JP2021515067A (en) | How to make resistant pea dextrin | |
| CN105163604A (en) | Fiber-containing carbohydrate composition | |
| JP7285052B2 (en) | Starch hydrolyzate, composition for food and drink using the starch hydrolyzate, and food and drink | |
| KR20170118816A (en) | FREE FLOWABLE EDIBLE COMPOSITION, FOOD INCLUDING THE SAME, METHOD OF USING THE SAME, AND METHOD FOR MANUFACTURING THE SAME | |
| JP2009161522A (en) | Renal disorder inhibitor | |
| WO2002072594A1 (en) | Branched cyclic tetrassacharide, process for producing the same, and use | |
| JP3102624B2 (en) | Buckwheat candy-containing food | |
| JPH0873482A (en) | Glucide reduced in reducing property and its production and use | |
| TW397840B (en) | Crystalline maltotetraosyl glucoside, and its production and use | |
| JP5839924B2 (en) | Acid gel food | |
| TWI829693B (en) | Modifier, composition for modification containing the modifier, target product, and method for modifying the target product | |
| JP2011200201A (en) | Sugar paste including composite crystalline carbohydrate comprising plurality of saccharides, method for producing the same, and application of the sugar paste | |
| WO2023152823A1 (en) | Oil-in-water emulsion composition and food item using oil-in-water emulsion composition | |
| JP7636157B2 (en) | Modifiers including starch hydrolysates and thickening/gelling agents | |
| JP2020186337A (en) | Starch decomposition product, as well as composition for foods using starch decomposition product, foods, rich enhancer, manufacturing method of foods, and rich enhancing method | |
| JP2006219416A (en) | Nigerose-containing crystals and method for producing the same, crystalline nigerose and method for producing the same, and powdered nigerose | |
| JP2022167684A (en) | Physical property stabilizer | |
| JP3746065B2 (en) | β-maltose hydrous crystal-containing powder, its production method and use |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| A621 | Written request for application examination |
Free format text: JAPANESE INTERMEDIATE CODE: A621 Effective date: 20220307 |
|
| A131 | Notification of reasons for refusal |
Free format text: JAPANESE INTERMEDIATE CODE: A131 Effective date: 20230411 |
|
| A521 | Request for written amendment filed |
Free format text: JAPANESE INTERMEDIATE CODE: A523 Effective date: 20230612 |
|
| A131 | Notification of reasons for refusal |
Free format text: JAPANESE INTERMEDIATE CODE: A131 Effective date: 20230905 |
|
| A521 | Request for written amendment filed |
Free format text: JAPANESE INTERMEDIATE CODE: A523 Effective date: 20231030 |
|
| TRDD | Decision of grant or rejection written | ||
| A01 | Written decision to grant a patent or to grant a registration (utility model) |
Free format text: JAPANESE INTERMEDIATE CODE: A01 Effective date: 20231205 |
|
| A61 | First payment of annual fees (during grant procedure) |
Free format text: JAPANESE INTERMEDIATE CODE: A61 Effective date: 20231213 |
|
| R150 | Certificate of patent or registration of utility model |
Ref document number: 7404233 Country of ref document: JP Free format text: JAPANESE INTERMEDIATE CODE: R150 |