JP2006131772A - Method for producing denatured starch with controlled thermal swelling - Google Patents
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Abstract
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本発明は、熱膨潤が抑制された変性澱粉に関するものであり、さらに詳しくは澱粉に対して5〜20質量%の極性溶媒、15〜30質量%の水を含有する極性溶媒水溶液を澱粉に分散させ、これを糊化開始温度以上100℃未満で加熱して得られることを特徴とする変性澱粉の製造方法に関する。 The present invention relates to a modified starch in which thermal swelling is suppressed, and more specifically, a polar solvent aqueous solution containing 5 to 20% by mass of a polar solvent and 15 to 30% by mass of water is dispersed in the starch. It is related with the manufacturing method of the modified starch characterized by being obtained by heating this above gelatinization start temperature or more and less than 100 degreeC.
従来、澱粉の熱膨潤の抑制する方法としてはエピクロルヒドリン、グリオキザール、トリメタリン酸などの架橋剤を用いて化学的に架橋する方法があった。一方、架橋剤を用いない方法としては、乾熱処理や湿熱処理が提案されている。 Conventionally, as a method of suppressing thermal swelling of starch, there has been a method of chemically crosslinking using a crosslinking agent such as epichlorohydrin, glyoxal, trimetaphosphoric acid or the like. On the other hand, dry heat treatment and wet heat treatment have been proposed as methods that do not use a crosslinking agent.
乾熱処理としては顆粒澱粉またはフラワーを実質的に無水状態にした後に熱処理を行う方法(特表平9−503549号)や、澱粉・オリゴ糖ブレンドを実質的に無水状態にした後に熱処理を行う方法(特表2003−501494号)があった。 Dry heat treatment includes a method in which the granular starch or flour is substantially anhydrous and then heat treated (Japanese Patent Publication No. 9-503549), and a method in which the starch / oligosaccharide blend is substantially anhydrous and then heat treated. (Special Table 2003-501494).
また湿熱処理としては減圧ラインと加圧蒸気ラインとの両方を付設し、内圧、外圧共に耐圧性の密閉できる容器内に澱粉を入れ、減圧とした後、蒸気導入による加圧加熱(120℃以上)を行い、その後冷却する方法(特許第2996707号)や、水分割合が25〜60容量%のエタノール溶液中に澱粉を分散・懸濁し、これを100℃〜130℃に加熱する方法(特許第3365656号)があった。
従来、澱粉懸濁液を加熱すると、ある温度で澱粉粒子が膨潤し、粘度上昇、粒子の崩壊に伴う粘度低下(ブレークダウン)が生じる。しかしながら、スープ、フラワーペースト、ジャムなどの食品用ペーストには、ブレークダウンが生じる澱粉は適さず、熱膨潤を抑制した澱粉が使用されてきた。一方、工業的用途で事務用糊、壁紙用糊剤などの糊剤には、曵糸性を有するものは作業性が悪く、曵糸性の低いものが好まれて使用されてきた。このような粘性を変化させた澱粉としては、架橋剤を用いて化学的に澱粉の膨潤を抑制した架橋澱粉、あるいは物理的に変性したものとして湿熱処理澱粉や特表平9−503549号公報、特表2003−501494号公報などに記載されている澱粉あるいは澱粉・オリゴ糖ブレンド体を中性以上に調整した後、無水状態で加熱処理を行った乾熱処理澱粉が挙げられる。 Conventionally, when a starch suspension is heated, starch particles swell at a certain temperature, resulting in an increase in viscosity and a decrease in viscosity (breakdown) due to the collapse of the particles. However, starches that cause breakdown are not suitable for food pastes such as soups, flour pastes, and jams, and starches that suppress thermal swelling have been used. On the other hand, for industrial use, as pastes such as office glue and wallpaper paste, those having spinnability are poor in workability, and those having low spinnage have been preferred and used. As the starch having such a viscosity changed, a cross-linked starch in which the swelling of the starch is chemically suppressed using a cross-linking agent, or a wet-heat-treated starch or a specially modified one as disclosed in JP 9-503549 A, The dry heat-treated starch which heat-processed in the anhydrous state after adjusting the starch or starch-oligosaccharide blend body described in the Japanese translations of PCT publication No. 2003-501494 etc. to neutrality or more is mentioned.
