JPH1036404A - Manufacture of polysaccharide containing uronic acid - Google Patents

Manufacture of polysaccharide containing uronic acid

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Publication number
JPH1036404A
JPH1036404A JP20886696A JP20886696A JPH1036404A JP H1036404 A JPH1036404 A JP H1036404A JP 20886696 A JP20886696 A JP 20886696A JP 20886696 A JP20886696 A JP 20886696A JP H1036404 A JPH1036404 A JP H1036404A
Authority
JP
Japan
Prior art keywords
polysaccharide
uronic acid
acid
producing
aqueous solution
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.)
Pending
Application number
JP20886696A
Other languages
Japanese (ja)
Inventor
Kenji Noguchi
健治 野口
Shin Shikanuma
伸 鹿沼
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Nisshin Oil Mills Ltd
Original Assignee
Nisshin Oil Mills Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Nisshin Oil Mills Ltd filed Critical Nisshin Oil Mills Ltd
Priority to JP20886696A priority Critical patent/JPH1036404A/en
Publication of JPH1036404A publication Critical patent/JPH1036404A/en
Pending legal-status Critical Current

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  • Polysaccharides And Polysaccharide Derivatives (AREA)

Abstract

PROBLEM TO BE SOLVED: To provide a polysaccharide rich in uronic acid from soybean hull, effectively. SOLUTION: A polysaccharide contg. not less than 20% uronic acid is obtd. by coexisting a soybean hull with an aq. soln. contg. e.g. hydrochloric acid and citric acid, pref. having a pH of 3-6, and after heat treating at 70-130 deg.C, pref. under a pressure of not more than 10kg/cm<2> by drying the soln. after removing insol. matters or by precipitating with the addn. of a polar org. solvent to the soln.

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明の属する技術分野】本発明は大豆種皮に含まれる
ウロン酸含有多糖類の効率的な製造方法に関する。
TECHNICAL FIELD The present invention relates to a method for efficiently producing a uronic acid-containing polysaccharide contained in soybean seed coat.

【0002】[0002]

【従来の技術】大豆種皮中に含まれる多糖類に関する研
究は古くから行われている。例えば、J.Chem.Soc.
(C)、第1945〜1949頁、1966年では、種
々の化学薬品の水溶液を用いてペクチン酸、キシラン、
マンナンタイプの多糖類の抽出に成功している。一部の
多糖類についてはその化学構造まで解析されている。ま
た、日本食品工業学会誌、第12巻、第9号、第380
〜386頁、1965年では、大豆種皮を熱水抽出した
りアルカリ抽出する等の一般的な抽出、分離方法によっ
て、いくつかの抽出区分に分け、各区分に含まれる単糖
類を定性評価したり推定している。これらの文献による
と、大豆種皮から抽出される多糖類として酸性糖である
ウロン酸を含む多糖類が得られることも記載されてい
る。
2. Description of the Related Art Studies on polysaccharides contained in soybean seed coat have been conducted for a long time. For example, J. Chem. Soc.
(C), 1945-1949, 1966, using aqueous solutions of various chemicals, pectic acid, xylan,
Mannan-type polysaccharide has been successfully extracted. The chemical structure of some polysaccharides has been analyzed. In addition, Journal of the Japan Food Industry Association, Vol. 12, No. 9, No. 380
386 pages, 1965, the soybean husk was divided into several extraction categories by common extraction and separation methods such as hot water extraction or alkali extraction, and the saccharides contained in each category were qualitatively evaluated. Estimated. According to these documents, it is described that a polysaccharide containing uronic acid, which is an acidic saccharide, can be obtained as a polysaccharide extracted from soybean seed coat.

