JPS6062996A - Preparation of xanthan gum - Google Patents

Preparation of xanthan gum

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Publication number
JPS6062996A
JPS6062996A JP17057083A JP17057083A JPS6062996A JP S6062996 A JPS6062996 A JP S6062996A JP 17057083 A JP17057083 A JP 17057083A JP 17057083 A JP17057083 A JP 17057083A JP S6062996 A JPS6062996 A JP S6062996A
Authority
JP
Japan
Prior art keywords
xanthan gum
culture solution
desalting
concentration
inorganic 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.)
Granted
Application number
JP17057083A
Other languages
Japanese (ja)
Other versions
JPS6111596B2 (en
Inventor
Keisuke Hisayoshi
啓資 久芳
Masashi Goto
後藤 政志
Toshihiro Ikemoto
池本 利廣
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.)
Kohjin Holdings Co Ltd
Original Assignee
Kohjin Holdings 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 Kohjin Holdings Co Ltd filed Critical Kohjin Holdings Co Ltd
Priority to JP17057083A priority Critical patent/JPS6062996A/en
Publication of JPS6062996A publication Critical patent/JPS6062996A/en
Publication of JPS6111596B2 publication Critical patent/JPS6111596B2/ja
Granted legal-status Critical Current

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  • Preparation Of Compounds By Using Micro-Organisms (AREA)

Abstract

PURPOSE:To obtain xanthan gum having high solution viscosity, improved salt resistance, heat resistance, and acid resistance, by desalting a culture solution containing xanthan gum until it has a specific concentration of inorganic salt, drying it directly. CONSTITUTION:A bacterium belonging to the genus Xanthomonas is cultivated ina nutritive medium consisting of carbon, nitrogen, and an inorganic salt to give a culture solution containing xanthan gum. The prepared culture solution is desalted until the concentration of inorganic salt becomes <=5wt%, preferably <=2wt% based on xanthan gum. The desalted culture solution is directly dried. Desalting bu ultrafilter is the fittest as desalting process used. Namely, since xanthan gum has high molecular weight of about 2,000,000, the inorganic salt is a low-molecular-weight substance, so the desired desalting can be easily attained by the ultrafilter having 10,000-500,000 fraction molecular weight.

Description

【発明の詳細な説明】 本発明は、その溶液粘度が高く、シかも耐塩性。[Detailed description of the invention] The present invention has high solution viscosity and salt resistance.

耐熱性、耐酸性が1?れてい売キサンタンガム本米のゲ
r性を有し、かつその製造コストがきわめて安価である
事を特徴とした。キサンタンガム製造方法に関するもの
である。
Heat resistance and acid resistance are 1? It is characterized by having the gelatin properties of regular xanthan gum and being extremely inexpensive to produce. This invention relates to a method for producing xanthan gum.

キサンタンガムは、タンク培養を行える事による生産の
安定性、並びに溶液物性の特異性等により近年、賞品あ
るいは二[業厘料としてその用途は益々広がりつつある
。しかしながらキサンタンガムは他の天然ガム類に比べ
高価なために、晶η的に優れてはいるがその使几1はか
なり限定されたものとなっているのが現状である。すな
わち、キサンタンガムの精製方法は、培養液を必要にt
L5、じ加熱殺菌し、菌体を遠心分Flftあるい(l
−j濾過により除去したのち、これにイソプロパツール
等のアルコール類を添加り、てガム*を沈睡せしめ、こ
れを分離回収し、乾燥して製品とする方法がその代表的
なものである。ここで、キサンタンガムの鞘製コストヲ
高めているのは、キサンタンガムの沈禮に1e用するア
ルコールのコストとその蒸留回収に必要な蒸気コストで
ある。、 従来かかるアルコールコスト&びアルコール回収コスト
を下げる方法と17で、以下に示した■。
In recent years, xanthan gum has been increasingly used as a prize or commercial material due to its production stability due to tank culture and unique solution properties. However, since xanthan gum is more expensive than other natural gums, its uses are currently quite limited, although it has excellent crystallization properties. In other words, the method for purifying xanthan gum requires t
L5, heat sterilized and centrifuged the bacterial cells by Flft or (l
A typical method is to remove the gum by filtration, add alcohol such as isopropanol to make the gum* settle, separate and collect it, and dry it to make a product. Here, what increases the cost of producing xanthan gum pods is the cost of the alcohol used to precipitate the xanthan gum and the cost of the steam necessary for its distillation recovery. , Methods to reduce conventional alcohol costs and alcohol recovery costs and 17 are shown below.

