JPH0782287A - Purification of oligosaccharide - Google Patents

Purification of oligosaccharide

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Publication number
JPH0782287A
JPH0782287A JP22745493A JP22745493A JPH0782287A JP H0782287 A JPH0782287 A JP H0782287A JP 22745493 A JP22745493 A JP 22745493A JP 22745493 A JP22745493 A JP 22745493A JP H0782287 A JPH0782287 A JP H0782287A
Authority
JP
Japan
Prior art keywords
oligosaccharides
oligosaccharide
syrup
organic solvent
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.)
Granted
Application number
JP22745493A
Other languages
Japanese (ja)
Other versions
JP3623974B2 (en
Inventor
Yasusuke Suzuki
庸介 鈴木
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.)
Asahi Soft Drinks Co Ltd
Original Assignee
Calpis Food Industry Co 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 Calpis Food Industry Co Ltd filed Critical Calpis Food Industry Co Ltd
Priority to JP22745493A priority Critical patent/JP3623974B2/en
Publication of JPH0782287A publication Critical patent/JPH0782287A/en
Application granted granted Critical
Publication of JP3623974B2 publication Critical patent/JP3623974B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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Abstract

PURPOSE:To easily purify oligosaccharides raised in the composition concentrations of triose or higher oligosaccharides from an oligosaccharides- contg. syrup and/or an aqueous solution of oligosaccharides-contg. powder with out the need of using any special equipment, etc. CONSTITUTION:Firstly, an oligosaccharides-contg. syrup and/or an aqueous solution of oligosaccharides-contg. powder is incorporated with an organic solvent followed by heating into a homogeneous solution. Secondly the lower layer of the two-layer separated liquid obtained by cooling the above solution is fractionatedly recovered, thus purifying the oligosaccharides raised in the content of triose or higher oligosaccharides. This purification method is hopeful of application in place of conventional methods using column chromatography. The oligosaccharide purified, which are hopeful of physiological effect, can be used as e.g. ingredients for various foods and beverages.

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、オリゴ糖類の精製方法
に関し、更に詳細にはオリゴ糖類含有シロップ及び/又
はオリゴ糖類含有粉末の水溶液における単糖類、二糖類
等を工業的に減少、除去し、三糖類以上のオリゴ糖類含
有率を向上させたオリゴ糖類の精製方法に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for purifying oligosaccharides, more specifically, industrially reducing and removing monosaccharides, disaccharides, etc. in an aqueous solution of oligosaccharide-containing syrup and / or oligosaccharide-containing powder. The present invention relates to a method for purifying oligosaccharides having an improved content of trisaccharides or higher oligosaccharides.

【0002】[0002]

【従来の技術】近年、健康志向の高まりと共に、腸内ビ
フィズス菌増殖促進機能を有し、整腸作用、腸内菌叢改
善、腸内腐敗産物生成抑制等の生理的効果を有する各種
オリゴ糖類が開発され、商品化されている。またオリゴ
糖を添加した各種飲食品の市場も拡大されている。特
に、特定用保健食品として厚生省の許可を受けた場合に
は、商品への効能表示が可能であって、商品価値が向上
する等の利点から種々の生理的効果を有するオリゴ糖類
の開発がなされている。このような生理的効果等を有す
るオリゴ糖類は、一般的に三糖類以上のものである。
2. Description of the Related Art In recent years, various oligosaccharides having a physiological effect such as an intestinal regulating effect, an improvement of intestinal flora, an inhibition of intestinal spoilage product, etc., having an intestinal bifidobacteria growth promoting function with the increasing health consciousness. Has been developed and commercialized. The market for various foods and drinks containing oligosaccharides is also expanding. In particular, when it is approved by the Ministry of Health and Welfare as a specified health food, it is possible to label the effect on the product, and oligosaccharides having various physiological effects have been developed because of the advantages such as improvement of the product value. ing. An oligosaccharide having such a physiological effect is generally a trisaccharide or more.