【0003】ウロン酸は、酸性ムコ多糖類を構成する繰
り返し単位として存在し、例えば発酵多糖類の1種であ
るキサンタンガムではその耐塩性の機能の発現に寄与し
ており、またペクチンにおいてはそのゲル化作用のため
に必須の成分となっている。このようにウロン酸は多糖
類において種々の重要な機能の発現に役立っている。し
たがって大豆種皮から抽出される多糖類のうちウロン酸
に富む多糖類が効率的に得られれば有意義であると考え
られる。
[0003] Uronic acid is present as a repeating unit constituting an acidic mucopolysaccharide. For example, xanthan gum, which is a kind of fermented polysaccharide, contributes to the development of its salt-tolerant function, and pectin has its gel-resistant property. It is an essential component for chemical action. As described above, uronic acid contributes to the expression of various important functions in polysaccharides. Therefore, it would be significant if uronic acid-rich polysaccharides among polysaccharides extracted from soybean hulls could be efficiently obtained.

【0004】[0004]

【発明が解決しようとする課題】しかしながら、前記文
献では、種々の多糖類が抽出、分離されているが、ウロ
ン酸に富む多糖類を抽出しようという技術的思想はな
く、またかかる多糖類の機能についても何ら記述されて
いない。さらに、多糖類の抽出処理時には種々の化学薬
品を用い、多段階の抽出操作を行っていることから、こ
れらの多糖類抽出方法はおよそ工業的レベルで採用でき
る方法とはいいがたい。
However, in the above literature, various polysaccharides are extracted and separated, but there is no technical idea of extracting a polysaccharide rich in uronic acid, and the function of such polysaccharides is not considered. Is not described at all. Furthermore, at the time of the polysaccharide extraction treatment, various chemicals are used and multi-stage extraction operations are performed. Therefore, these polysaccharide extraction methods cannot be said to be methods that can be employed on an industrial level.

【0005】したがって本発明では、大豆種皮を原料と
し、これからウロン酸含量に富む多糖類を効率的に製造
する方法を開発することを目的とした。
Accordingly, an object of the present invention is to develop a method for efficiently producing a polysaccharide rich in uronic acid from soybean seed coat as a raw material.

【0006】[0006]

【課題を解決するための手段】本発明者らは、上記実情
に鑑み、鋭意研究を行った結果、大豆種皮を水に分散さ
せた混合物を酸性条件下で加熱処理することにより目的
とする多糖類を簡便に抽出できることを見出し、本発明
を完成するに至った。
Means for Solving the Problems In view of the above-mentioned circumstances, the present inventors have made intensive studies and as a result, have found that a mixture obtained by dispersing soybean seed coat in water is subjected to heat treatment under acidic conditions to obtain the desired product. They have found that saccharides can be easily extracted, and have completed the present invention.

【0007】すなわち本発明によれば、大豆種皮を酸性
水溶液の共存下、70〜130℃で加熱処理した後、不
溶分を除去した水溶液を乾燥するか、またはこの水溶液
に極性有機溶剤を加えて沈澱物を生じせしめることを特
徴とする、ウロン酸に富む多糖類の製造法が提供され
る。
That is, according to the present invention, after soybean hulls are heat-treated at 70 to 130 ° C. in the presence of an acidic aqueous solution, the aqueous solution from which insolubles have been removed is dried, or a polar organic solvent is added to the aqueous solution. There is provided a method for producing a uronic acid-rich polysaccharide, which comprises causing a precipitate to form.

【0008】本発明で原料として用いる大豆種皮は、通
常の大豆種子をそのままあるいは湿潤させ、脱皮処理し
て得られるものでよく、食用油製造工程において多量に
産出される大豆種皮を利用するのが至便である。
[0008] The soybean hull used as a raw material in the present invention may be one obtained by moulting ordinary soybean seeds as they are or by moistening them. It is convenient.

【0009】[0009]

【発明の実施の形態】本発明で用いる大豆種皮は、大豆
種子から脱皮したものをそのまま利用できるが、本発明
の趣旨から粉砕物(1〜5mm程度)、微粉砕物(100
〜500μm程度)あるいは超微粉砕物(100μm程
度以下)を用いることが望ましい。
BEST MODE FOR CARRYING OUT THE INVENTION As a soybean seed coat used in the present invention, a soybean peeled from a soybean seed can be used as it is, but for the purpose of the present invention, a pulverized material (about 1 to 5 mm) and a finely pulverized material (100 mm) are used.
To about 500 μm) or an ultra finely pulverized product (about 100 μm or less).

