JP3331870B2 - Method for producing water-soluble polysaccharide - Google Patents

Description

DETAILED DESCRIPTION OF THE INVENTION

[0001] The present invention relates to a water-soluble polysaccharide in which foaming is prevented.
The present invention relates to a saccharide and a method for producing the saccharide .

[0002]

2. Description of the Related Art In general, when polysaccharides of plant origin are extracted from their raw materials, foaming occurs due to the effects of saccharides, proteins, glycoproteins, amino acids, saponins and the like contained in the raw materials, and also during the production process. It is also a problem during the use process. This problem is particularly serious when beans such as soybeans are used as a raw material. In order to prevent such foaming, a method of adding a defoaming agent such as a sucrose fatty acid ester or a sorbitan fatty acid ester, particularly a silicone resin, has been used. Not only does it impair the image, but also does not provide a fundamental solution, so it cannot always be said that a complete defoaming effect has been obtained. Further, among these water-soluble polysaccharides, since the turbidity of the aqueous solution is high, if a large amount is added to a transparent beverage, the transparency of the beverage may be impaired and the image may be deteriorated.

Further, the extracted water-soluble polysaccharide contains impurities such as so-called high molecular weight proteins, and is adsorbed and removed using activated carbon, ion exchange resin, hydrophobic resin, silica gel, etc. in order to remove these impurities. When the purification treatment is performed, impurities such as the protein block the pores of the adsorbent and rapidly reduce the adsorption performance. On the other hand, in the case of purification using filtration such as ultrafiltration or reverse osmosis membrane, the polymer component cannot be removed because it does not pass through its pores, and the degree of purification does not increase.

[0004]

As described above, the problems relating to the method for producing a water-soluble polysaccharide are not always completely satisfied at present.

[0005]

Means for Solving the Problems The inventors of the present invention have conducted intensive studies in view of the above points, and found that when producing water-soluble polysaccharides, particularly plant-derived water-soluble polysaccharides, they are treated with a protease. It was found that foaming was low, the transparency of the aqueous solution was good, and the cost in the purification process could be reduced.

That is, the present invention provides a water-soluble polysaccharide derived from soybean having a foaming power of not more than 6.0 and an extract of the water-soluble polysaccharide, which is treated with a protease to form an aggregate, A method for producing a water-soluble polysaccharide in which foaming is prevented, comprising removing the generated aggregates and further purifying the resultant using any of an adsorbent, ultrafiltration, or a reverse osmosis membrane. .

There are several methods for producing water-soluble polysaccharides from plants, for example, water-insoluble components of beans such as soybeans (such as okara), water-insoluble components of grains such as rice bran and bran, and the like.
A method for producing a water-soluble polysaccharide by pulverizing water-insoluble components derived from plants such as potatoes, vegetables and fruits, and enzymatically decomposing proteins and fibers contained in the finely divided fibers is disclosed in -67595. In the present invention, water-soluble polysaccharides from beans, especially soybeans, are most suitable for producing by utilizing extraction near the isoelectric point of the protein contained in the raw material, but the sap is collected like gum arabic. It is also effective for water-soluble polysaccharides obtained by
In the present invention, any of these methods can be applied.

As the protease in the present invention, proteases, peptidases and the like can be used. Specifically, any of endo-type and exo-type such as pepsin, trypsin, papain, subtilisin and bromelain can be used. They may be used alone or in combination.

[0009] The reaction conditions of the enzyme may be performed under the respective optimum conditions. However, when the enzyme is acted on when it is obtained by extracting from a plant, it is effective to perform it after the extraction. That is, after extracting the polysaccharide from the raw material, rather than allowing the enzyme to act on the slurry liquid before separating the extract, after extracting the polysaccharide from the raw material, the enzyme is allowed to act on the extract separated from the extract. It is more effective because the effect is exhibited with a small amount of enzyme.

[0010] The above-mentioned Japanese Patent Application Laid-Open No. 3-67595 discloses that an enzyme decomposes a protein contained in a finely divided fiber, but the enzymatic decomposition involves extracting a water-soluble polysaccharide. Therefore, the effect of the present invention cannot be obtained.

In the reaction solution after the enzymatic treatment, fine suspended matters which existed before the reaction are aggregated and coarsened, and this is filtered with filter cloth, filter paper, ceramic, membrane filter,
It is removed by filtration such as diatomaceous earth filtration or by centrifugation. The liquid thus purified (removed) has a higher transparency than the liquid not subjected to the enzyme treatment. Further, in the case of a polysaccharide mainly containing sap oozing out of a tree, such as gum arabic or Japanese larch arabinogalactan, it is preferable to use an aqueous solution having an appropriate concentration once.

Next, according to the present invention, the protein component present in the polysaccharide is reduced in molecular weight, and the protein present in the form of polysaccharide and glycoprotein is separated from the polysaccharide and further reduced in molecular weight. . As a result, when using adsorption such as activated carbon, ion exchange resin, hydrophobic resin, and silica gel in the purification process, the amount of adsorption per unit of the adsorbent increases because the adsorbent is used to the deep part of the pores. Even if an adsorbent is used, the amount of impurities removed increases and the degree of purification increases.

In the case of purification by removing low molecular components such as ultrafiltration and reverse osmosis membrane together with the filtrate in the purification, the amount of impurities passing through the pores of these filtration membranes increases. This not only increases the degree of purification per unit processing time, but also increases the amount of impurities removed, thereby improving the degree of purification at the final stage of purification.

[0014]

The embodiments of the present invention will be described below with reference to examples, but these are only examples, and the spirit of the present invention is not limited by these examples. In addition, in an example, all parts and% mean a weight basis.

