JP3365656B2 - Method for producing modified starch - Google Patents

Method for producing modified starch

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Publication number
JP3365656B2
JP3365656B2 JP24071793A JP24071793A JP3365656B2 JP 3365656 B2 JP3365656 B2 JP 3365656B2 JP 24071793 A JP24071793 A JP 24071793A JP 24071793 A JP24071793 A JP 24071793A JP 3365656 B2 JP3365656 B2 JP 3365656B2
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Japan
Prior art keywords
starch
volume
degree
swelling
water content
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JP24071793A
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Japanese (ja)
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JPH0770206A (en
Inventor
利章 小巻
昌裕 倉掛
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三和興産株式会社
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Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明は、各種澱粉の高分子的物
理的性質(懸濁液を加熱したときに、澱粉粒が大きく膨
潤し、粘度の高い糊液となる性質)を改変して、常温
(25℃)で吸水・膨潤性が著しく大であって、かつ温
度を上昇させても膨潤度の変化が少ない澱粉を製造する
方法に関するものであり、特に澱粉を水の割合が25〜
60容量%のエタノールのごときアルコール溶液中に分
散・懸濁し、これを密閉状態で加熱して少なくとも10
0℃以上とした後、該澱粉を集めて乾燥・粉砕して変性
澱粉を製造する方法に関する。
BACKGROUND OF THE INVENTION The present invention is to modify the polymer physical properties of various starches (the property that when the suspension is heated, the starch granules swell to a large extent to form a highly viscous paste solution). The present invention relates to a method for producing starch, which has a significantly large water-absorption / swelling property at room temperature (25 ° C.) and whose swelling degree changes little even when the temperature is increased.
Disperse and suspend in an alcohol solution such as 60% by volume of ethanol and heat it in a sealed state for at least 10
The present invention relates to a method for producing a modified starch by collecting the starch after drying at 0 ° C. or higher, drying and pulverizing the starch.

【0002】[0002]

【従来の技術】澱粉の用途は加水分解的利用が最も多
く、その利用割合は全体の約60%に達するが、その他
に高分子的性質の直接的な利用方法がある。後者の利用
の場合、澱粉を水と共に加熱すると、粒が著しく大きく
膨潤して糊液となるが、このときの糊液の粘性、糊化特
性、ゾルの安定性、ゾル−ゲルの転移、ゲルの性質など
の特性が特に重要である。これらの性質は澱粉の種類に
よって随分異なり、当業界ではそれぞれの用途によって
澱粉を使い分けしてきた。
2. Description of the Related Art Starch is most used for hydrolysis, and its utilization ratio reaches about 60% of the whole, but there is a direct method of utilizing its polymer property. In the case of the latter use, when starch is heated with water, the granules swell significantly and become a paste solution. At this time, the viscosity of the paste solution, the gelatinizing property, the stability of the sol, the sol-gel transition, and the gel. Properties such as the properties of are particularly important. These properties vary considerably depending on the type of starch, and in the industry, starch has been used properly according to each application.

【0003】実用的な糊液は、澱粉懸濁液を加熱する間
に糊化温度付近から澱粉の一部が溶解して溶液となり大
部分の澱粉粒が原形を保ったまま大きく膨潤したもの、
膨潤した粒が原形を留めないところまで粒が崩壊したも
のなどが種々さまざまな割合で分散した状態といえる。
このような糊液の性質は特徴であると共に工業的利用の
際に逆に色々障害となることがある。このために種々の
化学的方法で誘導体などのいわゆる化工澱粉とすること
で、これらの物理的性質を改良して用いてきた。特に、
物理的性質の中で澱粉粒の膨潤と澱粉糊の高粘度は特徴
であると共に欠点であるため、当業界では低粘度の澱粉
が要求されており、実際に酸化澱粉、エステル化澱粉等
が生産されている。
A practical paste solution is one in which a part of the starch is dissolved from around the gelatinization temperature during heating of the starch suspension to form a solution, and most of the starch granules are largely swollen while maintaining the original shape,
It can be said that particles that have collapsed to the point where swollen particles do not retain their original shape are dispersed at various ratios.
The properties of such a paste solution are not only characteristic but also sometimes cause various obstacles in industrial use. For this reason, so-called modified starches such as derivatives have been used by various chemical methods to improve their physical properties. In particular,
Among the physical properties, the swelling of starch granules and the high viscosity of starch paste are characteristic and disadvantageous, so low-viscosity starch is required in the industry, and actually oxidized starch, esterified starch, etc. are produced. Has been done.