【0003】単糖類からオリゴ糖類までを含む混合糖類
の精製方法として、従来はカラムクロマトグラフィーに
よる方法が一般に採用され工業化されている。しかしカ
ラムクロマトグラフィー精製法は、大規模な設備投資が
必要であり、しかも樹脂の再生又は逆再生、樹脂の補充
及び更新、電気、用水等のランニングコストが嵩むとい
う欠点がある。更に混合糖類を精製する場合に、精製原
料の糖液シロップを適当な濃度まで希釈して処理しなけ
ればならず、工程が煩雑化する。更にカラムクロマトグ
ラフィー処理中には、必然的に水で希釈されるため、カ
ラムクロマトグラフィー精製処理品は、大量の精製処理
液を再度濃縮しなければならず、大型の減圧濃縮機も必
要となる。
As a method for purifying a mixed saccharide containing monosaccharides to oligosaccharides, a column chromatography method has been generally adopted and industrialized. However, the column chromatography purification method has a drawback that large-scale capital investment is required and that running costs of resin regeneration or reverse regeneration, resin replenishment and renewal, electricity, water, etc. increase. Further, in the case of purifying a mixed saccharide, the sugar syrup as a raw material for purification must be diluted to an appropriate concentration for treatment, which complicates the process. Further, during the column chromatography treatment, it is inevitably diluted with water, so the column chromatography purification treatment product must re-concentrate a large amount of the purification treatment liquid, and a large vacuum concentration machine is also required. .

【0004】また目的のオリゴ糖を資化せず、単糖類、
ショ糖、麦芽糖等の二糖類のみを資化する酵母等の微生
物処理による方法も提案されている。しかし、工業的に
はオリゴ糖以外の糖類は回収されず、微生物処理に多大
の設備と処理コストを必要とするため実施されていない
のが実状である。
Further, a monosaccharide, which does not assimilate the desired oligosaccharide,
A method by microbial treatment of yeast or the like that utilizes only disaccharides such as sucrose and maltose has also been proposed. However, saccharides other than oligosaccharides are not industrially recovered, and in reality, they have not been carried out because microbial treatment requires a large amount of equipment and treatment cost.

【0005】これまでに各種混合糖類をアルコール等の
有機溶媒を用いて精製する方法、具体的にはでんぷん糖
化液に有機溶媒を添加混合し、静置することにより、オ
リゴ糖等を主成分とする上層と、高重合度成分を主成分
とする下層との2層に分離し、該下層に沈澱する高重合
度成分を除去する方法(特開昭62−118894号公
報)が提案されている。しかし、このような多糖類にア
ルコール等の有機溶媒を加えて沈澱する高重合度成分を
分離する方法は、2層を溶液層として分離する方法とは
異なる。
Up to now, a method for purifying various mixed sugars using an organic solvent such as alcohol, specifically, by adding an organic solvent to a starch saccharified solution and mixing the mixture, the mixture is allowed to stand and oligosaccharides are the main components. There is proposed a method (Japanese Unexamined Patent Publication (Kokai) No. 62-118894) in which the upper polymerization layer and the lower layer containing a high-polymerization component as the main component are separated into two layers, and the high-polymerization component precipitated in the lower layer is removed. . However, the method of adding an organic solvent such as alcohol to such a polysaccharide to separate the precipitated high polymerization degree component is different from the method of separating two layers into a solution layer.

【0006】[0006]

【発明が解決しようとする課題】本発明の目的は、大規
模の特殊な設備を必要とせず、簡便な方法でオリゴ糖を
含む混合糖類から三糖類以上のオリゴ糖成分の組成濃度
を増加させることができるオリゴ糖類の精製方法を提供
することにある。
SUMMARY OF THE INVENTION An object of the present invention is to increase the composition concentration of oligosaccharide components of trisaccharide or higher from mixed saccharides containing oligosaccharides in a simple manner without requiring large-scale special equipment. It is to provide a method for purifying oligosaccharides that can be used.