物理的に変性した澱粉のうち、乾熱処理をした澱粉は熱による着色が起こり、これを使用した最終製品の仕上がりに影響を与える。また湿熱処理澱粉は高温で加圧加熱処理を行う関係上、構造が非常に複雑な機械を使用しなければならない。 Among the physically modified starches, the starch that has been subjected to the dry heat treatment is colored by heat, which affects the finish of the final product using the starch. In addition, the wet heat-treated starch is subjected to pressure and heat treatment at a high temperature, and therefore a machine having a very complicated structure must be used.
本発明者らは、かかる課題を解決するため、鋭意研究の結果、澱粉に対して5〜20質量%の極性溶媒、15〜30質量%の水を含有する極性溶媒水溶液を澱粉に分散させ、これを使用する澱粉の糊化開始温度以上100℃未満で加熱することにより、熱膨潤抑制型変性澱粉が比較的容易に製造できることを発見し、本発明を完成した。 In order to solve this problem, the present inventors have dispersed a polar solvent aqueous solution containing 5 to 20% by mass of a polar solvent and 15 to 30% by mass of water in starch as a result of intensive studies. It was discovered that heat-swelling-inhibited modified starch can be produced relatively easily by heating at a gelatinization start temperature of starch using this or higher and lower than 100 ° C., thereby completing the present invention.
以上説明してきたように、本発明によれば、熱膨潤抑制型変性澱粉を、澱粉に対して5〜20質量%の極性溶媒、15〜30質量%の水を含有する極性溶媒水溶液を澱粉に分散させ、これを使用する澱粉の糊化開始温度以上100℃未満で加熱することにより比較的容易に製造できる。 As described above, according to the present invention, the heat-swelling-inhibited modified starch is converted from starch to a polar solvent aqueous solution containing 5 to 20% by mass of a polar solvent and 15 to 30% by mass of water based on the starch. It can be produced relatively easily by dispersing and heating at a temperature not lower than 100 ° C. and higher than the gelatinization start temperature of the starch using this.
本発明に使用できる澱粉としては馬鈴薯澱粉、コーンスターチ、甘藷澱粉、タピオカ澱粉、サゴ澱粉、米澱粉、アマランサス澱粉等の天然澱粉、それらの加工澱粉(酸分解澱粉、酸化澱粉、エーテル化、エステル化、架橋等の澱粉誘導体、乾熱処理澱粉、湿熱処理澱粉等)が挙げられる。 Examples of starch that can be used in the present invention include potato starch, corn starch, sweet potato starch, tapioca starch, sago starch, rice starch, and amaranthus starch. And starch derivatives such as cross-linking, dry heat-treated starch, and wet heat-treated starch.
本発明で用いる極性溶媒としては、メタノール、エタノール、アセトンなどが挙げられ、これらを1種以上含有したものであればよい。 Examples of the polar solvent used in the present invention include methanol, ethanol, acetone and the like, as long as they contain one or more of these.
本発明で用いる極性溶媒水溶液の極性溶媒の含有量は澱粉に対して5〜20質量%含有していればよい。含有量が5質量%未満では加熱処理中に澱粉が糊化してしまうので好ましくない。また20質量%を超えた場合、加熱処理による効果があまり得られなくなる。 Content of the polar solvent of the polar solvent aqueous solution used by this invention should just contain 5-20 mass% with respect to starch. If the content is less than 5% by mass, starch is gelatinized during the heat treatment, which is not preferable. Moreover, when it exceeds 20 mass%, the effect by heat processing will not be acquired so much.