■の方法が検討考案されている。■Method has been studied and devised.

■アルコール以外の沈澱剤をJfilいる方法。(例え
ばS、 P+Rogovinら、J3ioeng、 H
ioLechnoJ、 5. 91 +19(38) ■培養液を直接スプレー乾燥あるいはドラム乾燥する方
法。(例えばS、 13.几ogovinら、f3io
enr<。
■Method using Jfil as a precipitant other than alcohol. (e.g. S, P+Rogovin et al., J3ioeng, H
ioLechnoJ, 5. 91 +19 (38) ■ Direct spray drying or drum drying of the culture solution. (e.g. S, 13. Ogovin et al., f3io
enr<.

Uiolechnol、 L 161+ 1965 )
■培養液を濃縮し、アルコールの1史川引を減少させる
方法。
Uiolechnol, L 161+ 1965)
■A method of concentrating the culture solution and reducing the alcohol content.

しかしながら、上記の方法はそれぞれ実施に当っては問
題も多く、十分子r、解決方法とは言えない。
However, each of the above methods has many problems when implemented, and cannot be called a solution.

スfz b ラ、■の例としては、第4級アンモニウム
塩を添加して、キサンタンガムとコンプレックスを形成
させ、ガム質を培養n々から分離させた後。
For example, after adding a quaternary ammonium salt to form a complex with xanthan gum and separating the gum from the culture n.

この沈澱ガムをアルコールで洗滌し、第4級アンモニウ
ム塩を溶解除去し、精製キサンタンガムを得る方法があ
る。しかしながら、この方法では。
There is a method in which purified xanthan gum is obtained by washing this precipitated gum with alcohol to dissolve and remove the quaternary ammonium salt. However, with this method.

第4級アンモニウム塩及びアルコールの蒸留回収が必要
であり、十分なコストダウンは期待されない。1だ本方
法により得られたキサンタンガムは。
Distillation recovery of the quaternary ammonium salt and alcohol is required, and sufficient cost reduction is not expected. The xanthan gum obtained by this method is:

第44級アンモニウム塩が残存するため良品用途には1
史甲できない欠点も・目している。■はきわめて容易な
方法で、低コストの製品が得られる利a&まあるものの
、溶液物性1色、臭い等いづれもiM常のアルコール精
製方法によって得られたキサンタンガムに比較して、き
わめて劣るものである。■はアルコールの使用1景を下
げるための方法として。
Because the 44th class ammonium salt remains, 1.
He also sees flaws that Fukou can't do. Method (2) is an extremely easy method and has the advantage of producing a low-cost product, but the physical properties of the solution, such as one color and odor, are extremely inferior to xanthan gum obtained by iM's usual alcohol purification method. be. ■As a way to reduce alcohol use.

容易に思いつく方θ工であるが、培養液が高粘怖゛を示
すため、高1β度1での濃縮は帷しく、また沈澱ガムの
洗滌用に用いるアルコールも宮めると、やけり長棺−の
溶媒が必要であり、十分なコストダウンは期待されない
、 本発明者らは、最も工業的に・角利な製法と考えられる
培養液の直接乾燥方法によって、良質のキサンタンガム
を得る4↓を目的とし、従来の精製法の問題点の原因を
十分検討した結果、培養液中の無機塩の存在がこi”t
ら物性に大きな影響を与える事を見いだ【7.培養液を
直接乾燥するに当たり。
This method is easy to think of, but since the culture solution is highly viscous, concentration at a high 1β degree is time-consuming, and it also takes a long time if the alcohol used for washing the precipitated gum is also used. The present inventors obtained high-quality xanthan gum by direct drying of the culture solution, which is considered to be the most industrially and advantageous manufacturing method.4↓ With the aim of
It was found that this had a great effect on the physical properties [7. When directly drying the culture solution.

あらかじめ無機塩類を除去する事によって良質のキサン
タンガムが得ら几る事を見いだし9発明を完成するに至
ったものである。キサンタンガムを含む培養液中には、
初めに加えられた・1四稗塩類旬外にd(調整のために
添加された酸、アルカリにより形成されたN11!塩類
のため、ガム質にメll、−r。
They discovered that high-quality xanthan gum could be obtained by removing inorganic salts in advance, and completed the invention. In the culture solution containing xanthan gum,
The salts added at the beginning are d (N11! salts formed by acids and alkalis added for adjustment, so it becomes gummy, -r.