【0007】[0007]

【課題を解決するための手段】本発明によれば、オリゴ
糖類含有シロップ及び/又はオリゴ糖類含有粉末の水溶
液から三糖類以上のオリゴ糖類含有率を向上させたオリ
ゴ糖類を精製する方法であって、オリゴ糖類含有シロッ
プ及び/又はオリゴ糖類含有粉末の水溶液に、有機溶媒
を加えて加熱均一溶解し、冷却した後、得られる2層分
離液の下層を分別回収することを特徴とするオリゴ糖類
の精製方法が提供される。
According to the present invention, there is provided a method for purifying an oligosaccharide having an improved oligosaccharide content of trisaccharide or more from an aqueous solution of an oligosaccharide-containing syrup and / or an oligosaccharide-containing powder. , An oligosaccharide-containing syrup and / or an aqueous solution of an oligosaccharide-containing powder is added with an organic solvent to uniformly heat and dissolve, and after cooling, the lower layer of the obtained two-layer separated liquid is separated and collected. A purification method is provided.

【0008】以下本発明を更に詳細に説明する。The present invention will be described in more detail below.

【0009】本発明の精製方法では、まずオリゴ糖類含
有シロップ及び/又はオリゴ糖類含有粉末の水溶液に有
機溶媒を加えて加熱均一溶解する。
In the purification method of the present invention, first, an organic solvent is added to an aqueous solution of an oligosaccharide-containing syrup and / or an oligosaccharide-containing powder, and the mixture is heated and uniformly dissolved.

【0010】前記オリゴ糖類含有シロップ及び/又はオ
リゴ糖類含有粉末の水溶液中に含まれるオリゴ糖類とし
ては、大豆オリゴ糖、フルクトオリゴ糖、イソマルトオ
リゴ糖、キシロオリゴ糖、ガラクトオリゴ糖、乳果オリ
ゴ糖、でんぷん糖化液等の各種オリゴ糖類を挙げること
ができる。前記オリゴ糖類含有シロップ及び/又はオリ
ゴ糖類含有粉末の水溶液中における、該オリゴ糖類を含
むオリゴ糖類の含有濃度は、特に限定されるものではな
いが、好ましくは80W/W%以下、特に好ましくは、
後述する有機溶剤の使用量を少なくすることができる7
0〜80W/W%であるのが望ましい。含有濃度が80
W/W%を超える場合には、粘度が高くなり、しかも結
晶が析出し易くなり工業的操作性に問題が生じるので好
ましくない。
The oligosaccharides contained in the aqueous solution of the oligosaccharide-containing syrup and / or oligosaccharide-containing powder include soybean oligosaccharides, fructooligosaccharides, isomaltooligosaccharides, xylooligosaccharides, galactooligosaccharides, milk oligosaccharides, and starch saccharification. Various oligosaccharides such as liquid can be mentioned. In the aqueous solution of the oligosaccharide-containing syrup and / or oligosaccharide-containing powder, the content concentration of the oligosaccharide containing the oligosaccharide is not particularly limited, but preferably 80 W / W% or less, particularly preferably,
It is possible to reduce the amount of organic solvent used, which will be described later. 7
It is preferably 0 to 80 W / W%. Content concentration is 80
If it exceeds W / W%, the viscosity becomes high and crystals are likely to precipitate, which causes a problem in industrial operability, which is not preferable.