【0004】しかしながら、食品加工の面では食品衛生
及び食味の点から、これら化工澱粉の利用は好ましくな
いので、当業界でもこれを改良する手段として湿熱処理
により澱粉を変性させる工業的条件を見いだした特許出
願がされている(平成2年特許願第253029号)。
この方法は、原理的には平衡水分状態の澱粉を湿度10
0%の雰囲気下で100℃以上の高温度に加熱する方法
であり、減圧・加圧方式の採用により工業的に量産が容
易で、品質的に優れた変性澱粉の製造を可能にしたもの
である。この方法では、加熱温度によって澱粉の変性度
合いが異なるため、その調節が重要であり、均一な製品
を得るためには微細な工程管理が要求される。
However, in terms of food processing, the use of these modified starches is not preferable from the viewpoints of food hygiene and taste. Therefore, the industry has found industrial conditions for modifying starch by heat treatment as a means for improving it. A patent application has been filed (Patent application No. 253029, 1990).
In this method, in principle, starch in equilibrium moisture state is treated with a humidity of 10
This is a method of heating to a high temperature of 100 ° C. or higher in a 0% atmosphere. By adopting a reduced pressure / pressurization method, it is possible to industrially mass-produce, and it is possible to produce modified starch of excellent quality. is there. In this method, the degree of modification of starch differs depending on the heating temperature, and therefore its adjustment is important, and fine process control is required to obtain a uniform product.

【0005】[0005]

【発明が解決しようとする課題】変性澱粉の製造法にお
いて望まれることは、まず膨潤性、糊化特性、粘度、耐
熱安定性、溶解性等の澱粉の特性が連続的に変化させう
ること、また粒形の変化は少ないほうが好ましく、しか
もこれら変性の幅ができるだけ広く、かつ容易にその程
度を制御できること、そして可能なかぎり均一に変性で
きることである。さらに処理澱粉の収集と乾燥粉末化が
容易であることも望まれる。
What is desired in the method for producing a modified starch is that the properties of the starch such as swelling property, gelatinization property, viscosity, heat stability and solubility can be continuously changed. Further, it is preferable that the change in grain shape is small, and the range of these modifications is as wide as possible, the degree of which can be easily controlled, and the modification can be made as uniform as possible. Furthermore, it is also desired that the treated starch be easily collected and dried into powder.

【0006】本発明では水とエタノールのようなアルコ
ール溶剤との混合溶液中に澱粉を分散・懸濁してこれを
加熱処理することで、澱粉が上記したような諸性質の変
化、特に膨潤性が著しく変化を受けることを見いだし、
この時の水分割合と加熱温度との組合せにより容易に澱
粉の変性度合いを制御できることを見いだした。また、
これらの処理では澱粉粒は外観的にほとんど変化が認め
られず、処理後の分離・乾燥・粉末化が容易である。本
発明の目的は、条件の選択によって、特に常温(25
℃)での膨潤性が著しく大になり、しかも温度を上げて
もそれほど膨潤度に変化がない変性澱粉を調整すること
にある。
In the present invention, starch is dispersed / suspended in a mixed solution of water and an alcohol solvent such as ethanol and heat-treated to change the above-mentioned various properties of starch, particularly swelling property. Found to undergo significant changes,
It has been found that the degree of modification of starch can be easily controlled by combining the water content and the heating temperature at this time. Also,
In these treatments, the starch granules show almost no change in appearance, and separation, drying and pulverization after the treatment are easy. The purpose of the present invention is to set the temperature at room temperature (25
The purpose is to prepare a modified starch whose swelling property at (.degree. C.) becomes extremely large and whose swelling degree does not change so much even when the temperature is raised.

【0007】[0007]

【課題を解決するための手段】前記目的を達成するため
に本発明の変性澱粉は、水分割合が25〜60容量%の
アルコール溶液中に澱粉を分散・懸濁し、これを100
〜130℃に加熱することにより製造される。
In order to achieve the above object, the modified starch of the present invention is prepared by dispersing and suspending starch in an alcohol solution having a water content of 25 to 60% by volume to prepare 100 parts thereof.
It is produced by heating to ℃ to 130 ℃ .