本発明で用いる極性溶媒水溶液の水の含有量は澱粉に対して15〜30質量%含有していればよい。含有量が15質量%未満では加熱処理による効果があまり得られなくなり、また30質量%を超えた場合、加熱処理中に澱粉が糊化してしまうので好ましくない。。 The water content of the aqueous polar solvent solution used in the present invention may be 15 to 30% by mass with respect to the starch. When the content is less than 15% by mass, the effect of the heat treatment is not obtained so much, and when it exceeds 30% by mass, the starch is gelatinized during the heat treatment, which is not preferable. .
本発明で行う加熱温度は使用する澱粉の糊化開始温度以上100℃未満であればよい。例えばコーンスターチでは糊化開始温度が約70℃であるので、70℃以上で反応すればよい。使用する澱粉の糊化開始温度未満では熱膨潤型(ブレークダウンが少ない)澱粉にはならず、また100℃以上では加圧加熱処理を行う関係上、耐圧性の反応装置を使用しなければならず、構造が非常に複雑な機械を使用しなければならない。 The heating temperature performed by this invention should just be more than the gelatinization start temperature of the starch to be used, and less than 100 degreeC. For example, since corn starch has a gelatinization start temperature of about 70 ° C., the reaction may be performed at 70 ° C. or higher. If it is less than the gelatinization start temperature of the starch used, it will not become a heat-swelling type (low breakdown) starch. First, a machine with a very complex structure must be used.
本発明の熱膨潤抑制型変性澱粉を製造する方法としては以下の方法で行うことが出来る。まず、澱粉に対して5〜20質量%の極性溶媒、15〜30質量%の水を含有する水溶液を調製し、澱粉に分散させる。この時、水溶液の分散量は澱粉に対して20〜50質量%であれば加熱処理時の澱粉の攪拌が比較的うまくいき、製造時の塊(いわゆるダマ)ができにくくなる。その後、ジャケット付の攪拌機やニーダーを用いて品温を糊化開始温度以上100℃未満まで加熱すればよい。このとき攪拌機などを密閉する必要はなく、還流管などを用いて反応系に戻せばよい。加熱処理は、極性溶媒の添加量に応じて、澱粉が熱抑制されるまで適宜温度、時間を調節すればよい。
その後、乾燥、精粉、篩別など通常の処理を行い、変性澱粉を得ることができる。
The method for producing the heat-swelling-inhibited modified starch of the present invention can be carried out by the following method. First, an aqueous solution containing 5 to 20% by mass of a polar solvent and 15 to 30% by mass of water with respect to starch is prepared and dispersed in starch. At this time, when the dispersion amount of the aqueous solution is 20 to 50% by mass with respect to the starch, the stirring of the starch during the heat treatment is relatively successful, and it becomes difficult to form a lump (so-called lumps) during the production. Then, what is necessary is just to heat product temperature to gelatinization start temperature or more and less than 100 degreeC using a stirrer with a jacket, or a kneader. At this time, it is not necessary to seal the stirrer or the like, and it may be returned to the reaction system using a reflux tube or the like. In the heat treatment, the temperature and time may be appropriately adjusted according to the amount of the polar solvent added until the starch is thermally inhibited.
Thereafter, ordinary treatments such as drying, fine powder, and sieving are performed to obtain a modified starch.
以下、本発明を実施例にて更に詳しく説明するが、本発明はこれらの実施例のみに限定されるものではない。 EXAMPLES Hereinafter, although an Example demonstrates this invention in more detail, this invention is not limited only to these Examples.
コーンスターチ100質量部(以下「部」という)に、表1に記載された量の極性溶媒および水25部を混合した水溶液を添加し、ジャケット付攪拌機で30分攪拌した。その後ジャケット温度を85℃まで加温し4時間加熱処理を行った。比較としてコーンスターチ100部に水30部を添加し、同様の処理を行った。得られた混合物を乾燥、精粉し、ブラベンダー社製ビスコグラフを用いて粘度測定を行い、ブレークダウンの比較を行った。なお未処理のコーンスターチも同様に測定した。
粘度測定条件は以下の通りである。
測定濃度:無水8%、全量450g 攪拌速度:75rpm カートリッジ感度:700cmg
温度条件:50℃開始 95℃まで昇温(1.5℃/分) 10分保持
なおブレークダウンは(ピーク粘度)−(95℃10分後粘度)で表し、熱膨潤の指標とした。つまり値が小さいほど熱膨潤抑制効果があると考えられる。結果を表1に示す。
To 100 parts by mass of corn starch (hereinafter referred to as “parts”), an aqueous solution in which the amount of polar solvent described in Table 1 and 25 parts of water were mixed was added, and the mixture was stirred for 30 minutes with a jacketed stirrer. Thereafter, the jacket temperature was heated to 85 ° C. and heat treatment was performed for 4 hours. As a comparison, 30 parts of water was added to 100 parts of corn starch, and the same treatment was performed. The obtained mixture was dried and refined, and the viscosity was measured using a Viscograph manufactured by Brabender Co., Ltd., and the breakdown was compared. The untreated corn starch was also measured in the same manner.