【0011】前記オリゴ糖類含有シロップ及び/又はオ
リゴ糖類含有粉末の水溶液に加える有機溶媒は、水存在
下におけるオリゴ糖類の温度別溶解度差が大きいものが
好ましく、特に極性が高くて炭素数が多いものが効果的
である。具体的には例えばメタノール、エタノール、イ
ソプロパノール、ブタノール等のアルコール類;プロパ
ノン、メチルエチルケトン等のケトン類;エチルエーテ
ル等のエーテル類;アセトニトリル等を挙げることがで
き、使用に際しては単独若しくは混合物として用いるこ
とができる。該有機溶媒の添加量は、有機溶媒の種類及
び加熱温度等によりことなるが、加熱均一溶解した際に
有機溶媒が均一に溶解する濃度、即ちオリゴ糖類含有シ
ロップ及び/又はオリゴ糖類含有粉末の水溶液を加熱し
た際白濁しない最大可能量まで有機溶媒を添加すること
ができる。加熱した状態でオリゴ糖類含有シロップ及び
/又はオリゴ糖類含有粉末の水溶液が白濁する量以上有
機溶媒を添加すると、オリゴ糖類の精製効率が低下し、
有機溶媒添加量が増加して非経済的である。
The organic solvent to be added to the aqueous solution of the oligosaccharide-containing syrup and / or the oligosaccharide-containing powder is preferably one having a large difference in the solubility of the oligosaccharide depending on the temperature in the presence of water, particularly one having a high polarity and a large number of carbon atoms. Is effective. Specific examples thereof include alcohols such as methanol, ethanol, isopropanol and butanol; ketones such as propanone and methyl ethyl ketone; ethers such as ethyl ether; acetonitrile and the like, which may be used alone or as a mixture. it can. The amount of the organic solvent added varies depending on the type of the organic solvent, the heating temperature, etc., but the concentration at which the organic solvent dissolves uniformly when heated and uniformly dissolved, that is, an aqueous solution of oligosaccharide-containing syrup and / or oligosaccharide-containing powder The organic solvent can be added up to the maximum possible amount that does not become cloudy when heated. When an organic solvent is added in an amount more than the amount in which the aqueous solution of oligosaccharide-containing syrup and / or oligosaccharide-containing powder becomes cloudy in a heated state, the purification efficiency of oligosaccharides decreases,
It is uneconomical because the amount of organic solvent added increases.

【0012】前記加熱は、加えた有機溶媒の沸点程度の
温度で加熱するのが最も好ましいが、有機溶媒の種類、
添加量等に応じて、有機溶媒が均一に溶解できる温度を
種々選択することができる。
Most preferably, the heating is carried out at a temperature around the boiling point of the added organic solvent.
Various temperatures at which the organic solvent can be uniformly dissolved can be selected according to the amount of addition and the like.

【0013】前記有機溶媒を加えて加熱均一溶解するに
は、例えば予め加熱温度及び有機溶媒の添加量を設定し
ておき、オリゴ糖類含有シロップ及び/又はオリゴ糖類
含有粉末の水溶液に、有機溶媒を添加し、白濁化した溶
液を所定温度に加熱して有機溶媒を均一溶解させて透明
にする方法、前記透明にした溶液の加熱温度を保持しな
がら、更に白濁しない最大可能量まで有機溶媒を徐々に
添加する方法若しくはオリゴ糖類含有シロップ及び/又
はオリゴ糖類含有粉末の水溶液を所定温度に加熱し、有
機溶媒を白濁しない量添加する方法等により行なうこと
ができる。この際いずれの場合も撹拌下に行なうことが
可能であり、更に水等を添加して溶液を希釈することも
できる。
To add the above organic solvent and dissolve it uniformly by heating, for example, the heating temperature and the addition amount of the organic solvent are set in advance, and the organic solvent is added to the aqueous solution of the oligosaccharide-containing syrup and / or the oligosaccharide-containing powder. A method of adding and heating the clouded solution to a predetermined temperature to uniformly dissolve the organic solvent to make it transparent, while maintaining the heating temperature of the transparent solution, gradually adding the organic solvent to the maximum possible amount without clouding. Or a method in which an aqueous solution of oligosaccharide-containing syrup and / or oligosaccharide-containing powder is heated to a predetermined temperature and an organic solvent is added in an amount that does not cause cloudiness. In this case, in any case, it can be carried out under stirring, and water or the like can be added to dilute the solution.