【0008】本発明において用いる澱粉は各種の澱粉及
び小麦粉のような穀粉末が使用できるが、実用的には、
最も大量生産され、入手が容易で、かつ価格が安価なコ
ーンスターチを用いるのが適している。本発明において
は、主として澱粉膨潤度と膨潤時の溶解度を、温度を変
えて測定することにより澱粉の変性の程度を判定した。
澱粉膨潤度及び溶解度は貝沼の方法に準じて行った。
As the starch used in the present invention, various starches and cereal powders such as wheat flour can be used, but practically,
It is suitable to use cornstarch, which is the most mass produced, readily available and inexpensive. In the present invention, the degree of starch denaturation was determined by measuring the degree of starch swelling and the solubility during swelling at different temperatures.
The starch swelling degree and the solubility were performed according to the method of Kainuma.

【0009】即ち、無水物として0.25〜0.50g
の試料を遠心分離管に精秤し、それに10mlの水を加
えて25〜100℃の各温度で1時間加熱した後、直ち
に4500rpmで30分間、遠心分離し、上澄液を除
いて沈澱物の重量を測定し、その時の上澄液中の全糖量
をフエノール硫酸法で測定して溶解量を算出し、さらに
これらの値から澱粉の膨潤度及び溶解度を算出した。生
澱粉やほとんど変性されていない澱粉は、高温になると
大きく膨潤して、使用した水が全部澱粉粒に吸収されて
上澄液がなくなり、溶解度の測定が不可能となるので試
料量を0.25gとした。
That is, 0.25 to 0.50 g as an anhydride
The sample of 1 was precisely weighed in a centrifuge tube, 10 ml of water was added thereto, and the mixture was heated at each temperature of 25 to 100 ° C. for 1 hour, then immediately centrifuged at 4500 rpm for 30 minutes, and the supernatant was removed to remove the precipitate. Was measured, the total amount of sugar in the supernatant at that time was measured by the phenol-sulfuric acid method to calculate the amount of dissolution, and the swelling degree and solubility of starch were calculated from these values. Raw starch and almost unmodified starch swell significantly at high temperatures, and the water used is completely absorbed by the starch granules, and the supernatant liquid disappears, making it impossible to measure the solubility. It was set to 25 g.

【0010】この測定条件によると、変性していない未
処理の生澱粉は、膨潤度は25℃では1〜2%である
が、70℃を越えると昇温と共に急速に膨潤し、100
℃では約25%の膨潤度となり、25℃の値の10倍以
上になる。また、溶解度は25℃ではほとんど溶けず1
%以下であるが、同じく70℃から上昇し100℃では
溶解度は20%以上とかなり溶解するようになる。この
ことを基準にして澱粉の変性の程度を判定した。
According to this measurement condition, unmodified raw starch which has not been modified has a swelling degree of 1 to 2% at 25 ° C., but when it exceeds 70 ° C., it rapidly swells as the temperature rises to 100%.
The degree of swelling at 25 ° C is about 25%, which is more than 10 times the value at 25 ° C. The solubility is almost insoluble at 25 ° C.
%, But it also rises from 70 ° C., and at 100 ° C., the solubility is 20% or more, which means that the solubility is considerably high. Based on this, the degree of starch modification was determined.

【0011】また、澱粉粒の被染色性も比較した。即
ち、微量の試料を遠心分離管にとり、これへ1%サフラ
ニンT(塩基性赤色染料)溶液を約0.5ml加えて混
合し、約5分間放置した。それを遠心分離し上澄を捨て
て沈澱物を3回水洗して余分の染料を除いた後、赤く染
まった試料澱粉をデッキグラス上にとり、これに一滴の
1%ダイレクトスカイブルー5B(直接青色染料)を加
えて混和して顕微鏡下で観察し、青色に染まった澱粉粒
の割合を読み取った。同時に澱粉粒の大きさ及び形状の
変化を観察した。また、示差走査熱量計、粘度計の測定
も適宜行った。
The dyeability of starch granules was also compared. That is, a small amount of a sample was placed in a centrifuge tube, and about 0.5 ml of a 1% safranine T (basic red dye) solution was added to and mixed with the centrifuge tube, and the mixture was allowed to stand for about 5 minutes. After centrifuging it and discarding the supernatant, the precipitate was washed 3 times with water to remove excess dye, and then sample starch dyed in red was placed on a deck glass and a drop of 1% Direct Sky Blue 5B (direct blue color) (Dye) was added and mixed, and the mixture was observed under a microscope to read the ratio of starch granules dyed in blue. At the same time, changes in the size and shape of the starch granules were observed. Moreover, the measurement with a differential scanning calorimeter and a viscometer was also performed appropriately.