約7〜25%の無機塩類が仔在しており、これを。Approximately 7 to 25% of inorganic salts are present.

このまま直接乾燥して得られた製品は、1(7品中のキ
サンタンガム純度が低くなるばかりでなく、キサンタン
ガム濃度当りの粘度もきわめて低く、さらに着色度、臭
いも太きく、良itのキサンタンガムとは言えないもの
であった。本発明においては同じ培養液をあらかじめそ
の無機塩類の#用゛がガム質に対し5%以下、好ましく
は2係却下になるまで脱塩し、た後、直接乾燥すること
により、すべての品′e(が改善され、精製法としてず
tt米711いられて米たアルコール精製法によって得
られたキサンタンガムとほぼ同等の品質を射するものを
得ることができる。
The product obtained by directly drying it as it is is 1 (7 products) Not only does the xanthan gum purity become low, but the viscosity per xanthan gum concentration is also extremely low, and the degree of coloration and odor are also strong. In the present invention, the same culture solution is desalted in advance until the content of inorganic salts in the gum is less than 5%, preferably less than 2%, and then directly dried. As a result, all the products 'e' are improved, and it is possible to obtain a product which exhibits almost the same quality as the xanthan gum obtained by the rice alcohol purification method.

更に本発明の特徴の1つは、製品の俗解性がi憂れてい
る事である。利点の2つ目は、アルコール精製法では、
設備にすべて防爆性が要求され、また消火設備等も必要
となるのに比べ本発明の製造方法では一切アルコール類
ケ団用せず、しかも工程がきわめて簡略でちるため、初
期の設備コストを大幅に低減する事ができる事である。
Furthermore, one of the features of the present invention is that the product is not easy to understand. The second advantage is that with the alcohol purification method,
All equipment is required to be explosion-proof and also requires fire extinguishing equipment, etc. However, the manufacturing method of the present invention does not use alcohol at all, and the process is extremely simple, resulting in a significant reduction in initial equipment costs. This can be reduced to

利点の3つ目は1食品用途向けに使用する場合、従来の
アルコール精製法においては、4q品中の残存アルコー
ル、特に残存イソプロピルアルコールが問題となってお
9.残存溶媒を下げる半は技術的にもかなり喧しいと言
われているが1本発明の製造方法によれば、アルコール
を使用しないためそのような残存溶媒の問題はまったく
発生する事がないへ魅に利点の4つ目は、 41機浴媒
ケ1史)T+ +、、ないため作宥環境が改善される点
であり、これは工業化の点でも大きな利点となる。
The third advantage is 1. When used for food applications, in conventional alcohol purification methods, residual alcohol, especially residual isopropyl alcohol, in the 4q product becomes a problem.9. It is said that reducing the amount of residual solvent is technically quite difficult, but according to the production method of the present invention, no alcohol is used, so such problems with residual solvent do not occur at all. The fourth advantage is that the environment is improved because there is no T+ +, which is a great advantage in terms of industrialization.

以下に1本発明を庚に説明する。The present invention will be briefly explained below.

本発明で用いるキサンタンガム培養液eま1通常の栄養
培地でキサントモナス属#1lV4を培養して得られた
ものなら、その培養方法がバッチ培養でも。
The xanthan gum culture solution used in the present invention can be obtained by culturing Xanthomonas #11V4 in a normal nutrient medium, even if the culture method is batch culture.

連続培養であっても適用可能である。It is also applicable to continuous culture.

次に2本発明で使用する脱塩方法とし−Cは、紳種検討
し7た結果、限外濾過膜による脱塩方式がIi)χ適で
ある事を見いだした。すなわち、キサンタンガムの分子
音が約200万と大きいのに対し、 Jet:機塩は低
分子物質であるため1分画分子量1万〜50万の限外濾
過膜により容易に目的の脱塩を1宰成する事ができる。
Next, as for the desalting method used in the present invention, -C, after thorough investigation, it was found that the desalting method using an ultrafiltration membrane is suitable for Ii). In other words, while xanthan gum has a large molecular sound of approximately 2 million yen, Jet: Machine Salt is a low-molecular substance, so it can easily achieve the desired desalination using an ultrafiltration membrane with a molecular weight cut-off of 10,000 to 500,000. can be organized.

