JPS5886090A - Separation of dicarboxylic acid - Google Patents

Separation of dicarboxylic acid

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Publication number
JPS5886090A
JPS5886090A JP18311181A JP18311181A JPS5886090A JP S5886090 A JPS5886090 A JP S5886090A JP 18311181 A JP18311181 A JP 18311181A JP 18311181 A JP18311181 A JP 18311181A JP S5886090 A JPS5886090 A JP S5886090A
Authority
JP
Japan
Prior art keywords
acid
dicarboxylic acid
alcohol
fermentation liquid
fermentation
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
JP18311181A
Other languages
Japanese (ja)
Inventor
Toshiro Furukawa
古川 敏郎
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.)
Mitsui Petrochemical Industries Ltd
Original Assignee
Mitsui Petrochemical Industries 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 Mitsui Petrochemical Industries Ltd filed Critical Mitsui Petrochemical Industries Ltd
Priority to JP18311181A priority Critical patent/JPS5886090A/en
Publication of JPS5886090A publication Critical patent/JPS5886090A/en
Pending legal-status Critical Current

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

Abstract

PURPOSE:To recover a dicarboxylic acid, economically, in high efficiency, from a fermentation liquid containing the dicarboxylic acid as a salt, by removing the microbial cells from the liquid, treating the liquid with a strong acid, and extracting the objective compound with an alicyclic alcohol and/or an aromatic alcohol. CONSTITUTION:Microbial cells are removed from the fermentation liquid containing a dicarboxylic acid as a salt and obtained by conventional process, and the pH of the residual fermentation liquid is adjusted to <=4.0, preferably <= 3.0 with a strong acid such as sulfuric acid, hydrochloric acid, etc. to precipitate the free dicarboxylic acid. The dicarboxylic acid is extracted with an alicyclic alcohol and/or an aromatic alcohol such as cyclohexanol, benzyl alcohol, etc. The amount of the extractant should be sufficiently large to form two layers with the fermentation liquid. If necessary, the extracted liquid is brought into contact with an aqueous solution of an alkali to extract the dicarboxylic acid with the solution, and the dicarboxylic acid is precipitated by treating the extract with a strong acid.

Description

【発明の詳細な説明】 本発明はジカルボン酸の精製方法に関する。[Detailed description of the invention] The present invention relates to a method for purifying dicarboxylic acids.

更に詳しくは、本発明は発酵法により製造されたジカル
ボン酸の精製方法に関する。
More specifically, the present invention relates to a method for purifying dicarboxylic acids produced by fermentation.

近年n−パラフィンを原料とし、微生物発酵によりジカ
ルボン酸を製造することが試みられている。一般に発酵
法により製造されるジカルボン酸を発酵液から分離精製
するには、発酵液から菌体を除去した後(1)カルシウ
ム塩などの不溶性の金属塩として析出させる方法、(2
)エーテルで抽出した後、溶媒を溜去する方法、(6)
アルカリ金属塩および可溶性無機金属塩を添加してジア
ルカリ金属塩として塩析させる方法、(4)酸f添加し
て酸析させる方法などが知られている。これらの方法の
うちで、は酸析法が処理工程が簡易なため、有利なよう
に考えられるが、実際には、発酵原料であるn−’パラ
フィンあるいは発酵液中の蛋白質などの影響で酸析によ
り析出した結晶が鱗片状かつ微結晶になり、p過分離の
際の水切れ効率が著しく劣り、工業化上問題となる。酸
析後、加熱すれば結晶の成長を促すことができるが、一
般に発酵液中のジカルボン酸濃度は、例えば3ないし6
%の如く非′Kに低いために、このような発酵液を加熱
するには多大のエネルギーを要し、経済的とはいえない
In recent years, attempts have been made to produce dicarboxylic acids by microbial fermentation using n-paraffin as a raw material. In general, in order to separate and purify dicarboxylic acids produced by fermentation methods from fermentation liquor, there are two methods: (1) removing bacterial cells from fermentation liquor and then precipitating them as insoluble metal salts such as calcium salts;
) A method of distilling off the solvent after extraction with ether, (6)
Known methods include adding an alkali metal salt and a soluble inorganic metal salt to cause salting out as a dialkali metal salt, and (4) adding acid f to cause acid precipitation. Among these methods, the acid precipitation method is considered to be advantageous because the treatment process is simple, but in reality, acid precipitation may occur due to the influence of n-' paraffin, which is a fermentation raw material, or proteins in the fermentation liquid. The crystals precipitated by the analysis become scaly and microcrystalline, resulting in extremely poor water removal efficiency during P over-separation, which poses a problem in terms of industrialization. After acid precipitation, crystal growth can be promoted by heating, but generally the dicarboxylic acid concentration in the fermentation liquid is, for example, 3 to 6.
%, heating such a fermentation liquid requires a large amount of energy and is not economical.