【0010】本発明では、まず、大豆種皮を酸性水溶液
の共存下において加熱処理するが、該水溶液のpHは3〜
6に設定することが好ましい。pHが3より低いと加水分
解反応が進みすぎるため多糖類の低分子量化が促進さ
れ、得られる多糖類において前記機能が低下する傾向が
大きくなる。逆に、pH6を超えると多糖類は得られるが
ウロン酸に富むものではなくなってしまう。なお、アル
カリ性の条件下でも多糖類を抽出、分離することはでき
るが、この場合には大豆種皮に含まれるリグニン等の分
解も同時に進行するため抽出液が黒褐色となり、脱色精
製のために大量の例えば活性炭を必要とするなど好まし
くない。
In the present invention, first, soybean seed coat is heat-treated in the presence of an acidic aqueous solution.
Preferably, it is set to 6. If the pH is lower than 3, the hydrolysis reaction proceeds too much, and the molecular weight of the polysaccharide is promoted, and the function of the obtained polysaccharide tends to be reduced. Conversely, above pH 6, polysaccharides are obtained, but not uronic acid-rich. In addition, polysaccharides can be extracted and separated under alkaline conditions, but in this case, the decomposition of lignin and the like contained in soybean hulls also proceeds at the same time, so that the extract becomes blackish brown, and a large amount is used for decolorization and purification. For example, it is not preferable that activated carbon is required.

【0011】pH調整のために用いる酸性物質としては任
意のものを利用でき、例えば塩酸、リン酸、クエン酸、
酒石酸、リンゴ酸、酢酸等のいずれでもよく、またこれ
らの2種類以上を組み合わせて用いてもよい。しかしな
がら本発明では、特に塩酸のみでpH調整すること、また
は塩酸とクエン酸とを組み合わせてpH調整を行うのがよ
い。後者の場合には、さらに多糖類の収率の向上も認め
られる。
As the acidic substance used for pH adjustment, any substance can be used, for example, hydrochloric acid, phosphoric acid, citric acid,
Any of tartaric acid, malic acid, acetic acid and the like may be used, or two or more of these may be used in combination. However, in the present invention, it is particularly preferable to adjust the pH only with hydrochloric acid, or to adjust the pH using a combination of hydrochloric acid and citric acid. In the latter case, a further improvement in the yield of the polysaccharide is also observed.

【0012】かかる酸性水溶液は大豆種皮に対して4〜
10倍(重量)の割合で用いる。この範囲を外れると作
業性が低下し、あるいは目的物の濃度が小さい前記処理
液しか得られず、いずれも効率的でない。
The acidic aqueous solution is used in an amount of 4 to
Used 10 times (weight). Outside this range, the workability is reduced, or only the treatment liquid having a low concentration of the target substance is obtained, and neither is efficient.

【0013】加熱温度は70〜130℃で行うことが重
要である。70℃未満では得られる多糖類中のウロン酸
含有量がが低く、また多糖類自体の収率も悪くなる。一
方、130℃超過では大豆種皮に含まれる蛋白質と糖類
との反応によると考えられる褐色物質の発生量が増えて
しまい好ましくない。本発明では特に100℃〜120
℃で処理することが、多糖類の収率、ウロン酸の含有量
および色調の点で好ましい。
It is important that the heating is performed at a temperature of 70 to 130 ° C. When the temperature is lower than 70 ° C., the uronic acid content in the obtained polysaccharide is low, and the yield of the polysaccharide itself is poor. On the other hand, if the temperature is higher than 130 ° C., the amount of the brown substance generated due to the reaction between the protein and the saccharide contained in the soybean seed coat increases, which is not preferable. In the present invention, in particular, 100 ° C to 120 ° C.
C. is preferred in terms of polysaccharide yield, uronic acid content and color.