【0014】次いで本発明の精製方法では、前記加熱均
一溶解した溶液を、冷却することにより2層に分離す
る。該冷却は二層に分離する温度であれば良く、特に室
温程度であるのが好ましい。このように2層分離した上
層は、単糖類が多く含まれ、更に二糖類も含み、三糖類
以上のオリゴ糖類の含有量が少ない透明な液層であり、
一方下層は、二糖類、単糖類等も若干含まれるが三糖類
以上のオリゴ糖類が多く含まれる透明又は若干白濁した
液層である。このように2層に分離した下層のみを分別
回収して、例えば減圧濃縮等により有機溶媒を留去する
ことにより、下層から目的とする三糖類以上のオリゴ糖
類含有率が高いオリゴ糖類を得ることができる。この際
三糖類以上のオリゴ糖類含有率を更に高くするために、
分別回収した下層に対し、前記有機溶媒を加えて加熱均
一溶解し、冷却分離する工程を繰返し行なうこともでき
る。
Next, in the purification method of the present invention, the solution obtained by heating and uniformly dissolving is separated into two layers by cooling. The cooling may be performed at a temperature at which it is separated into two layers, and it is particularly preferable that it is about room temperature. In this way, the upper layer separated into two layers is a transparent liquid layer containing a large amount of monosaccharides, further containing disaccharides, and having a small content of oligosaccharides of trisaccharides or more,
On the other hand, the lower layer is a transparent or slightly cloudy liquid layer containing a small amount of disaccharides, monosaccharides, etc. but a large amount of trisaccharide or higher oligosaccharides. Thus, by separately collecting only the lower layer separated into two layers, and distilling off the organic solvent by, for example, concentration under reduced pressure, an oligosaccharide having a high content of oligosaccharides higher than the target trisaccharide is obtained from the lower layer. You can At this time, in order to further increase the oligosaccharide content of trisaccharide or higher,
It is also possible to repeat the steps of adding the organic solvent to the separated and recovered lower layer, heating and uniformly dissolving it, and cooling and separating.

【0015】[0015]

【発明の効果】本発明の精製方法では、特殊な設備等を
使用せずにオリゴ糖類含有シロップ及び/又はオリゴ糖
類含有粉末の水溶液から、三糖類以上のオリゴ糖類の組
成濃度が増加したオリゴ糖類を容易に精製することがで
きるので、従来のカラムクロマトグラフィー精製処理に
代えての利用が期待できる。また精製されたオリゴ糖類
は、生理的効果等を期待して、各種飲食品の添加成分等
として利用することができる。
EFFECTS OF THE INVENTION In the purification method of the present invention, an oligosaccharide having an increased composition concentration of oligosaccharides of trisaccharides or higher is prepared from an aqueous solution of oligosaccharide-containing syrup and / or oligosaccharide-containing powder without using special equipment. Since it can be easily purified, it can be expected to be used in place of conventional column chromatography purification treatment. The purified oligosaccharide can be used as an additive component of various foods and drinks, expecting physiological effects and the like.

【0016】[0016]

【実施例】以下実施例及び比較例により更に詳細に説明
するが、本発明はこれらに限定されるものではない。
EXAMPLES The present invention will be described in more detail with reference to Examples and Comparative Examples below, but the present invention is not limited thereto.

【0017】[0017]

【実施例1】市販の大豆オリゴ糖シロップ(SOE)をR.Bri
x40、60、76に調製した後、それぞれ50gに、エタノ
ールを60℃加熱時に均一溶解して、白濁化せずに透明
液となる限界量添加した。次いで室温まで冷却したとこ
ろ、液層が2層に分離したので、下層を分離回収し、下
層溶液の糖組成を高性能液体クロマトグラフィー(HP
LC)により分析した。その結果を表1に示す。尚試料
に用いた大豆オリゴ糖シロップの糖組成は、スタキオー
ス22.1%、ラフィノース11.4%、ショ糖41.
5%、グルコース10.0%、フラクトース15.0%
である。
Example 1 Commercially available soybean oligosaccharide syrup (SOE) was added to R. Bri.
After preparing x40, 60, and 76, ethanol was uniformly dissolved in 50 g each at the time of heating at 60 ° C., and a critical amount was added so that a transparent liquid was obtained without clouding. Then, when cooled to room temperature, the liquid layer was separated into two layers, so the lower layer was separated and recovered, and the sugar composition of the lower layer solution was analyzed by high performance liquid chromatography (HP
LC). The results are shown in Table 1. The sugar composition of the soybean oligosaccharide syrup used in the sample was stachyose 22.1%, raffinose 11.4%, sucrose 41.
5%, glucose 10.0%, fructose 15.0%
Is.