更に、限外濾過法によれば。Furthermore, according to ultrafiltration methods.

培養液中の着色物質も同時に除去できるため、青色度の
低いブリ品を得る利点も伯し−Cいる0−また。
Since colored substances in the culture solution can also be removed at the same time, there is also the advantage of obtaining yellowtail products with low blueness.

使」する限外濾過膜モジュールは、彼処〃11沼・が高
粘性である事を考慮した選択が必要であるが、基本的に
は、平膜、チューブラ−、スパイラル、ホローファイバ
ーのいずれもが期用Li(能である。ただし、ガム濃篤
が比較的高くなると粘度も急激に上昇し1通俄に比較的
高い圧力を必要とする事から、平膜、チューブラ−の使
用4が好ましい。
The ultrafiltration membrane module to be used must be selected taking into consideration the high viscosity of these membranes, but basically flat membrane, tubular, spiral, and hollow fiber are all suitable. However, when the gum density becomes relatively high, the viscosity increases rapidly and a relatively high pressure is required for one batch, so it is preferable to use a flat membrane or a tubular membrane.

次に、脱塩された培養液の乾燥方法としては。Next, how to dry the desalted culture solution.

真空乾燥、ドラム乾燥、スプレー乾燥、熱風乾・栗等、
効案良く乾燥できる方法ならすべて適月可能である。
Vacuum drying, drum drying, spray drying, hot air drying, chestnuts, etc.
Any method that can dry effectively can be used in any suitable month.

以上記載のように9本発明は、あらゆる培育方法によっ
て得られたキサンタンガム培養液を、限外濾過膜を用い
た方法などにより脱環、脱色し。
As described above, in the present invention, a xanthan gum culture solution obtained by any cultivation method is decyclized and decolorized by a method using an ultrafiltration membrane or the like.

これを直接乾燥する事を特畝とした。キサンタンガムの
製造方法であり1本発明により、従来の培養液を直接乾
燥して得られたキサンタンガム製品の重信を大幅に改善
し、アルコール精製法でイ4)られるキサンタンガムと
同等の品′員のキサンタンガム製品を、きわめて容易か
つ工業的にM利な手段でイhる事が1丁能となった□ 以下実施例をあげて説明するが1本発明はかかる実施例
のみに限定されるものではない。
The special feature was to dry this directly. This is a method for producing xanthan gum.1 The present invention greatly improves the reliability of xanthan gum products obtained by directly drying a conventional culture solution, and produces xanthan gum with the same product composition as the xanthan gum produced by the alcohol purification method. It has now become possible to manufacture products using very easy and industrially advantageous means.The following will explain the invention with examples, but the present invention is not limited to these examples. .

実施例 1 ffivコース4 % 、 ヘフ) 70.4 s、 
K、I−IPo、 0゜5%、 Mg80.・711.
o o、 i%、から成る培地18tを801容発酵槽
に入れ、キサントモナス カンペストリス(IFO−1
8551由米株)のa14培養液を接種し、pH7,3
0℃に24日間通気攪拌培養を行った。培養液中の無機
塩の濃度は対キサンタンガム10%であった。この培養
fA5/、1l)IAI”LOPMIO直径150m、
平膜タイプ(Amlcon社製)の限外濾過膜を取り付
けた限外bs過装置により、無機塩濃度がガムrC対し
、1%になるまで脱塩した。次に、このガム濃度が約2
.5係の脱塩された培養液を、高粘度Mlノズルを装着
l−たスプレードライヤーにより噴霧乾燥し、キ1ノー
ンタンガム製品粉末180fをイ■たり一方、脱塩を行
わない培養液5tをその捷ま直接スプレー乾燥したもの
をコントロール−(5)1回シ<培養液5tにインプロ
パツール106′(t7 添加し、生成したキサンタン
ガムの沈澱を回収し、(15wt%イソプロパツール水
溶液で洗滌したのら。
Example 1 ffiv course 4%, Hef) 70.4 s,
K, I-IPo, 0°5%, Mg80.・711.
18 t of a medium consisting of o.
8551 Yume strain) was inoculated, and the pH was adjusted to 7.3.
Aeration and agitation culture was performed at 0°C for 24 days. The concentration of inorganic salt in the culture solution was 10% relative to xanthan gum. This culture fA5/, 1l) IAI”LOPMIO diameter 150 m,
Desalting was carried out using an ultraBS filtration device equipped with a flat membrane type (manufactured by Amlcon) ultrafiltration membrane until the inorganic salt concentration was 1% based on the gum rC. Next, this gum concentration is about 2
.. The desalted culture solution in Section 5 was spray-dried using a spray dryer equipped with a high-viscosity Ml nozzle, and 180 f of Kinone Tan gum product powder was spray-dried. Direct spray drying was used as a control. and others.