【0012】本発明で最も重要な点は澱粉の変性に適し
た水とアルコール類との混合割合と加熱温度である。本
発明で用いるアルコールとしては、食用に供する変性澱
粉を製造する観点から、安全性、味覚の条件を満足した
エタノールが最も好ましい。但し、プロピルアルコー
ル、イソプロピルアルコール等も用いることができる。
これらアルコール類と水との混合割合が本発明を構成す
る重要な因子である。エタノールの場合、水との混合割
合は、水が25容量%以下ではほとんど変性効果がな
く、また60容量%以上では澱粉が過剰に膨潤して粒形
が崩れて好ましくない。加熱温度は水分の割合によって
変性度合いへの影響が異なる。水分割合が50容量%以
上では80℃でも軽度に変性するが、水分割合が30容
量%以下では100℃以上に加熱しないと実質的な変性
は認められない。好ましくは、水分割合が34〜50容
量%で、加熱温度110〜130℃で約10〜20分加
熱して実施するのが良い。
In the present invention, the most important points are the mixing ratio of water and alcohols and the heating temperature suitable for modifying starch. The alcohol used in the present invention is most preferably ethanol that satisfies the safety and taste conditions from the viewpoint of producing a modified starch to be used for food. However, propyl alcohol, isopropyl alcohol and the like can also be used.
The mixing ratio of these alcohols and water is an important factor constituting the present invention. In the case of ethanol, if the mixing ratio with water is 25% by volume or less, there is almost no denaturing effect, and if it is 60% by volume or more, the starch swells excessively and the particle shape is broken, which is not preferable. The heating temperature has different effects on the degree of denaturation depending on the proportion of water. When the water content is 50% by volume or more, it is mildly modified even at 80 ° C, but when the water content is 30% by volume or less, substantial modification is not observed unless it is heated to 100 ° C or more. Preferably, it is carried out by heating at a heating temperature of 110 to 130 ° C. for about 10 to 20 minutes with a water content of 34 to 50% by volume.

【0013】本発明において使用する澱粉の反応容器
は、間接加熱で内容を加熱することが可能であって、澱
粉の沈澱を防止することができる程度の攪拌装置を付設
した密閉型の加圧加熱が可能なものである。この反応容
器では、水−アルコール溶液に澱粉を分散させて加熱反
応させ、一定時間後に冷却して処理澱粉を濾過して集
め、これを適当な乾燥機で乾燥粉末とすれば変性澱粉が
製造される。少量の製造の場合は適当な容器に、25〜
60容量%の水を含んだエタノール溶液を入れて、この
中に澱粉を分散し、密栓し、この容器を沸騰水中で振り
動かしながら、容器内がエタノールの沸点より少し低い
約70〜75℃になるまで加熱し、直ちに十分予熱した
オートクレーブに入れて加圧加熱すれば良い。その後、
澱粉を濾過または遠心分離で集めて、エタノール、アセ
トンまたはエーテルで洗浄するなどの方法で乾燥させれ
ば良い。
The starch reaction vessel used in the present invention is capable of heating the contents by indirect heating, and is a closed type pressure heating system equipped with a stirrer capable of preventing the precipitation of starch. Is possible. In this reaction vessel, starch is dispersed in a water-alcohol solution and reacted by heating, and after a certain period of time, cooled and treated starch is collected by filtration, and dried by an appropriate dryer to produce modified starch. It In the case of small quantity production, put it in a suitable container.
An ethanol solution containing 60% by volume of water was added, the starch was dispersed therein, and the container was tightly stoppered. While shaking the container in boiling water, the inside of the container was slightly lower than the boiling point of ethanol to about 70 to 75 ° C. It is sufficient to heat until it is heated, and immediately put it in a fully preheated autoclave and heat it under pressure. afterwards,
The starch may be collected by filtration or centrifugation and dried by a method such as washing with ethanol, acetone or ether.