【0018】[0018]

【表1】 [Table 1]

【0019】表1の結果より、いずれのR.Brixの大豆オ
リゴ糖シロップからも、精製前よりも三糖類以上のオリ
ゴ糖類含有量が増加したシロップが精製されたことが判
る。尚、R.Brixが低い場合には、下層部分の分離率が低
くなるが、三糖類以上の精製効率は非常に向上すること
が判る。
From the results shown in Table 1, it can be seen that the syrup having an increased oligosaccharide content of trisaccharides or higher than that before purification was purified from any R. Brix soybean oligosaccharide syrup. It should be noted that when R. Brix is low, the separation rate of the lower layer portion is low, but it is understood that the purification efficiency of trisaccharides or higher is greatly improved.

【0020】[0020]

【実施例2】市販の大豆オリゴ糖シロップ(R.Brix76)
50gに、エタノールを表2に示すそれぞれの加熱温度
において均一溶解する限界量添加した。次いで室温まで
冷却したところ、液層が2層に分離したので、下層を分
離回収した後、再度下層溶液にエタノールを表2に示す
それぞれの加熱温度において均一溶解する限界量添加
し、室温まで冷却して2層に分離した後、下層を分離回
収した。回収した下層溶液の糖組成を実施例1と同様に
測定した。その結果を表2に示す。
Example 2 Commercial soybean oligosaccharide syrup (R. Brix76)
To 50 g, ethanol was added in a critical amount so that ethanol was uniformly dissolved at each heating temperature shown in Table 2. Then, when the mixture was cooled to room temperature, the liquid layer separated into two layers. Therefore, after separating and recovering the lower layer, ethanol was added again to the lower layer solution in the limit amount capable of uniformly dissolving at each heating temperature shown in Table 2, and cooled to room temperature. After separating into two layers, the lower layer was separated and collected. The sugar composition of the recovered lower layer solution was measured in the same manner as in Example 1. The results are shown in Table 2.

【0021】[0021]

【表2】 [Table 2]

【0022】表2の結果より、いずれの加熱温度におい
ても、精製前よりも三糖類以上のオリゴ糖類含有量が増
加したシロップが精製されたことが判る。また加熱温度
が高くなるにしたがって、三糖類以上の下層への移行が
高くなることが判る。
From the results shown in Table 2, it can be seen that at any heating temperature, the syrup having an increased content of oligosaccharides of trisaccharides or more than that before purification was purified. It is also found that the higher the heating temperature, the higher the transfer of trisaccharides or more to the lower layer.

【0023】[0023]

【実施例3】大豆オリゴ糖シロップ(R.Brix76)100
0gにエタノール518gを添加し、穏やかに撹拌しな
がら、75℃まで加熱して均一の透明溶液を得た。次い
で室温まで冷却して、2時間静置したところ2層に分離
したので、下層液955gを回収した。回収した下層液
を減圧濃縮機(ロータリーエバポレーター、バス温度5
0℃、真空度700mmHg、コンデンサー用循環冷却水温
度5℃)により処理して、精製大豆オリゴ糖シロップ
(R.Brix76)872gを回収した。回収物の糖組成を実
施例1と同様に分析した。結果を表3に示す。
[Example 3] Soybean oligosaccharide syrup (R.Brix76) 100
518 g of ethanol was added to 0 g, and heated to 75 ° C. with gentle stirring to obtain a uniform transparent solution. Then, the mixture was cooled to room temperature and allowed to stand for 2 hours, so that two layers were separated, so that 955 g of a lower layer liquid was recovered. The collected lower layer liquid is concentrated under reduced pressure (rotary evaporator, bath temperature 5
Treatment with 0 ° C., vacuum degree 700 mmHg, circulating cooling water temperature for condenser 5 ° C.) recovered 872 g of purified soybean oligosaccharide syrup (R.Brix76). The sugar composition of the recovered product was analyzed in the same manner as in Example 1. The results are shown in Table 3.