これ全真空乾燥して得られたキサンタンガノ^製品をコ
ントロール−(ハ)とし1本発明の方法によって得られ
たキサンタンガム製品と品質の比+9を行ったり (測定は13型粘度計を用’I’+ 3 Or−p、I
n、 。
The xanthan gum product obtained by complete vacuum drying was used as a control (c) and the quality ratio of the xanthan gum product obtained by the method of the present invention was +9. '+ 3 Or-p, I
n.

25℃で行ったO) 第1表に示したように1本発明の方法によって得られた
製品は、従来の培養液を直接乾燥してイ閂tられた製品
の品質に比較して、大幅に改善きtしており、アルコー
ル精製により得られた製品とFi ?!同等の品質をM
していた0 実施例 2 ゲルコール2%、ペプトン0.2%、 K2HP0.0
゜5%2MgSO4・71(,00,1%から成る培地
を用い。
As shown in Table 1, the quality of the product obtained by the method of the present invention was significantly lower than that of the product obtained by directly drying the conventional culture solution. The products obtained by alcohol purification and Fi? ! Same quality M
Example 2 Gelcol 2%, peptone 0.2%, K2HP 0.0
A medium consisting of 5% 2MgSO4.71 (,00,1%) was used.

1(10tg発酵槽を用いて希釈率0. l Ohr 
で直続培養を行い、排出される培養液(無機塩の濃度は
対キサンタンガム約10係)を連続的にチー、−ブラー
タイプ限外濾過膜L(F M(Abcor社製9分社製
9置 ガム質に対し無機塩の量が05%になる寸で脱塩した培
養液50t(ガム濃度約5%)をドラム(晶度を1’2
0℃に調整したドラムドライヤーにより乾燥し,キサン
タンガム製品2.5Kfを得た^一方.連続培養によっ
て得られたキサンタンガム培養沿を用いて,実施例IK
記載した方法で。
1 (dilution rate 0.l Ohr using 10tg fermenter)
The culture solution (concentration of inorganic salts is about 10 parts xanthan gum) was continuously cultured using a Qi-Blur type ultrafiltration membrane L (FM (Abcor, 9 parts). 50 tons of culture solution (gum concentration approximately 5%) that has been desalinated to the point where the amount of inorganic salt is 0.5% of the gum quality is placed in a drum (with a crystallinity of 1'2).
It was dried using a drum dryer adjusted to 0°C to obtain a xanthan gum product of 2.5Kf. Using xanthan gum culture obtained by continuous culture, Example IK
in the manner described.

コントロール(4)(但し,乾燥frtドラム乾イ!V
り及びコントロール0を調製した。
Control (4) (However, dry frt drum dry!V
Control 0 and control 0 were prepared.

図−1に,各調製方法によりイ(+られたキサンタンガ
ムの溶液濃度とみかけ粘度の関係を示し,比較した。各
キサンタンガム溶液に食塩を1%添加したものにつきB
型粘度計を用い8Or.μ+n 25“Cの条件で測定
した。本発明の方法によって111られた製品は,アル
コール精製法によって得られたものとtlぼ同等の粘度
全示し,従来の培養液を直した。
Figure 1 shows and compares the relationship between the solution concentration and apparent viscosity of xanthan gum prepared by each preparation method.
8 Or. using a type viscometer. Measurements were made under the conditions of .mu.+n 25"C. The product obtained by the method of the present invention had a viscosity almost the same as that obtained by the alcohol purification method, and the conventional culture solution was modified.

