JPH0574351B2 - - Google Patents

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Publication number
JPH0574351B2
JPH0574351B2 JP13479786A JP13479786A JPH0574351B2 JP H0574351 B2 JPH0574351 B2 JP H0574351B2 JP 13479786 A JP13479786 A JP 13479786A JP 13479786 A JP13479786 A JP 13479786A JP H0574351 B2 JPH0574351 B2 JP H0574351B2
Authority
JP
Japan
Prior art keywords
polygalactosamine
precipitate
necessary
precipitation
salt
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.)
Expired - Lifetime
Application number
JP13479786A
Other languages
Japanese (ja)
Other versions
JPS62292801A (en
Inventor
Junichi Tamura
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.)
Higeta Shoyu Co Ltd
Original Assignee
Higeta Shoyu 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 Higeta Shoyu Co Ltd filed Critical Higeta Shoyu Co Ltd
Priority to JP13479786A priority Critical patent/JPS62292801A/en
Publication of JPS62292801A publication Critical patent/JPS62292801A/en
Publication of JPH0574351B2 publication Critical patent/JPH0574351B2/ja
Granted legal-status Critical Current

Links

Description

【発明の詳細な説明】[Detailed description of the invention]

本発明はポリガラクトサミンの精製法に関する
ものである。 更に詳細には、本発明は、ペシロマイセス属菌
の生産するPF−101やアスペルギルス・パラシテ
イガスの生産するポリガラクトサミンなどを、有
機溶媒を使用することなく特異的に析出せしめ、
効率的に精製する方法に関するものである。 一般に、微生物の生産するポリガラクトサミン
としては、ペシロマイセス属菌の生産するPF−
101(特公昭56−12639)とアスペルギス・パラシ
テイカスの生産するポリガラクトサミン(J.B.C
vol.235 No.9 2538〜2541(1960))が知られて
いる。 従来、これらのポリガラクトサミンを精製する
には、培養液にアルコールなどの溶媒を添加して
沈澱として分離し、洗滌し、次いで熱水に溶解す
るか、または、更に精製する為には、セフアロー
ス6Bに吸着させ、緩衝液で溶出し、ポリガラク
トサミン画分を集める(特公昭56−12639)など
の方法によつて行なわれていた。 しかしながら、培養液中には中性多糖や低分子
糖が多量含まれ、溶媒による沈澱に随伴してしま
い、精製をくりかえし、純度の高い精製品を得る
には非常に煩雑な操作が必要であるし、また、回
収率も非常に悪い等の問題があつた。 本発明に先だつて、ポリガラクトサミンそのも
のが等電点をもつことから、清澄化した培養液を
PH調整し、等電点沈澱を試みたのであるが、PH調
整だけではポリガラクトサミンの沈澱を生起させ
るには至らなかつたのである。 本発明者は、ポリガラクトサミンの等電点沈澱
を起させれば精製は著じるしく容易になるとの考
えのもとに研究を行つたところ、培養液などのポ
リガラクトサミン含有液に液を存在させておけ
ば、中性多糖などの夾雑物があつても、析出物が
生じることを知つたのである。 また、本発明においては、塩の存在による析出
物は酸に良好に溶解することも分つたので、これ
らの方法を用いて著じるしく精製されたポリガラ
クトサミンをきわめて容易にしかも安価に製造す
ることを可能としたものである。 本発明は、ポリガラクトサミン含有液に有機溶
媒を用いることなく塩を2〜50%添加し、必要に
よつて析出を生ずるPH7.0〜9.0に調整し、析出物
を生成せしめることを特徴とするポリガラクトサ
ミンの精製法である。 また本発明は、ポリガラクトサミン含有液に有
機溶媒を用いることなく塩を2〜50%添加し、必
要によつて析出を生ずるPH7.0〜9.0に調整し、得
られた析出物を必要に応じて洗滌し、該析出物を
酸に溶解することを特徴とするポリガラクトサミ
ンの精製法である。 また、本発明は、ポリガラクトサミン含有液に
有機溶媒を用いることなく塩を2〜50%添加し、
必要によつて析出を生ずるPH7.0〜9.0に調整し、
得られた析出物を必要に応じて水洗し、該析出物
を酸に溶解し、析出を生ずるPH7.0〜9.0に調整
し、得られた析出物を必要に応じて洗滌し、再び
析出物を酸に溶解し、必要があれば上記の析出−
洗滌−溶解の操作をくり返すことを特徴とするポ
リガラクトサミンの精製法である。 本発明の精製法に適用されるポリガラクトサミ
ン含有液としては、夾雑物の多い培養液、除蛋白
した培養液、低分子物質を除去しかなり精製され
た培養液などいずれでもよい。 ポリガラクトサミン含有液に添加される塩とし
ては、次の例示の塩を含めて塩の1又は2以上で
ある。 即ち、塩化カリ、塩化ナトリウム、塩化カルシ
ウム、塩化アンモニウムなどの塩酸塩、硝酸カ
リ、硝酸ナトリウムなどの硝酸塩、酢酸ソーダな
どの酢酸塩、硫酸2カリ、硫安、硫酸カルシウ
ム、硫酸銅などの硫酸塩、リン酸2カリ、リン酸
1カリ、リン酸2ソーダ、リン酸1ソーダなどの
リン酸塩などが例示される。 添加する塩は溶解した状態であれば、どれだけ
でもよいが、好ましいのはポリガラクトサミン含
有液に対し0.5〜50%、より好ましくは2〜40%
程度である。 添加する塩の種類によつてはPHが7以上になる
ので、この場合はPHの調整を行なうことなく、ポ
リガラクトサミンが析出するので、析出物を分離
すればよい。 塩を添加しても析出を生じない場合はカセイソ
ーダ等のアルカリを用いて、PHを7〜9、好まし
くは等電点である8.5附近にPH調整を行えばよい。 ポリガラクトサミン含有液に塩の添加と場合に
よつてはPH7〜9の調整を行えば、夾雑物の妨害
によつて容易に析出しなかつたポリガラクトサミ
ンが析出を起し、夾雑物とは分離して析出する。
この析出物は遠心分離又は濾布による濾過によつ
て分離できる。 培養液をPH8.5の等電点処理をしてもポリガラ
クトサミンの析出は全く起らなかつたことからみ
れば、塩の添加だけでポリガラクトサミンの析出
が完全に起るということはきわめて意外なことで
ある。 分離した析出物は多量の塩を含んでいるので、
これを水や溶媒で洗滌して脱塩し、酸に溶解す
る。 酸としては酢酸などの有機酸、塩酸などの無機
酸などいずれの酸でもよく、また、濃度としては
0.01〜3モル程度のものがよい。 析出物を酸に溶解した後は、PH7〜9の等電点
附近の処理のみで容易に析出するようになつてい
るので、カセイソーダ等のアルカリを添加し、PH
7〜9、好ましくはPH8.5とPH調整し、析出物を
得る。 更に、精製するためには、この析出物を水等で
洗滌し、再び酸に溶解し、PH7〜9のPH調整を行
い、析出物を得ることができる。 この精製処理は何度でも行なうことができ、ほ
とんど純粋なポリガラクトサミンを得ることが可
能となつたのである。 次に本発明の試験例及び実施例を示す。 試験例 グルコース 3% ポリペプトン 0.3% CaCl2 0.5% PH 7.0 上記培地を用いてPaecilomyces sp I−1、
FERM−P3928を培養し、培養瀘液20を得た。
これを、55〜60℃に加熱しながら、限界分子量16
万のUF膜にて低分子物質の除去と循環を行い、
液量10を得た。 この清澄濃縮培養濾過液を100mlづつ21本用意
し、これに表1の塩を添加し、表1のPH調整を行
い、析出物の量を測定した。得られた結果は表1
に示される。 表中の回収率=析出物の乾燥重量/培養液中のガラクト
サミン量をインドール塩酸法で測定し、総量を算出×10
0 で表示した。
The present invention relates to a method for purifying polygalactosamine. More specifically, the present invention specifically precipitates PF-101 produced by Pecilomyces bacteria and polygalactosamine produced by Aspergillus parasitigus without using an organic solvent,
This invention relates to an efficient purification method. In general, polygalactosamine produced by microorganisms includes PF-
101 (Special Publication No. 56-12639) and polygalactosamine (JBC) produced by Aspergis parasiticus.
vol.235 No.9 2538-2541 (1960)) are known. Conventionally, to purify these polygalactosamines, a solvent such as alcohol is added to the culture solution to separate it as a precipitate, washed, and then dissolved in hot water, or for further purification, Sepharose 6B This was accomplished by adsorbing the polygalactosamine to a molecule, eluting it with a buffer solution, and collecting the polygalactosamine fraction (Japanese Patent Publication No. 12639/1983). However, the culture solution contains large amounts of neutral polysaccharides and low-molecular sugars, which are accompanied by precipitation from the solvent, requiring repeated purification and extremely complicated operations to obtain a purified product. However, there were also problems such as a very poor recovery rate. Prior to the present invention, since polygalactosamine itself has an isoelectric point, clarified culture fluid was