【0014】加熱温度を130℃と高くすると水分割合
30%でも25℃の膨潤度が6となり、100℃での膨
潤度は約2,3倍となる。加熱温度を120℃、加熱時
間を20分としたときのアルコール溶液の水の割合が、
20容量%以下では実質的に膨潤度が生澱粉とほとんど
変化がなく、常温の膨潤度に対して100℃のそれは約
10〜13倍になる。しかし、示差走査熱量計の測定結
果では、糊化時の吸熱量が生澱粉より約10〜30%低
下する。また、粘度的にも最高粘度到達温度が約10℃
低くなり、明らかに変化を受けていることが認められ
る。澱粉の膨潤度の変化は水分割合が25容量%を越え
る点から変化し、34%以上では常温での膨潤度が大き
くなるが、逆に高温度での膨潤度は常温でのそれの1.
2から数倍程度にしかならなく、温度による膨潤度の差
が少なくなる。しかもこの傾向はアルコール溶液中の水
分割合が高くなるほど大きくなり、34〜60容量%の
水分割合では25℃における膨潤度は約4〜10の値に
なる。このことは澱粉1gが3〜9gの水分を吸水して
膨潤したことを意味し、この性質は錠剤製造時の崩壊剤
として充分利用できるものである。その一方で、100
℃に加熱したときの膨潤度がわずかに25℃の時の1.
5〜2.3倍にしかならないことも見いだした。
When the heating temperature is increased to 130 ° C., the swelling degree at 25 ° C. becomes 6 even when the water content is 30%, and the swelling degree at 100 ° C. becomes about 2-3 times. When the heating temperature is 120 ° C. and the heating time is 20 minutes, the proportion of water in the alcohol solution is
Below 20% by volume, the degree of swelling is virtually unchanged from that of raw starch, and that at 100 ° C. is about 10 to 13 times the degree of swelling at room temperature. However, the measurement result of the differential scanning calorimeter shows that the endothermic amount at the time of gelatinization is about 10 to 30% lower than that of raw starch. Also, regarding the viscosity, the maximum viscosity reaching temperature is about 10 ° C.
It becomes lower and is clearly under the change. The change in the degree of swelling of starch changes from the point where the water content exceeds 25% by volume, and the degree of swelling at room temperature increases when it exceeds 34%, but conversely the degree of swelling at high temperature is 1.
It is only about 2 to several times, and the difference in the degree of swelling with temperature is reduced. Moreover, this tendency becomes larger as the water content in the alcohol solution becomes higher, and the swelling degree at 25 ° C. becomes about 4 to 10 at a water content of 34 to 60% by volume. This means that 1 g of starch absorbs 3 to 9 g of water and swells, and this property can be sufficiently utilized as a disintegrant during tablet production. On the other hand, 100
1. When the degree of swelling when heated to ℃ is only 25 ℃.
I also found that it was only 5 to 2.3 times.

【0015】澱粉の溶解度の点では、常温(25℃)で
は未処理のものは、0.1%以下と極めて少なくほとん
ど溶けないが、70℃から溶解度は急激に上昇する(表
2参照)。生澱粉及びアルコール溶液中の水分割合が2
0容量%以下での処理澱粉は100℃では溶解度は約2
5%前後になるが、水分割合を25容量%以上で処理す
ると高温度での溶解度は逆に小さくなる傾向を示した。
高温度で溶出した澱粉の沃素定色反応による青価は高
く、沈澱部分の澱粉の約2.8倍、元の澱粉の2倍弱で
あった。
In terms of solubility of starch, untreated ones at room temperature (25 ° C.) are less than 0.1% and hardly dissolve, but the solubility rapidly increases from 70 ° C. (see Table 2). Water content in raw starch and alcohol solution is 2
Starch treated with 0% by volume or less has a solubility of about 2 at 100 ° C.
Although it was around 5%, the solubility at high temperature tended to decrease on the contrary when treated with a water content of 25% by volume or more.
The blue value of the starch eluted at a high temperature due to the iodine color reaction was high, which was about 2.8 times that of the precipitated starch and slightly less than twice that of the original starch.