The viscosity measurement conditions are as follows.
Measurement concentration: anhydrous 8%, total amount 450 g Stirring speed: 75 rpm Cartridge sensitivity: 700 cmg
Temperature condition: Start at 50 ° C. Temperature rise to 95 ° C. (1.5 ° C./min) Hold for 10 minutes The breakdown is expressed as (peak viscosity) − (viscosity after 10 minutes at 95 ° C.) and used as an index of thermal swelling. In other words, it is considered that the smaller the value, the more effective the thermal swelling suppression. The results are shown in Table 1.
表1よりエタノールを澱粉に対して5〜20質量%含有する水溶液を分散させ、加熱して得られた変性澱粉は熱膨潤抑制効果があった。またエタノールを含まずに水だけを添加して処理したものは未処理の澱粉と同様にブレークダウンかなり大きかった。 From Table 1, the modified starch obtained by dispersing and heating an aqueous solution containing 5 to 20% by mass of ethanol with respect to starch had a thermal swelling inhibiting effect. Moreover, the thing which added only water and did not contain ethanol, and the unprocessed starch were quite large like breakdown.
コーンスターチ100部に、エタノール10部および水25部を混合した水溶液を添加し、表2記載の加熱温度以外は実施例1と同様の方法で加熱処理を行った。得られた混合物を精粉し、ブラベンダー社製ビスコグラフを用いて実施例1と同様の条件で粘度測定を行い、ブレークダウンの比較を行った。なお未処理の澱粉についても同様に測定した。結果を表2に示す。表中、ピークが存在しない時には「NIL」とした。 An aqueous solution in which 10 parts of ethanol and 25 parts of water were mixed was added to 100 parts of corn starch, and heat treatment was performed in the same manner as in Example 1 except for the heating temperature described in Table 2. The obtained mixture was refined, and the viscosity was measured under the same conditions as in Example 1 using a Brabender Viscograph, and the breakdown was compared. In addition, it measured similarly about unprocessed starch. The results are shown in Table 2. In the table, when there was no peak, “NIL” was assigned.
表2より、糊化開始温度以上である70℃からブレークダウンの減少が始まっているが、75℃以上で熱膨潤抑制効果が顕著に出てくるのがわかった。また98℃では95℃10分後の粘度が濃度に対して低くなりすぎることがわかった。 From Table 2, it was found that the breakdown started to decrease from 70 ° C., which is higher than the gelatinization start temperature, but that the thermal swelling suppression effect is noticeable at 75 ° C. or higher. It was also found that at 98 ° C., the viscosity after 10 minutes at 95 ° C. was too low with respect to the concentration.
表3記載の澱粉100部に、エタノール10部および水25部を混合した水溶液を添加し、実施例1と同様の方法で加熱処理を行った。得られた混合物を精粉し、ブラベンダー社製ビスコグラフを用いて、表3記載の濃度で実施例1と同様の条件で粘度測定を行い、ブレークダウンの比較を行った。なお未処理の澱粉についても同様に測定した。結果を表3に示す。 An aqueous solution obtained by mixing 10 parts of ethanol and 25 parts of water was added to 100 parts of the starch shown in Table 3, and heat treatment was performed in the same manner as in Example 1. The obtained mixture was refined, and the viscosity was measured under the same conditions as in Example 1 at the concentrations shown in Table 3 using a Brabender Viscograph, and the breakdown was compared. In addition, it measured similarly about unprocessed starch. The results are shown in Table 3.