They attempted isoelectric precipitation by adjusting the pH, but pH adjustment alone did not lead to precipitation of polygalactosamine. The present inventor conducted research based on the idea that purification would be significantly easier if polygalactosamine was caused to undergo isoelectric precipitation. They learned that if left to dry, precipitates would form even in the presence of impurities such as neutral polysaccharides. In addition, in the present invention, it has been found that precipitates due to the presence of salts are well dissolved in acids, so using these methods, significantly purified polygalactosamine can be produced very easily and at low cost. This made it possible. The present invention is characterized in that 2 to 50% of salt is added to a polygalactosamine-containing liquid without using an organic solvent, and if necessary, the pH is adjusted to 7.0 to 9.0, which causes precipitation, to form a precipitate. This is a method for purifying polygalactosamine. In addition, the present invention adds 2 to 50% salt to a polygalactosamine-containing liquid without using an organic solvent, adjusts the pH to 7.0 to 9.0 to cause precipitation as necessary, and controls the resulting precipitate as necessary. This is a method for purifying polygalactosamine, which is characterized by washing the precipitate with water and dissolving the precipitate in acid. In addition, the present invention adds 2 to 50% salt to a polygalactosamine-containing liquid without using an organic solvent,
If necessary, adjust the pH to 7.0 to 9.0, which will cause precipitation.
The obtained precipitate is washed with water as necessary, the precipitate is dissolved in acid, the pH is adjusted to 7.0 to 9.0 at which precipitation occurs, the obtained precipitate is washed as necessary, and the precipitate is dissolved again. Dissolve in acid and precipitate as above if necessary.
This is a polygalactosamine purification method characterized by repeating washing and dissolving operations. The polygalactosamine-containing solution that can be applied to the purification method of the present invention may be any culture solution containing a large amount of contaminants, a culture solution from which protein has been removed, or a culture solution that has been significantly purified by removing low-molecular substances. The salt added to the polygalactosamine-containing solution is one or more salts including the following exemplified salts. Namely, hydrochlorides such as potassium chloride, sodium chloride, calcium chloride, ammonium chloride, nitrates such as potassium nitrate, sodium nitrate, acetates such as sodium acetate, sulfates such as dipotassium sulfate, ammonium sulfate, calcium sulfate, copper sulfate, Examples include phosphates such as dipotassium phosphate, monopotassium phosphate, disodic phosphate, and monosodium phosphate. Any amount of salt may be added as long as it is in a dissolved state, but it is preferably 0.5 to 50%, more preferably 2 to 40%, based on the polygalactosamine-containing liquid.
That's about it. Depending on the type of salt added, the pH will be 7 or more, so in this case, polygalactosamine will precipitate without adjusting the pH, so it is sufficient to separate the precipitate. If precipitation does not occur even after adding salt, the pH may be adjusted to 7 to 9, preferably around 8.5, which is the isoelectric point, using an alkali such as caustic soda. If salt is added to the polygalactosamine-containing solution and the pH is adjusted to 7 to 9 in some cases, polygalactosamine, which was not easily precipitated due to the interference of impurities, will precipitate and be separated from the impurities. and precipitate.
This precipitate can be separated by centrifugation or filtration with a filter cloth. Considering that no precipitation of polygalactosamine occurred even when the culture solution was subjected to isoelectric point treatment at pH 8.5, it is extremely surprising that the precipitation of polygalactosamine completely occurs just by adding salt. That's true. Since the separated precipitate contains a large amount of salt,
This is washed with water or a solvent to desalt it, and then dissolved in an acid. The acid may be any acid such as an organic acid such as acetic acid or an inorganic acid such as hydrochloric acid, and the concentration may be
It is preferably about 0.01 to 3 moles. After dissolving the precipitate in acid, the precipitate can be easily precipitated only by treatment near the isoelectric point of pH 7 to 9, so add an alkali such as caustic soda to the pH.
The pH is adjusted to 7 to 9, preferably 8.5, to obtain a precipitate. For further purification, the precipitate can be obtained by washing the precipitate with water or the like, dissolving it again in acid, and adjusting the pH to 7 to 9. This purification process can be repeated any number of times, making it possible to obtain almost pure polygalactosamine. Next, test examples and examples of the present invention will be shown. Test Example Glucose 3% Polypeptone 0.3% CaCl 2 0.5% PH 7.0 Using the above medium, Paecilomyces sp I-1,
FERM-P3928 was cultured and culture filtrate 20 was obtained.
While heating this to 55-60℃, limit molecular weight 16
We remove and circulate low-molecular substances using ten thousand UF membranes.
A liquid volume of 10 was obtained. Twenty-one bottles of 100 ml each of this clear concentrated culture filtrate were prepared, the salts shown in Table 1 were added thereto, the pH was adjusted as shown in Table 1, and the amount of precipitate was measured. The results obtained are shown in Table 1.
is shown. Recovery rate in the table = Dry weight of precipitate/Measure the amount of galactosamine in the culture solution using the indole-hydrochloric acid method and calculate the total amount x 10
Displayed as 0.