【0016】また、アルコール溶液中の水分割合が30
容量%を越えると120℃加熱処理でも40℃でのα−
アミラーゼによる澱粉消化の初速度が、急激に水分割合
に対応して大になる傾向を示した。水分割合が40〜6
0容量%になると澱粉粒がやや膨潤して大きくなるが、
まだ原形を保っており、ほとんどの澱粉が染色されるよ
うになる。これらのことから澱粉粒に隙間が生じたもの
と推察される。水分割合が70容量%になると膨潤し過
ぎて粒の崩壊が認められ、部分糊化澱粉のようになる。
このようになると処理澱粉の乾燥がやや困難になる。処
理澱粉の乾燥粉末化の点では、水分割合50容量%以下
の方が操作が容易である。
The water content in the alcohol solution is 30.
If the volume% is exceeded, α-at 40 ° C even at 120 ° C heat treatment
The initial rate of starch digestion by amylase tended to rapidly increase in proportion to the water content. Moisture content is 40-6
At 0% by volume, the starch granules swell and grow larger,
It still retains its original shape and most starches become dyed. From these, it is inferred that the starch granules had gaps. When the water content is 70% by volume, it swells too much and the disintegration of the grains is recognized, and it becomes like a partially gelatinized starch.
In this case, drying of the treated starch becomes somewhat difficult. From the point of dry powdering of the treated starch, the operation is easier when the water content is 50% by volume or less.

【0017】先に説明したごとく澱粉の変性度合いは、
処理温度が一定であれば、アルコール溶液の水分割合に
よって連続的に変化する。また、水分割合を一定にし、
処理温度を変化させることでも、連続的に変性度合いが
変化する。膨潤性について明らかに変性が認められたの
は、エタノールと水の容量比が75:25くらいから水
分比が多くなったときであった。高温に加熱したときの
膨潤度が低い点と、常温での高吸水・高膨潤性、後処理
の容易さの両面性を考えると、加熱温度110〜120
℃、加熱時間20分で水分割合が30〜50容量%であ
ることが好ましい。
As described above, the degree of modification of starch is
If the treatment temperature is constant, it continuously changes depending on the water content of the alcohol solution. Also, keep the water content constant,
The degree of denaturation also changes continuously by changing the treatment temperature. The apparent denaturation of the swelling property was observed when the volume ratio of ethanol and water was about 75:25 and the water content increased. Considering the low degree of swelling when heated to a high temperature, the high water absorption and high swelling at room temperature, and the ease of post-treatment, the heating temperature is 110 to 120.
It is preferable that the moisture content is 30 to 50% by volume at 20 ° C. for 20 minutes.

【0018】本発明において澱粉懸濁液を調整するとき
の澱粉に対するアルコール溶液の使用割合は、3〜5倍
容量が好ましい。但し、アルコール溶液中の水分割合が
少ない時(25〜35容量%)には澱粉の2倍容量でも
可能である。アルコールを澱粉の5倍容量使用したとし
て、水分割合が40容量%のとき、澱粉:水:エタノー
ルの比は1:2:3となる。
In the present invention, when the starch suspension is prepared, the ratio of the alcohol solution to the starch used is preferably 3 to 5 times the volume. However, when the water content in the alcohol solution is low (25 to 35% by volume), it is possible to use double the volume of starch. Assuming that the alcohol is used at 5 times the volume of starch and the water content is 40% by volume, the ratio of starch: water: ethanol is 1: 2: 3.

【0019】[0019]