【0014】かかる加熱処理は30分〜5時間、より好
ましくは30分〜2時間、静置あるいは攪拌して行う。
また本発明では、加熱処理を加圧下、より好ましくは1
0kg/cm2 以下の加圧下で行うと多糖類の収率、ウロン
酸の含有量および色調の点でさらに望ましいものが得ら
れ、また加熱処理時間を短縮できる。なお、10kg/cm
2 を超えて加圧してもそれに見合う前記効果の増大は認
められない。
The heat treatment is carried out for 30 minutes to 5 hours, more preferably 30 minutes to 2 hours, with standing or stirring.
In the present invention, the heat treatment is carried out under pressure, more preferably 1 hour.
When performed under a pressure of 0 kg / cm 2 or less, more desirable ones can be obtained in terms of the yield of polysaccharide, the content of uronic acid and the color tone, and the heat treatment time can be shortened. In addition, 10kg / cm
Even if the pressure is increased beyond 2 , no corresponding increase in the effect is observed.

【0015】前記の加熱処理後、大豆種皮および酸性水
溶液の混合物を金網、篩、濾紙、ガラス製フィルター、
セラミックス製フィルター、遠心分離等の適当な手段を
用いて処理し、大豆種皮の残渣を分離、除去する。かく
して得られる清澄、透明な水溶液には目的の多糖類が溶
解している。
After the above-mentioned heat treatment, the mixture of soybean seed coat and the acidic aqueous solution is subjected to a wire mesh, a sieve, filter paper, a glass filter,
Treatment is performed using a ceramic filter, centrifugation or other appropriate means to separate and remove soybean seed coat residues. The target polysaccharide is dissolved in the thus obtained clear and transparent aqueous solution.

【0016】ついで前記水溶液を酸性状態のままで、あ
るいは水酸化ナトリウム、水酸化カリウムや炭酸ナトリ
ウム等のアルカリ性物質を加えて中和した後、必要に応
じて活性炭、活性白土等の脱色剤を用いて脱色精製し、
乾燥するか、あるいはメタノール、エタノール、イソプ
ロパノール、n−プロパノール、ブタノール、アセト
ン、メチルエチルケトン、ジエチルエーテル、メチルエ
チルエーテル等の極性有機溶剤、好ましくはエタノール
等の前記低級アルコールを液体部に対して1〜5倍(容
量)加え、適宜に攪拌してから沈澱物を生じせしめ、こ
の沈澱物を濾別して本発明の目的とするウロン酸に富む
多糖類を得ることができる。前記極性有機溶剤を用いて
沈澱物としこれを回収する方法が、そのまま乾燥して回
収する方法に比べてウロン酸の収率の点で優れる。
Next, the aqueous solution is neutralized by keeping it in an acidic state or by adding an alkaline substance such as sodium hydroxide, potassium hydroxide or sodium carbonate, and then, if necessary, using a decolorizing agent such as activated carbon or activated clay. To decolorize and purify,
Dry or dry a polar organic solvent such as methanol, ethanol, isopropanol, n-propanol, butanol, acetone, methyl ethyl ketone, diethyl ether and methyl ethyl ether, preferably the lower alcohol such as ethanol, with respect to the liquid part by 1 to 5 parts. After adding twice (by volume) and stirring appropriately, a precipitate is formed, and the precipitate is separated by filtration to obtain the uronic acid-rich polysaccharide desired in the present invention. The method of recovering a precipitate by using the polar organic solvent is superior to the method of drying and recovering the precipitate in terms of the yield of uronic acid.

【0017】以上のようにして得られる、大豆種皮由来
の多糖類は、糖組成としてウロン酸を多く含み、より好
ましくは抽出される多糖類を基準(以下特にことわらな
い限り同じ)として20重量%以上、さらに好ましくは
20〜50重量%含み、また多糖類を構成する単糖とし
てヘキソースを主体とし、より好ましくは抽出物を基準
(以下特にことわらない限り同じ)として50重量%以
上含有するものである。
The polysaccharide derived from soybean seed coat obtained as described above contains a large amount of uronic acid as a sugar composition, and more preferably 20% by weight based on the extracted polysaccharide (hereinafter the same unless otherwise specified). % Or more, more preferably 20 to 50% by weight, and hexose as the main sugar constituting the polysaccharide, more preferably 50% by weight or more based on the extract (the same unless otherwise specified). Things.