【表】 実施例 1 シユークロース 2% 酵母エキス 0.2% CaCl2 0.5% PH 7.0 上記培地を用いてPaecilomyces sp−−1、
FERM−P3928を培養し、培養濾過液150を得
た。これを55〜60℃に加熱しながら、限界分子量
16万のUF膜にて低分子物質の除去と濃縮を行い、
液量50を得た。さらに、これを遠心分離して熱
変性蛋白質と菌体残渣を除き、清澄濃縮培養液を
得た。得られた清澄濃縮培養液に酢酸ナトリウム
15Kgを加えて撹拌し溶解し、一夜放置した。生じ
た析出物をサラン製の布上に集め、大量の水で洗
い塩及び中性糖等の夾雑物を洗滌した。更にこの
析出物をオートクレーブで滅菌し、乾燥、粉砕し
て精製ポリガラクトサミンを得た。 回収ポリガラクトサミンの分析値を表2に示
す。 表中の回収(%)は実験例に同じ、galn含量
(%)の表示は精製物中のガラクトサミン含量を
インドール塩酸法で測定したものである。 表2 回収(%) galn含量(%) 水分(%) 灰 分 97 85 9.0 0.6 galn:ガラクトサミン 実施例 2 グルコース 3% ポリペプトン 0.3% CaCl2 0.5% PH 7.0 上記培地を用いてPaeclomyces sp −1、
FERM−P3928を培養し、培養濾過液100を得
た。これを55〜60℃に加熱しながら、限界分子量
16万のUF膜にて低分子物質の除去と濃縮とを行
い液量を60とした。さらに、これを遠心分離し
て菌体残渣と熱変性タンパク質を除き、清澄濃縮
培養濾過液を得た。得られた清澄濃縮培養濾過液
に硫安10.6Kg(30%飽和)を加えて溶解した。次
い、40%苛性ソーダを用いてPHを8.5にした。生
じた析出物を遠心して回収し、水に分散させて脱
塩した。さらに、これを0.1モルの塩酸に溶解し
た後、40%苛性ソーダにより再びPHを8.5にし、
析出物を得た。 この操作を二度繰返し夾雑物を除いた。さら
に、この析出物をオートクレーブ滅菌し、乾燥、
粉砕して精製ポリガラクトサミンとした。 精製結果は表3に示される。 表3中のgalnは各液中のガラクトサミン含量を
インドール塩酸法で測定し、その総量を算出した
ものである。また、回収(%)は培養液のgalnを
100とした時の各精製段階でのgalnの量の比率で
示してある。
[Table] Example 1 Seuculose 2% Yeast extract 0.2% CaCl 2 0.5% PH 7.0 Using the above medium, Paecilomyces sp--1,
FERM-P3928 was cultured to obtain 150 ml of culture filtrate. While heating this to 55-60℃, limit molecular weight
160,000 UF membranes remove and concentrate low-molecular substances,
A liquid volume of 50 was obtained. Furthermore, this was centrifuged to remove heat-denatured proteins and bacterial cell residue, to obtain a clear concentrated culture solution. Sodium acetate was added to the obtained clear concentrated culture solution.
15 kg was added, stirred to dissolve, and left overnight. The resulting precipitate was collected on a saran cloth and washed with a large amount of water to remove impurities such as salt and neutral sugar. Furthermore, this precipitate was sterilized in an autoclave, dried, and ground to obtain purified polygalactosamine. Table 2 shows the analytical values of the recovered polygalactosamine. The recovery (%) in the table is the same as in the experimental example, and the galn content (%) is the galactosamine content in the purified product measured by the indole-hydrochloric acid method. Table 2 Recovery (%) galn content (%) Moisture (%) Ash content 97 85 9.0 0.6 galn: Galactosamine Example 2 Glucose 3% Polypeptone 0.3% CaCl 2 0.5% PH 7.0 Using the above medium, Paeclomyces sp -1,
FERM-P3928 was cultured to obtain 100 ml of culture filtrate. While heating this to 55-60℃, limit molecular weight
Low molecular weight substances were removed and concentrated using a 160,000 UF membrane, and the liquid volume was reduced to 60,000. Furthermore, this was centrifuged to remove bacterial cell residue and heat-denatured proteins to obtain a clear concentrated culture filtrate. 10.6 kg of ammonium sulfate (30% saturation) was added and dissolved in the obtained clear concentrated culture filtrate. The pH was then brought to 8.5 using 40% caustic soda. The resulting precipitate was collected by centrifugation, dispersed in water, and desalted. Furthermore, after dissolving this in 0.1 mol of hydrochloric acid, the pH was adjusted to 8.5 again with 40% caustic soda.
A precipitate was obtained. This operation was repeated twice to remove impurities. Furthermore, this precipitate was sterilized in an autoclave, dried,
It was pulverized to obtain purified polygalactosamine. The purification results are shown in Table 3. Galn in Table 3 is the galactosamine content in each solution measured by the indole-hydrochloric acid method and the total amount calculated. In addition, the recovery (%) is based on the galn of the culture solution.
It is shown as the ratio of the amount of galn in each purification step when it is set to 100.