【実施例】本発明を以下の実施例により詳細に説明する
が、本発明はこれらに限定されるものではない。 実施例 1 まず、市販コーンスターチを水−エタノール混合液中に
分散し、オートクレーブ中で120℃で20分間加熱処
理した。次に、共栓付き三角フラスコ(300ml)に
市販コーンスターチ20gを入れ、これへ表1に記載の
容積比のエタノールと水の混合溶液100mlを各々加
えて振とう攪拌して分散液とした。これを沸騰水バス中
で揺り動かしながら加熱して、内容物が約70℃に達し
た時、予熱をしておいたオートクレーブ中に入れて密閉
し、120℃で20分間加圧加熱した。そして、直ちに
冷却して遠心分離し、沈澱部を無水エタノールで洗浄
し、さらにエーテルで洗浄した。これを40℃で真空乾
燥して乾燥澱粉とした。この水−エタノール2成分系で
の水分割合の影響による処理澱粉の変性度を表1に示し
た。
The present invention will be described in more detail with reference to the following examples, but the present invention is not limited thereto. Example 1 First, commercially available corn starch was dispersed in a water-ethanol mixed solution, and heat-treated at 120 ° C. for 20 minutes in an autoclave. Next, 20 g of commercially available cornstarch was placed in an Erlenmeyer flask with a ground stopper (300 ml), and 100 ml of a mixed solution of ethanol and water having a volume ratio shown in Table 1 was added thereto, and the mixture was shaken and stirred to obtain a dispersion liquid. This was heated while shaking in a boiling water bath, and when the contents reached about 70 ° C, the contents were placed in a preheated autoclave, sealed, and heated under pressure at 120 ° C for 20 minutes. Then, it was immediately cooled and centrifuged, and the precipitate was washed with absolute ethanol and further washed with ether. This was vacuum dried at 40 ° C. to obtain dry starch. Table 1 shows the modification degree of the treated starch under the influence of the water content in the water-ethanol binary system.

【0020】[0020]

【表1】 [Table 1]

【0021】表1から明らかなように、エタノールで処
理した水分割合0〜20容量%の澱粉は、未処理の生澱
粉とほとんど変わらなかった。また、水分割合70容量
%では明らかに澱粉粒が崩壊し、低温度でもよく膨潤
し、部分糊化澱粉とよく似た状態となり、100℃の溶
解度は生澱粉とほとんど変わらなかった。さらに、水分
割合30〜60容量%でも明らかに、低温度での膨潤度
が大きく、特に40〜60容量%では25℃の膨潤度が
約7〜10倍となり、逆に高温になってもさほど膨潤度
は変化しなかった。このことは本発明の変性澱粉製造法
の特徴を示している。
As is clear from Table 1, the starch treated with ethanol with a water content of 0 to 20% by volume was almost the same as the untreated raw starch. Also, when the water content was 70% by volume, the starch granules clearly disintegrated, swelled well even at low temperature, and became in a state similar to that of partially gelatinized starch, and the solubility at 100 ° C. was almost the same as that of raw starch. Further, even when the water content is 30 to 60% by volume, the degree of swelling at a low temperature is obviously large, and particularly at 40 to 60% by volume, the degree of swelling at 25 ° C. is about 7 to 10 times, and conversely, it is not so high even at high temperature. The degree of swelling did not change. This shows the feature of the modified starch production method of the present invention.

【0022】上述したエタノール:水の容積比が6:4
における120℃、20分処理の各温度での澱粉の変性
度(膨潤度及び溶解度)を表2に示した。
The above-mentioned ethanol: water volume ratio is 6: 4.
Table 2 shows the denaturation degree (swelling degree and solubility) of starch at 120 ° C. for 20 minutes at each temperature.

【0023】 [0023]

【0024】実施例 2 共栓付きプラスチック壜(2000ml)に、表3に記
載の容積比のエタノールと水の混合溶液を各々1000
mlを入れて、約90℃のバス中に付けて内容物の温度
を約70℃とした。そして直ちに300gの市販コーン
スターチを分散し共栓をして、同じバス中でしばらく振
り動かしながら加熱し、予め蒸気を発生させて室温を上
昇させておいてからオートクレーブに入れて密閉し、2
0分間、120℃で加圧加熱した。そして直ちに冷却し
濾過した後、得られた湿澱粉ケーキをエタノール液で洗
浄した。その後、圧搾して脱水してから薄く広げて45
℃で通風乾燥して乾物澱粉を得た。これらの水−エタノ
ール2成分系(水分割合30〜36容量%)の処理澱粉
の変性度を表3に示す。
Example 2 A plastic bottle with a stopper (2000 ml) was mixed with a mixed solution of ethanol and water in a volume ratio shown in Table 3 at 1,000 times each.
The temperature of the contents was adjusted to about 70 ° C. by putting ml in a bath at about 90 ° C. Immediately after, 300 g of commercially available cornstarch was dispersed, stoppered and heated while shaking in the same bath for a while, steam was generated in advance to raise the room temperature, and then placed in an autoclave and sealed.
It was heated under pressure at 120 ° C. for 0 minutes. Then, immediately after cooling and filtering, the obtained wet starch cake was washed with an ethanol solution. Then, squeeze and dehydrate, then spread thinly and 45
Dried starch was obtained by air-drying at ℃. Table 3 shows the modification degree of these treated starches of the water-ethanol binary system (water content 30 to 36% by volume).