Example 1 Three times the amount of water was added to raw okara obtained in the step of producing isolated soybean protein, and the pH was adjusted to 4.5 with hydrochloric acid.
Extracted at 1.5 ° C. for 1.5 hours. After cooling, centrifuge (1000
× 30 minutes), and separated into a supernatant and a precipitate. The supernatant (water-soluble polysaccharide solution) thus obtained was adjusted to pH 7.0, and protease A (manufactured by Amano Pharmaceutical Co., Ltd.) was added as a protease at a concentration of 0.01% per solution.
For 120 minutes. The solution is centrifuged (1000
(0 G × 20 minutes), and suspended matter generated by the reaction was removed. The removed solution was heated at 90 ° C. for 15 minutes to deactivate the enzyme, and then activated carbon (Shirasagi KL: Takeda Pharmaceutical Co., Ltd.,
) Column. The purified solution was freeze-dried, and the crude protein, crude ash, 5% aqueous turbidity, and foaming power were measured. Crude protein and ash were analyzed by a method in accordance with the Food Sanitation Law, and turbidity was measured using a spectrophotometer. Foaming power is 5% aqueous solution in 100 ml of graduated cylinder with stopper.
It was obtained by the method shown in FIG. That is, the height (h) of the foam in the container (measuring cylinder) was divided by the total height (H) of the foam and the solution, and expressed as a percentage.

COMPARATIVE EXAMPLE 1 As in Example 1, a water-soluble polysaccharide was extracted from soybeans, and then adjusted to pH 7.0 without adding a protease.
Heat for 20 minutes. This solution was centrifuged (10000 G ×
20 minutes) and the precipitate was removed. The solution from which the precipitate was removed was purified using an activated carbon (Shirasagi KL: Takeda Pharmaceutical Co., Ltd.) column. The purified solution was freeze-dried, and the crude protein, crude ash content, 5% aqueous solution turbidity and foaming power were measured.

Example 2 A water-soluble polysaccharide was extracted from soybeans in the same manner as in Example 1 and then subjected to protease treatment, followed by centrifugation, followed by inactivation of the enzymes and ultrafiltration (Tosoh: UF-LMS system membrane). : UF-2CS-1000PS) and concentrated by 5 times. The purified solution was freeze-dried, and the crude protein, crude ash content, 5% aqueous solution turbidity and foaming power were measured.

Comparative Example 2 A water-soluble polysaccharide was extracted from soybeans in the same manner as in Example 1, and then the pH was adjusted to 7.0 without adding protease.
Heat at 0 ° C. for 120 minutes. The solution is centrifuged (100
(00G × 20 minutes), and the precipitate was removed. The solution from which the precipitate has been removed is subjected to ultrafiltration (Tosoh: UF-LMS system).
The membrane was purified in the same manner as in Example 2 using UF-2CS-1000PS). The purified solution was freeze-dried, and the crude protein, crude ash content, 5% aqueous solution turbidity and foaming power were measured.

The results of the analysis and the operation time ratio when the purification is performed by ultrafiltration (operation time when Example 2 is set to 100) are shown below. Analysis result and operation time ratio of each polysaccharide ──────────────────────────────── Measurement item Example 1 Comparative example 1 Example 2 Comparative Example 2 粗 Crude protein (%) 3.2 5.2 2.5 4.7 Crude ash (%) 4.5 4.6 2.2 2.9 Turbidity 0.07 0.54 0.03 0.57 Foaming power 5.7 73.9 6.0 77.5 Ultrafiltration time ratio 100 143 ─────────────────────── ─────────

From the above results, the degree of purification of the polysaccharide obtained according to the present invention was improved as compared with the comparative example in which similar purification was carried out.
Foaming power and turbidity were significantly reduced. In addition, the operation time when purification was performed using ultrafiltration was shorter in the present invention, and the treatment operation was easier.

[0021]

As described above, by performing the protease treatment when preparing the water-soluble polysaccharide, the foaming power and the turbidity of the aqueous solution are significantly reduced, and the amount of auxiliary materials used for purification can be reduced.

[Brief description of the drawings]

FIG. 1 is a schematic diagram of a method of obtaining a foaming power in each example.

Continued on the front page (72) Inventor Mitsuo Hattori 4-3, Kinokudai, Taniwahara-mura, Tsukuba-gun, Ibaraki Pref. Fuji Oil Co., Ltd. Tsukuba R & D Center (72) Inventor Yuichi Maeda 4-chome, Kinawadai, Yawahara-mura, Tsukuba-gun, Ibaraki No. 3 Fuji Oil Co., Ltd. Tsukuba Research & Development Center (72) Inventor Norio Sawamura 1 Sumiyoshi-cho, Izumisano-shi, Osaka Prefecture Fuji Oil Co., Ltd. Hannan Factory Inspector Kenji Hiromi (56) References JP JP-A-7-188301 (JP, A) JP-A-57-115145 (JP, A) Agricultural and Biological Chemistry, 46 (5), 129 Production Research, 33 (6), p. 299-302, 1981 PERIODICA POLYTEC HNICA CHEMICAL ENG INEERING, 36 ((58) Fields investigated (Int. Cl. ⁷ , DB name) C08B 37/00 CA (STN)

Claims (2)

(57) [Claims] 1. A large body prescribed foaming power is 6.0 or less
Water-soluble polysaccharides derived from beans . 2. A proteinaceous water-soluble polysaccharide extract derived from soybean
Prevention of foaming, characterized by treating with a degrading enzyme to form aggregates, removing the formed aggregates, and further purifying using any of an adsorbent, an ultrafiltration or a reverse osmosis membrane. Of producing a water-soluble polysaccharide.