表3より、ワキシコーンスターチを除く澱粉では熱膨潤抑制効果が出てくるのがわかった。ワキシコーンスターチを用いたものは未処理の澱粉に比べるとブレークダウンは小さくなるが、他の澱粉に比べると大きくなってしまう。 From Table 3, it was found that the starch excluding waxy corn starch has a thermal swelling inhibiting effect. Those using waxy corn starch have a smaller breakdown than untreated starch, but are larger than other starches.
<耐酸性試験>
実施例1で作成したエタノール10部添加したものを用いて、無水8%懸濁液を調製し、各pHに調整後、85℃以上10分間加熱した。水分補正後、糊液を30℃まで冷却し、B型粘度計30rpmで粘度を測定した。比較として未処理のコーンスターチを同様の条件で粘度測定を行った。結果を表4に示す
<Acid resistance test>
An anhydrous 8% suspension was prepared using 10 parts of ethanol prepared in Example 1, adjusted to each pH, and heated to 85 ° C. or higher for 10 minutes. After the moisture correction, the paste solution was cooled to 30 ° C., and the viscosity was measured with a B-type viscometer at 30 rpm. As a comparison, the viscosity of untreated corn starch was measured under the same conditions. The results are shown in Table 4.
表4より、原料澱粉にはない低pHでの粘度安定性が付与されているのが分かった。 From Table 4, it was found that viscosity stability at a low pH, which is not found in the raw material starch, was imparted.
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Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
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WO2008143144A1 (en) * | 2007-05-18 | 2008-11-27 | San-Ei Gen F.F.I., Inc. | Starch-containing composition and process for producing the same |
WO2009110610A1 (en) | 2008-03-07 | 2009-09-11 | 三栄源エフ・エフ・アイ株式会社 | Method for modifying starch and method for producing starch blended preparation |
KR101854993B1 (en) * | 2016-09-19 | 2018-05-04 | 경희대학교 산학협력단 | Method for preparing amorphous granular starch using ethanol |
CN110746510A (en) * | 2019-11-05 | 2020-02-04 | 广西民族大学 | Method for simultaneously reducing relative crystallinity and thermal stability of starch |
KR20210030625A (en) * | 2019-09-10 | 2021-03-18 | 경희대학교 산학협력단 | Method for preparing amorphous granular starch using ethanol and high hydrostatic pressure |
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Publication number | Priority date | Publication date | Assignee | Title |
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WO2008143144A1 (en) * | 2007-05-18 | 2008-11-27 | San-Ei Gen F.F.I., Inc. | Starch-containing composition and process for producing the same |
JP5127826B2 (en) * | 2007-05-18 | 2013-01-23 | 三栄源エフ・エフ・アイ株式会社 | Starch-containing composition and method for producing the same |
WO2009110610A1 (en) | 2008-03-07 | 2009-09-11 | 三栄源エフ・エフ・アイ株式会社 | Method for modifying starch and method for producing starch blended preparation |
US10968334B2 (en) | 2008-03-07 | 2021-04-06 | San-Ei Gen F.F.I., Inc. | Method for modifying starch and method for producing starch blended preparation |
KR101854993B1 (en) * | 2016-09-19 | 2018-05-04 | 경희대학교 산학협력단 | Method for preparing amorphous granular starch using ethanol |
KR20210030625A (en) * | 2019-09-10 | 2021-03-18 | 경희대학교 산학협력단 | Method for preparing amorphous granular starch using ethanol and high hydrostatic pressure |
KR102507593B1 (en) | 2019-09-10 | 2023-03-07 | 경희대학교 산학협력단 | Method for preparing amorphous granular starch using ethanol and high hydrostatic pressure |
CN110746510A (en) * | 2019-11-05 | 2020-02-04 | 广西民族大学 | Method for simultaneously reducing relative crystallinity and thermal stability of starch |
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