【0024】[0024]

【表3】 [Table 3]

【0025】[0025]

【比較例1】実施例3と同一ロットの大豆オリゴ糖シロ
ップ(R.Brix76)1000gにエタノール518gを添
加して、室温にて30分間撹拌した後、2時間静置した
ところ2層に分離したので、下層液1256gを回収し
た。回収した下層液を減圧濃縮機(ロータリーエバポレ
ーター、バス温度50℃、真空度700mmHg、コンデン
サー用循環冷却水温度5℃)により処理して、精製大豆
オリゴ糖シロップ(R.Brix76)953gを回収した。回
収物の糖組成を実施例1と同様に分析した。結果を表4
に示す。
Comparative Example 1 To 1000 g of the same lot of soybean oligosaccharide syrup (R.Brix76) as in Example 3 was added 518 g of ethanol, and the mixture was stirred at room temperature for 30 minutes and allowed to stand for 2 hours, whereby two layers were separated. Therefore, 1256 g of the lower layer liquid was recovered. The recovered lower layer solution was treated with a vacuum concentrator (rotary evaporator, bath temperature 50 ° C., vacuum degree 700 mmHg, circulating cooling water temperature for condenser 5 ° C.) to recover 953 g of purified soybean oligosaccharide syrup (R.Brix76). The sugar composition of the recovered product was analyzed in the same manner as in Example 1. The results are shown in Table 4.
Shown in.

【0026】[0026]

【表4】 [Table 4]

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】 オリゴ糖類含有シロップ及び/又はオリ
ゴ糖類含有粉末の水溶液から三糖類以上のオリゴ糖類含
有率を向上させたオリゴ糖類を精製する方法であって、
オリゴ糖類含有シロップ及び/又はオリゴ糖類含有粉末
の水溶液に、有機溶媒を加えて加熱均一溶解し、冷却し
た後、得られる2層分離液の下層を分別回収することを
特徴とするオリゴ糖類の精製方法。
1. A method for purifying an oligosaccharide having an improved oligosaccharide content of trisaccharide or higher from an aqueous solution of an oligosaccharide-containing syrup and / or an oligosaccharide-containing powder, the method comprising:
Purification of oligosaccharides, characterized by adding an organic solvent to an aqueous solution of oligosaccharide-containing syrup and / or oligosaccharide-containing powder, heating and uniformly dissolving the mixture, and cooling and then separating and recovering the lower layer of the resulting two-layer separation liquid. Method.
JP22745493A 1993-09-13 1993-09-13 Oligosaccharide purification method Expired - Lifetime JP3623974B2 (en)

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WO2002100875A1 (en) * 2001-06-11 2002-12-19 Kyowa Hakko Kogyo Co., Ltd. Crystals of oligosaccharides and processes for preparation thereof
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Cited By (9)

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Publication number Priority date Publication date Assignee Title
CN1093544C (en) * 1999-12-23 2002-10-30 中国食品发酵工业研究所 Stachyose and its preparing process
WO2002100875A1 (en) * 2001-06-11 2002-12-19 Kyowa Hakko Kogyo Co., Ltd. Crystals of oligosaccharides and processes for preparation thereof
US6913771B2 (en) 2002-01-09 2005-07-05 Oladur, Ltd Process for the production of soybean sugars and the product produced thereof
KR100450619B1 (en) * 2002-04-22 2004-09-30 학교법인 인제학원 The screening method for the immunomodulating oligosaccharides extracted from natural material using programmed cell death
US7618671B2 (en) 2003-11-05 2009-11-17 E.I. Du Pont De Nemours And Company Recovery of isoflavones and removal of oligosaccharides from aqueous mixtures using zeolites
JP2011037974A (en) * 2009-08-10 2011-02-24 Rengo Co Ltd Method for producing polysaccharide depolymerized product
CN103265583A (en) * 2013-03-05 2013-08-28 中国食品发酵工业研究院 Method for preparing stachyose crystal
CN103896994A (en) * 2014-03-11 2014-07-02 黑龙江八一农垦大学 Method for separating and extracting oligosaccharide from soybean whey waste liquid
CN114213475A (en) * 2021-12-29 2022-03-22 山东百龙创园生物科技股份有限公司 Preparation method of stachyose

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