また酸析したジカルボン酸を芳香族炭化水素に溶解抽出
して醗酵液と分離する方法はあるが、室温近辺における
芳香族炭化水素に対する溶解度が充分に大きくないため
、矢張75°C以上に加熱しなければ効率良く抽出を行
うことができないという難点がある。
There is also a method of dissolving and extracting the acid-precipitated dicarboxylic acid in aromatic hydrocarbons to separate it from the fermentation liquid, but since the solubility of aromatic hydrocarbons at around room temperature is not high enough, it is necessary to heat the dicarboxylic acid to temperatures above 75°C. Otherwise, there is a drawback that extraction cannot be performed efficiently.

本発明者らは、上記の如き高温加熱操作が必要でなく、
一層簡単な方法で発酵液からジカルボン酸を単離する方
法を検討した結果、以下の方法を見出すに至った。すな
わち本発明は、発酵法によりジカルボン酸を製造する方
法において、ジカルボン酸を塩として含有する発酵液か
らジカルボン酸を分離取得するにあたり、予め菌体を分
離した発酵液に強酸を作用させてジカルボン酸を遊離さ
せ、該遊離したジカルボン酸を前記発酵液と2層を形成
するに充分な量の脂環族アルコールおよびまたは芳香族
アルコール中に抽出させ、該抽出した脂環族アルコール
およびまたは芳香族アルコール層からジカルボン酸を回
収することを特徴とするジカルボン酸の分離方法である
The present inventors discovered that the above-mentioned high-temperature heating operation is not necessary;
As a result of investigating a simpler method for isolating dicarboxylic acids from fermentation broth, the following method was discovered. That is, the present invention provides a method for producing dicarboxylic acid by fermentation, in which dicarboxylic acid is separated and obtained from a fermentation broth containing dicarboxylic acid as a salt by applying a strong acid to the fermentation broth from which bacterial cells have been separated in advance. is released, the liberated dicarboxylic acid is extracted into a sufficient amount of alicyclic alcohol and/or aromatic alcohol to form two layers with the fermentation liquid, and the extracted alicyclic alcohol and/or aromatic alcohol is This is a dicarboxylic acid separation method characterized by recovering dicarboxylic acid from a layer.

本発明は、発酵法によりジカルボンr11を製造する方
法において、ジカルボン酸を塩として含有する発酵液を
原料とするものである。このような発酵液を得る手段は
すでに公知である。すなわち種々の次素源とジカルボン
酸を生成し得る微生物とを用いて好気的に発酵させるも
のであるが、発酵時のP、H調整の目的で添加された塩
基性化合物によって、ジカルボン酸は塩として得られる
The present invention is a method for producing dicarboxylic acid r11 by a fermentation method, in which a fermentation liquid containing dicarboxylic acid as a salt is used as a raw material. Means for obtaining such a fermentation liquid are already known. In other words, it is aerobic fermentation using various secondary element sources and microorganisms that can produce dicarboxylic acids, but dicarboxylic acids are produced by basic compounds added for the purpose of adjusting P and H during fermentation. Obtained as salt.

上記ジカルボン酸としては、例えばスペリン酸、アゼラ
イン酸、セバシン酸、1,9−ノナンジカルボン酸、1
.10−デカンジカルボン酸、ブラシル酸、1.12−
ドデカンジカルボン酸、1,13−トリデカンジカルボ
ン酸、タブシン酸などを挙げることができる。これらの
うちでは、とくに炭素数10以上の脂肪族ジカルボン酸
に対して効果的である。
Examples of the dicarboxylic acids include speric acid, azelaic acid, sebacic acid, 1,9-nonanedicarboxylic acid,
.. 10-decanedicarboxylic acid, brassylic acid, 1.12-
Examples include dodecanedicarboxylic acid, 1,13-tridecanedicarboxylic acid, tabsic acid, and the like. Among these, it is particularly effective for aliphatic dicarboxylic acids having 10 or more carbon atoms.