【表】 実施例 3 実施例2と同様にして得た清澄濃縮培養濾過液
160に食塩40Kgを加えて溶解した。 これから10づつサンプルA、B、Cをとり、
AはPH8.5に調整後生じた析出物をサラン製の布
上に集め、大量の水で洗い、過剰な食塩、夾雑物
を洗い流した後滅菌、乾燥、粉砕し精製ポリガラ
クトサミンを得た。 BはPH8.5に調整後生じた析出物を大量の水で
洗つた後、析出物を、0.1モルの酢酸に溶解した。
そして、この酢酸溶液を40%カセイソーダでPH
8.5に調整し析出物を生じせしめ、同様に水洗、
滅菌、乾燥、粉砕して精製ポリガラクトサミンを
得た。 CはPH7.5に調整後生じた析出物を大量の水で
洗つた後、滅菌、乾燥、粉砕し精製ポリガラクト
サミンを得た。 各サンプルについての回収(%)分析値を表4
に示す。 表4中の回収(%)、galn含量(%)の表示は
実施例1に同じ。
[Table] Example 3 Clear concentrated culture filtrate obtained in the same manner as Example 2
160 and 40 kg of salt was added and dissolved. From now on, take 10 samples A, B, and C.
In A, the precipitate generated after adjusting the pH to 8.5 was collected on a saran cloth, washed with a large amount of water, excess salt and impurities were washed away, and then sterilized, dried, and crushed to obtain purified polygalactosamine. In B, the precipitate formed after adjusting the pH to 8.5 was washed with a large amount of water, and then the precipitate was dissolved in 0.1 mol of acetic acid.
Then, PH this acetic acid solution with 40% caustic soda.
Adjust to 8.5 to generate precipitate, wash with water in the same way,
Purified polygalactosamine was obtained by sterilization, drying, and pulverization. After adjusting the pH to 7.5, the resulting precipitate was washed with a large amount of water, followed by sterilization, drying, and pulverization to obtain purified polygalactosamine. Table 4 shows recovery (%) analysis values for each sample.
Shown below. The indications of recovery (%) and galn content (%) in Table 4 are the same as in Example 1.