【0018】[0018]

【実施例】以下に実施例および比較例を用いて本発明を
さらに詳細に説明する。
The present invention will be described in more detail with reference to the following Examples and Comparative Examples.

【0019】実施例1 3リットル三角フラスコに大豆種皮(日清製油(株)
製、商品名:日清ビンフレ、サイズ:5〜10mm)10
0gおよびイオン交換水1リットルを加え分散させた。
ついで、これに1N−塩酸を加えてpH3に調整した後、
圧力釜(ヤマト科学(株)製、型式:SP52、以下同
様)に入れ、121℃、5kg/cm2 の加圧下で1時間加
熱処理した。該処理物を70℃まで冷却し、金網(32
メッシュ)を用いて大豆種皮の残渣等のキョウ雑物を粗
く分離した後、さらにグラスフィルター(東洋濾紙
(株)製、型式:GA−200、以下同様)を用いて不
溶分を濾別し透明な濾液600mlを得た。次にこれに3
倍容量のエタノールを加え、ゆるやかに攪拌し、生じた
白色沈澱物を濾紙で濾別、乾燥して本発明の目的物であ
る大豆種皮由来の多糖類8.5gを得た。
EXAMPLE 1 A soybean seed coat (Nisshin Oil Co., Ltd.) was placed in a 3-liter Erlenmeyer flask.
Product name: Nisshin Binfure, size: 5-10mm) 10
0 g and 1 liter of ion-exchanged water were added and dispersed.
Next, 1N-hydrochloric acid was added thereto to adjust the pH to 3, and then
It was placed in a pressure cooker (manufactured by Yamato Scientific Co., Ltd., model: SP52, the same applies hereinafter) and heat-treated at 121 ° C. under a pressure of 5 kg / cm 2 for 1 hour. The treated material was cooled to 70 ° C., and the wire mesh (32
After coarsely separating kyoto miscellaneous substances such as soybean seed coat residue using a mesh), insoluble components are further filtered off using a glass filter (manufactured by Toyo Roshi Kaisha, Ltd., model: GA-200, the same applies hereinafter), and the mixture is transparent. 600 ml of a fresh filtrate were obtained. Then 3
A double volume of ethanol was added, the mixture was gently stirred, and the resulting white precipitate was separated by filtration with filter paper and dried to obtain 8.5 g of a polysaccharide derived from soybean seed coat, which was the object of the present invention.

【0020】比較例1 実施例1と同様に大豆種皮100gをイオン交換水1リ
ットルに分散させた。この分散液はpH6.4であった。
分散液のpHを調整せずに、70℃、常圧下で1時間加熱
処理した。ついで該処理物を実施例1と同じ方法、条件
で処理し、多糖類2.3gを得た。
Comparative Example 1 In the same manner as in Example 1, 100 g of soybean seed coat was dispersed in 1 liter of ion-exchanged water. This dispersion had a pH of 6.4.
The dispersion was heated for 1 hour at 70 ° C. under normal pressure without adjusting the pH of the dispersion. Then, the treated product was treated in the same manner and under the same conditions as in Example 1 to obtain 2.3 g of polysaccharide.

【0021】比較例2 実施例1と同様に大豆種皮100gをイオン交換水1リ
ットルに分散させた。ついで、これに1N−塩酸を加え
てpH3に調整した後、60℃、常圧下で1時間加熱処理
した。ついで該処理物を実施例1と同じ方法、条件で処
理し、多糖類3.6gを得た。
Comparative Example 2 In the same manner as in Example 1, 100 g of soybean seed coat was dispersed in 1 liter of ion-exchanged water. Then, the mixture was adjusted to pH 3 by adding 1N-hydrochloric acid, and then heat-treated at 60 ° C. under normal pressure for 1 hour. Then, the treated product was treated in the same manner and under the same conditions as in Example 1 to obtain 3.6 g of a polysaccharide.