【図面の簡単な説明】[Brief explanation of drawings]

第1図は実施例20本発明方法及び本発明以外の方法に
よって得たキサンタンガム溶液の粘度特性を示す。 特許出,1.10八 株式会社 典人 +辣桶′正( 2 (v5明9,ン、不丁・ ヤYンタ/ガ2・の駁痔方鵡 、t 、ria正をすb九 斗4f乙の岡a・、 者財Δ1犀す人 +p山’,B/1 j千tit l:!1曲−一一シー
FIG. 1 shows the viscosity characteristics of xanthan gum solutions obtained by the method of the present invention and a method other than the present invention in Example 20. Patent issued, 1.108 Co., Ltd. 4f Otsu no Oka a・, person wealth Δ1 rhinoceros + p mountain', B/1 j thousand tit l:! 1 song - 11 sea +

Claims (1)

【特許請求の範囲】 (1) 炭素、窒素1%機塩類から成る栄饗培地で。 キチ7トモナス嘴細iINを培養する事によって得られ
たキサンタンガムをき有する培養液を。 無機塩類の濃度がキサンタンガムに対し5%以下となる
まで脱塩し、この脱塩された培喪液をそのまま乾燥する
事を/!+、lr徴としたキサンタンガムの製造方法。 (2)・I!11.機地類の濃度がキサンタンガムに対
し2係以下となるまで脱塩する事を特徴とする特許請求
範囲第1項制戦のキサンタンガムの製造方法。 (8)脱塩方法が限外濾過膜を/Llいた限外濾過法で
ある小を特徴とする特許請求師、囲yA1項記載のキサ
ンタンガムの製造方法。
[Claims] (1) Eikai medium consisting of 1% carbon and nitrogen salts. A culture solution containing xanthan gum obtained by culturing Kichi7 Tomonas beak iIN. Desalt until the concentration of inorganic salts is less than 5% of the xanthan gum, and then dry the desalted culture solution as it is. A method for producing xanthan gum with + and lr characteristics. (2)・I! 11. 1. A method for producing xanthan gum according to claim 1, characterized in that desalination is carried out until the concentration of minerals becomes less than 2 times the concentration of xanthan gum. (8) The method for producing xanthan gum according to claimant, box yA1, characterized in that the desalting method is an ultrafiltration method using an ultrafiltration membrane.
JP17057083A 1983-09-17 1983-09-17 Preparation of xanthan gum Granted JPS6062996A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP17057083A JPS6062996A (en) 1983-09-17 1983-09-17 Preparation of xanthan gum

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP17057083A JPS6062996A (en) 1983-09-17 1983-09-17 Preparation of xanthan gum

Publications (2)

Publication Number Publication Date
JPS6062996A true JPS6062996A (en) 1985-04-11
JPS6111596B2 JPS6111596B2 (en) 1986-04-03

Family

ID=15907281

Family Applications (1)

Application Number Title Priority Date Filing Date
JP17057083A Granted JPS6062996A (en) 1983-09-17 1983-09-17 Preparation of xanthan gum

Country Status (1)

Country Link
JP (1) JPS6062996A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR2621926A1 (en) * 1987-10-20 1989-04-21 Inst Francais Du Petrole PROCESS FOR TREATING A FERMENTATION MOUT CONTAINING A POLYSACCHARIDE FOR THE PURPOSE OF INCREASING FILTRABILITY AND USE OF SUCH ASSISTED OIL RECOVERY MILL
EP0621040A3 (en) * 1993-04-23 1995-01-18 Shinetsu Chemical Co Method for reducing the number of contaminative live bacteria in xanthan gum.

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0577091U (en) * 1992-03-30 1993-10-19 日立化成工業株式会社 Manhole for septic tank

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR2621926A1 (en) * 1987-10-20 1989-04-21 Inst Francais Du Petrole PROCESS FOR TREATING A FERMENTATION MOUT CONTAINING A POLYSACCHARIDE FOR THE PURPOSE OF INCREASING FILTRABILITY AND USE OF SUCH ASSISTED OIL RECOVERY MILL
EP0621040A3 (en) * 1993-04-23 1995-01-18 Shinetsu Chemical Co Method for reducing the number of contaminative live bacteria in xanthan gum.
US5493015A (en) * 1993-04-23 1996-02-20 Shin-Etsu Chemical Co. Ltd. Method for reducing contaminative live bacteria in xanthan gum

Also Published As

Publication number Publication date
JPS6111596B2 (en) 1986-04-03

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