【表】 実施例 4 実施例2の培値を用いてPaeclomyces −
1、FERM−P 3928を液体培養して培養濾過
液10を得た。これを80℃、一時間加熱してタン
パク質を変性させた。さらに、これを遠心して不
溶物を除いた。次いで、この溶液に塩安3Kg(30
%溶液)を加えて溶解し、PHを8.5に合せた。生
じた析出物を遠心して回収した。この析出物を同
じ濃度の塩安溶液で洗い可溶物質を除いた。次に
この沈澱を0.01モルの燐酸に溶解し、40%苛性ソ
ーダでPHを8.5に合わせて等電点沈澱させた。 次に実施例1と同様に、脱塩、燐酸溶解、PH
8.5調整を二度くり返し、滅菌、乾燥、粉砕し、
精製ポリガラクトサミンを得た。 表5中の回収(%)、galn含量(%)は実施例
1に同じ。 回収(%)と分析値は表5に示す。 表5 精製ポリガラクトサミンの回収と分析値 回収(%) galn含量(%) 水分(%) 灰分(%) 73 92.5 5.5 1.9
[Table] Example 4 Using the culture values of Example 2, Paeclomyces −
1. FERM-P 3928 was cultured in liquid to obtain culture filtrate 10. This was heated at 80°C for one hour to denature the protein. Furthermore, this was centrifuged to remove insoluble matter. Next, add 3 kg of ammonium chloride (30 kg) to this solution.
% solution) was added and dissolved, and the pH was adjusted to 8.5. The resulting precipitate was collected by centrifugation. This precipitate was washed with an ammonium salt solution of the same concentration to remove soluble substances. Next, this precipitate was dissolved in 0.01 mol of phosphoric acid, and the pH was adjusted to 8.5 with 40% caustic soda for isoelectric precipitation. Next, in the same manner as in Example 1, desalination, phosphoric acid dissolution, PH
8.5 Repeat the adjustment twice, sterilize, dry, crush,
Purified polygalactosamine was obtained. Recovery (%) and galn content (%) in Table 5 are the same as in Example 1. Recovery (%) and analytical values are shown in Table 5. Table 5 Recovery of purified polygalactosamine and analysis value recovery (%) Galn content (%) Moisture (%) Ash content (%) 73 92.5 5.5 1.9