【0022】実施例1、比較例1および2で得た大豆種
皮由来の多糖類の糖分析を行った。ウロン酸含有量はBl
umenkrantzの方法(Analytical Biochemistry 、第54
巻、第484〜486頁、1973年に記載の方法)に
より、またヘキソース含有量はフェノール硫酸法(例え
ば福井作蔵 著、「還元糖の定量法・第2版」、第50
〜52頁、1990年、(株)学会出版センターに記
載)によりそれぞれ定量分析した(以下同様)。この結
果を表−1に示す。実施例および比較例の対比から、本
発明の方法によれば、ウロン酸に富む多糖類を効果的に
抽出できることが明らかになった。
The polysaccharides derived from soybean hulls obtained in Example 1 and Comparative Examples 1 and 2 were subjected to sugar analysis. Uronic acid content is Bl
umenkrantz method (Analytical Biochemistry, 54th edition)
Pp. 484-486, 1973), and the hexose content was determined by the phenol-sulfuric acid method (for example, Sakuzo Fukui, "Quantitative Method for Reducing Sugar, 2nd Edition", 50th Edition).
, Page 52, 1990, described in Gakkai Shuppan Center Co., Ltd.) (the same applies hereinafter). The results are shown in Table 1. From comparison between the examples and comparative examples, it was revealed that the method of the present invention can effectively extract polysaccharides rich in uronic acid.

【0023】[0023]

【表1】 *1:抽出多糖類の重量基準。 *2:抽出物の重量基準。[Table 1] * 1: Based on the weight of the extracted polysaccharide. * 2: Based on the weight of the extract.

【0024】実施例2 大豆種皮(実施例1と同じ)100gをイオン交換水1
リットルに分散させた。ついで30%酢酸を加えてpH5
に調整した後、圧力釜中で121℃、1kg/cm2 の加圧
下で1時間加熱処理した。該処理物を70℃まで冷却
し、遠心分離機を用いて大豆種皮の残渣等の不溶分を粗
く分離した後、さらにグラスフィルターを用いて不溶分
を濾別し、透明な濾液600mlを得た。次に、これに5
倍容量のエタノールを加え、生じた白色沈澱物を濾紙で
濾別し、風乾して本発明の多糖類6.5gを得た。該多
糖類の糖分析の結果、ウロン酸含量:39.1重量%、
またヘキソース含量:63.8重量%であった。
Example 2 100 g of soybean seed coat (same as in Example 1) was added to deionized water 1
Dispersed in liters. Then, 30% acetic acid was added to adjust the pH to 5.
Then, the mixture was heated in a pressure cooker at 121 ° C. under a pressure of 1 kg / cm 2 for 1 hour. The treated product was cooled to 70 ° C., and the insolubles such as soybean seed coat residue were roughly separated using a centrifugal separator. The insolubles were further filtered off using a glass filter to obtain 600 ml of a transparent filtrate. . Next, this is 5
A double volume of ethanol was added, and the resulting white precipitate was separated by filtration with filter paper and air-dried to obtain 6.5 g of the polysaccharide of the present invention. As a result of sugar analysis of the polysaccharide, uronic acid content: 39.1% by weight,
Hexose content: 63.8% by weight.

【0025】実施例3 大豆種皮(実施例1と同じ)100gをイオン交換水1
リットルに分散させた。これに無水クエン酸7.5gを
添加、溶解させた後、pHを測定したところ3.5であっ
た。この分散液を80℃、常圧下で2時間加熱処理し
た。該処理物を70℃まで冷却し、実施例1と同様の方
法および条件で処理し、本発明の多糖類4.3gを得
た。該多糖類の糖分析の結果、ウロン酸含量:22.9
重量%、またヘキソース含量:75.0重量%であっ
た。
Example 3 100 g of soybean seed coat (same as in Example 1) was added to deionized water 1
Dispersed in liters. After adding and dissolving 7.5 g of citric anhydride thereto, the pH was measured to be 3.5. This dispersion was heated at 80 ° C. under normal pressure for 2 hours. The treated product was cooled to 70 ° C. and treated in the same manner and under the same conditions as in Example 1 to obtain 4.3 g of the polysaccharide of the present invention. As a result of sugar analysis of the polysaccharide, uronic acid content: 22.9
Hexose content: 75.0% by weight.