【0025】 [0025]

【0026】表3から明らかなように、100℃におけ
る膨潤度は水分割合が30〜36容量%では大差がない
が、25℃における膨潤度では34%から容積比が増え
るにつれて大になる傾向を示した。実施例1と合わせて
この実施例2で考えられることは、変性の目的に応じて
水分割合を変えて、所望の澱粉を実施することが可能な
ことである。
As is clear from Table 3, the degree of swelling at 100 ° C. does not differ greatly when the water content is 30 to 36% by volume, but the degree of swelling at 25 ° C. tends to increase from 34% as the volume ratio increases. Indicated. What is considered in this Example 2 together with Example 1 is that it is possible to carry out the desired starch by changing the water content according to the purpose of modification.

【0027】[0027]

【発明の効果】本発明の変性澱粉は、特定の水分割合を
有するアルコール溶液中に分散・懸濁し、特定の温度ま
で加熱することにより製造されているので、水分割合及
び加熱温度の選択により、所望の変性澱粉が容易に得ら
れる。特に、常温(25℃)での膨潤度が大であり、し
かも温度を上昇させてもそれほど膨潤度に変化がない変
性澱粉を簡単に調整できる。
The modified starch of the present invention is produced by dispersing and suspending it in an alcohol solution having a specific water content and heating it to a specific temperature. The desired modified starch is easily obtained. In particular, it is possible to easily prepare a modified starch that has a large degree of swelling at room temperature (25 ° C.) and that does not change so much even when the temperature is increased.

Claims (3)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】 水分割合が25〜60容量%のアルコー
ル溶液中に澱粉を分散・懸濁し、これを100℃〜13
0℃に加熱することにより高分子的物理的性質を改変し
たことを特徴とする変性澱粉の製造法。
1. Starch is dispersed / suspended in an alcohol solution having a water content of 25 to 60% by volume, and this is placed at 100 ° C. to 13 ° C.
A method for producing a modified starch, characterized in that a polymer physical property is modified by heating at 0 ° C.
【請求項2】 前記アルコールがエタノールであること
を特徴とする請求項1記載の変性澱粉の製造法。
2. The method for producing a modified starch according to claim 1, wherein the alcohol is ethanol.
【請求項3】 水分割合が34〜50容量%のアルコー
ル溶液中で、加熱温度110〜130℃で処理すること
を特徴とする請求項1又は2記載の変性澱粉の製造法。
3. The method for producing modified starch according to claim 1, wherein the treatment is carried out in an alcohol solution having a water content of 34 to 50% by volume at a heating temperature of 110 to 130 ° C.
JP24071793A 1993-08-31 1993-08-31 Method for producing modified starch Expired - Lifetime JP3365656B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
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Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
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Publications (2)

Publication Number Publication Date
JPH0770206A JPH0770206A (en) 1995-03-14
JP3365656B2 true JP3365656B2 (en) 2003-01-14

Family

ID=17063663

Family Applications (1)

Application Number Title Priority Date Filing Date
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Country Status (1)

Country Link
JP (1) JP3365656B2 (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2007267623A (en) * 2006-03-30 2007-10-18 Takara Shuzo Co Ltd Burn-preventive material for food
JP2007267624A (en) * 2006-03-30 2007-10-18 Takara Shuzo Co Ltd Seasoning modifying material for food
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Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US7189288B2 (en) * 2004-10-08 2007-03-13 Tate & Lyle Ingredients Americas, Inc. Enzyme-resistant starch and method for its production

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2007267623A (en) * 2006-03-30 2007-10-18 Takara Shuzo Co Ltd Burn-preventive material for food
JP2007267624A (en) * 2006-03-30 2007-10-18 Takara Shuzo Co Ltd Seasoning modifying material for food
JP4641963B2 (en) * 2006-03-30 2011-03-02 宝酒造株式会社 Food seasoning improver
JP4641962B2 (en) * 2006-03-30 2011-03-02 宝酒造株式会社 Non-sticking material for food
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

Also Published As

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