Claims (1)

【特許請求の範囲】 1 ポリガラクトサミン含有液に有機溶媒を用い
ることなく塩を2〜50%添加し、必要によつて析
出を生ずるPH7.0〜9.0に調整し、析出物を生成せ
しめることを特徴とするポリガラクトサミンの精
製法。 2 ポリガラクトサミン含有液に有機溶媒を用い
ることなく塩を2〜50%添加し、必要によつて析
出を生ずるPH7.0〜9.0に調整し、得られた析出物
を必要に応じて洗滌し、該析出物を酸に溶解する
ことを特徴とするポリガラクトサミンの精製法。 3 ポリガラクトサミン含有液に有機溶媒を用い
ることなく塩を2〜50%添加し、必要によつて析
出を生ずるPH7.0〜9.0に調整し、得られた析出物
を必要に応じて水洗し、該析出物を酸に溶解し、
析出を生ずるPHに調整し、得られた析出物を必要
に応じて洗滌し、再び析出物を酸に溶解し、必要
があれば上記の析出−洗滌−溶解の操作をくり返
すことを特徴とするポリガラクトサミンの精製
法。
[Claims] 1. Adding 2 to 50% salt to a polygalactosamine-containing solution without using an organic solvent, adjusting the pH to 7.0 to 9.0, which causes precipitation if necessary, and causing precipitation to occur. Characteristic polygalactosamine purification method. 2 Add 2 to 50% of salt to the polygalactosamine-containing solution without using an organic solvent, adjust the pH to 7.0 to 9.0 to cause precipitation if necessary, wash the obtained precipitate as necessary, A method for purifying polygalactosamine, which comprises dissolving the precipitate in an acid. 3. Add 2 to 50% of salt to the polygalactosamine-containing solution without using an organic solvent, adjust the pH to 7.0 to 9.0 to cause precipitation if necessary, and wash the obtained precipitate with water if necessary, Dissolving the precipitate in acid,
The method is characterized by adjusting the pH to a level that causes precipitation, washing the obtained precipitate as necessary, dissolving the precipitate in acid again, and repeating the above precipitation-washing-dissolution operation if necessary. A method for purifying polygalactosamine.
JP13479786A 1986-06-12 1986-06-12 Purification of polygalactosamine Granted JPS62292801A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP13479786A JPS62292801A (en) 1986-06-12 1986-06-12 Purification of polygalactosamine

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP13479786A JPS62292801A (en) 1986-06-12 1986-06-12 Purification of polygalactosamine

Publications (2)

Publication Number Publication Date
JPS62292801A JPS62292801A (en) 1987-12-19
JPH0574351B2 true JPH0574351B2 (en) 1993-10-18

Family

ID=15136757

Family Applications (1)

Application Number Title Priority Date Filing Date
JP13479786A Granted JPS62292801A (en) 1986-06-12 1986-06-12 Purification of polygalactosamine

Country Status (1)

Country Link
JP (1) JPS62292801A (en)

Also Published As

Publication number Publication date
JPS62292801A (en) 1987-12-19

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