【0026】実施例4 大豆種皮(実施例1と同じ)100gをイオン交換水1
リットルに分散させた。これに無水クエン酸7.5gを
添加、溶解させた後、さらに1N−塩酸を加えてpH3に
調整した。この分散液を圧力釜中で121℃、1kg/cm
2 の加圧下で1時間加熱処理した。該処理物を70℃ま
で冷却し、実施例1と同様に不溶分を除去して透明な濾
液600mlを得た。この濾液に粉末活性炭を3.3g添
加し1時間撹拌した。濾別後、さらに3倍容量のエタノ
ールを加え、生じた白色沈澱物を濾別し、減圧乾燥して
本発明の多糖類5.8gを得た。該多糖類の糖含量を分
析した結果、ウロン酸含量:44.0重量%、またヘキ
ソース含量:61.4重量%であった。なお本実施例で
得られた多糖類は実施例1〜3のものより白さの点で優
れていた。
Example 4 100 g of soybean seed coat (same as in Example 1) was added to deionized water 1
Dispersed in liters. After adding and dissolving 7.5 g of citric anhydride thereto, the pH was adjusted to 3 by further adding 1N-hydrochloric acid. This dispersion is placed in a pressure cooker at 121 ° C., 1 kg / cm
Heat treatment was performed under pressure of 2 for 1 hour. The treated product was cooled to 70 ° C., and the insolubles were removed in the same manner as in Example 1 to obtain 600 ml of a transparent filtrate. 3.3 g of powdered activated carbon was added to the filtrate and stirred for 1 hour. After filtration, a three-fold volume of ethanol was further added, and the resulting white precipitate was separated by filtration and dried under reduced pressure to obtain 5.8 g of the polysaccharide of the present invention. As a result of analyzing the sugar content of the polysaccharide, the uronic acid content was 44.0% by weight and the hexose content was 61.4% by weight. The polysaccharide obtained in this example was superior to those of Examples 1 to 3 in terms of whiteness.

【0027】実施例5 大豆種皮(実施例1で使用したものの微粉砕物、サイ
ズ:100〜500μm)1kgをイオン交換水5リット
ルに加え分散させた。これに1N−塩酸を加えてpH4に
調整した後、圧力釜中で105℃、3kg/cm2 の加圧下
で1時間加熱処理した。該処理物を70℃に冷却後、遠
心分離機を用いて大豆種皮の残渣等のキョウ雑物を粗く
分離、除去し、得られた上澄液に粉末活性炭を10g添
加し1時間撹拌した。ついでグラスフィルターを用いて
濾別し、透明な濾液を得た。この濾液を10%水酸化ナ
トリウム水溶液で中和し、さらに減圧乾燥して水分を除
き、本発明の多糖類125gを得た。該多糖類の糖含量
を分析した結果、ウロン酸含量(ただし乾燥固形分の重
量基準):33.2重量%、またヘキソース含量(ただ
し乾燥固形分の重量基準):66.0重量%であった。
Example 5 1 kg of soybean seed coat (finely pulverized material used in Example 1, size: 100 to 500 μm) was added to 5 liters of ion-exchanged water and dispersed. After adjusting the pH to 4 by adding 1N-hydrochloric acid, the mixture was heated in a pressure cooker at 105 ° C. under a pressure of 3 kg / cm 2 for 1 hour. After cooling the treated product to 70 ° C., coarse gypsum such as soybean seed coat residue was roughly separated and removed using a centrifugal separator, and 10 g of powdered activated carbon was added to the obtained supernatant and stirred for 1 hour. Then, the mixture was filtered using a glass filter to obtain a transparent filtrate. This filtrate was neutralized with a 10% aqueous sodium hydroxide solution, and further dried under reduced pressure to remove water, thereby obtaining 125 g of the polysaccharide of the present invention. As a result of analyzing the sugar content of the polysaccharide, the uronic acid content (based on the weight of dry solids) was 33.2% by weight, and the hexose content (however, based on the weight of dry solids): 66.0% by weight. Was.

【0028】[0028]

【発明の効果】本発明によれば、大豆種皮を原料として
ウロン酸含量の高い多糖類を簡便な方法により高収率で
製造することができる。大豆種皮は食用油製造時に多量
の副産物として発生し、従来、その利用法や用途が限ら
れていたが、本発明によれば大豆種皮の新たな利用法を
提供できる。
According to the present invention, a polysaccharide having a high uronic acid content can be produced at a high yield by a simple method using soybean seed coat as a raw material. Soybean husks are generated as a large amount of by-products during the production of edible oil, and their use and use have been limited in the past. According to the present invention, a new use of soybean husks can be provided.

Claims (7)

【特許請求の範囲】[Claims] 【請求項1】 大豆種皮を酸性水溶液の共存下、70〜
130℃で加熱処理した後、不溶分を除去した水溶液を
乾燥するか、またはこの水溶液に極性有機溶剤を加えて
沈澱物を生じせしめることを特徴とするウロン酸に富む
多糖類の製造法。
1. A soybean seed coat is prepared by coexisting an acidic aqueous solution with
A process for producing a polysaccharide rich in uronic acid, which comprises heat-treating at 130 ° C. and then drying an aqueous solution from which insolubles have been removed, or adding a polar organic solvent to the aqueous solution to form a precipitate.
【請求項2】 多糖類がウロン酸を20重量%以上含む
ものである請求項1に記載の多糖類の製造法。
2. The method for producing a polysaccharide according to claim 1, wherein the polysaccharide contains uronic acid in an amount of 20% by weight or more.
【請求項3】 多糖類がウロン酸を20〜50重量%含
有し、かつヘキソースを50重量%以上含有するもので
ある請求項1または2に記載の多糖類の製造法。
3. The method for producing a polysaccharide according to claim 1, wherein the polysaccharide contains 20 to 50% by weight of uronic acid and 50% by weight or more of hexose.
【請求項4】 酸性水溶液が塩酸およびクエン酸を含有
してなるものである請求項1に記載の多糖類の製造法。
4. The method for producing a polysaccharide according to claim 1, wherein the acidic aqueous solution contains hydrochloric acid and citric acid.
【請求項5】 酸性水溶液のpHが3〜6である請求項1
または4に記載の多糖類の製造法。
5. An acidic aqueous solution having a pH of 3 to 6.
Or the method for producing a polysaccharide according to 4.
【請求項6】 加熱処理が加圧下で行われるものである
請求項1に記載の多糖類の製造法。
6. The method for producing a polysaccharide according to claim 1, wherein the heat treatment is performed under pressure.
【請求項7】 加熱処理が10kg/cm2 以下の加圧下で
100〜120℃に加熱するものである請求項1または
6に記載の多糖類の製造法。
7. The method for producing a polysaccharide according to claim 1, wherein the heat treatment comprises heating to 100 to 120 ° C. under a pressure of 10 kg / cm 2 or less.
JP20886696A 1996-07-19 1996-07-19 Manufacture of polysaccharide containing uronic acid Pending JPH1036404A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP20886696A JPH1036404A (en) 1996-07-19 1996-07-19 Manufacture of polysaccharide containing uronic acid

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP20886696A JPH1036404A (en) 1996-07-19 1996-07-19 Manufacture of polysaccharide containing uronic acid

Publications (1)

Publication Number Publication Date
JPH1036404A true JPH1036404A (en) 1998-02-10

Family

ID=16563425

Family Applications (1)

Application Number Title Priority Date Filing Date
JP20886696A Pending JPH1036404A (en) 1996-07-19 1996-07-19 Manufacture of polysaccharide containing uronic acid

Country Status (1)

Country Link
JP (1) JPH1036404A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2012162485A (en) * 2011-02-07 2012-08-30 Higashimaru Shoyu Co Ltd Iron absorption promoter

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2012162485A (en) * 2011-02-07 2012-08-30 Higashimaru Shoyu Co Ltd Iron absorption promoter

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