前記の如きジカルボン酸を微生物による発酵法で製造す
る際の原料としては、好適にはn−パラフィンあるいは
これを含有する炭化水素、とくに好適には、目的とする
ジカルボン酸と同一の炭素数のn−パラフィンを選択す
るのがよい。
The raw material for producing the above dicarboxylic acid by microbial fermentation is preferably n-paraffin or a hydrocarbon containing it, particularly preferably n-paraffin having the same number of carbon atoms as the target dicarboxylic acid. - Paraffin is a good choice.

このようなn−パラフィンからジカルボン酸を製造しう
る微生物としては、例えば特開昭49−25186号に
記載されているようにジカルボン酸を生産する能力を有
するトルロプシス属に属する酵母、あるいはキャンデイ
ダ属に属する酵母等が知られている。
Examples of microorganisms that can produce dicarboxylic acid from n-paraffin include yeast belonging to the genus Torulopsis, which has the ability to produce dicarboxylic acid, as described in JP-A No. 49-25186, or yeast belonging to the genus Candida. The yeasts belonging to this species are known.

本発明の方法につき工程を迫って説明する。本発明では
、まず発酵液から微生物菌体を除去する。
The process of the method of the present invention will be explained in detail. In the present invention, first, microbial cells are removed from the fermentation liquid.

ジカルボン酸は、発酵時にPH調整のため添加されたア
ルカリ金属水酸化物などにより、発酵液中にアルカリ金
属塩などとして溶解しているため、発酵液を濾過もしく
は遠心分離することにより菌体を分離することができる
Dicarboxylic acids are dissolved as alkali metal salts in the fermentation liquid due to alkali metal hydroxides added to adjust the pH during fermentation, so bacterial cells can be separated by filtering or centrifuging the fermentation liquid. can do.

次に本発明では、菌体を分離した発酵液に強酸、例えば
無機酸を作用させて好ましくはPH4,0以下程度とし
、遊離のジカルボン酸を析出させる0この酸析に用いる
ことのできる無機酸としては、硫酸、塩酸、硝酸等を挙
げることができる。これらの無機酸は通常水溶液として
用いられる。酸析の際のPHは少なくとも4.0以下、
好ましくは6.0以下であることが望ましく、PHの小
さい程ジカルボン酸の収率が向上する。
Next, in the present invention, a strong acid, such as an inorganic acid, is applied to the fermentation liquid from which the bacterial cells have been separated, preferably to a pH of about 4.0 or below, to precipitate free dicarboxylic acids.An inorganic acid that can be used for this acid precipitation Examples include sulfuric acid, hydrochloric acid, and nitric acid. These inorganic acids are usually used as an aqueous solution. The pH during acid precipitation is at least 4.0 or less,
The pH value is preferably 6.0 or less, and the smaller the pH, the higher the yield of dicarboxylic acid.

ジカルボン酸を酸析した発酵液は、この発酵液と2層を
形成するに充分な鷲の脂環族アルコールおよびまたは芳
香族アルコールと接触させ、ジカルボン酸をアルコール
層に抽出させる。勿論、前記アルコールは、酸析の前に
発酵液と接触させておき、酸析を行いつつ抽出を行う方
法を採用してもよい。この目的に使用できるアルコール
としてハ、シフ)ロペンタノール、シクロヘキサノール
などの脂環族アルコール、ベンジルアルコール、メチル
ベンジルアルコールなどの芳香族アルコールを例示する
ことができる。抽出に使用されるアルコールの量は、発
酵液と2層を形成するに充分な量であって、しかもあま
り多量に用いない方が好ましく、通常発酵液10容量部
に対し、6ないし4容量部程度とするのが好ましい。前
記アルコールはまた水不溶蘇の他の溶媒、例えば炭化水
素類と併用してもよい。
The fermented liquor in which the dicarboxylic acid has been precipitated is brought into contact with enough alicyclic alcohol and/or aromatic alcohol to form two layers with the fermented liquor, and the dicarboxylic acid is extracted into the alcohol layer. Of course, a method may be adopted in which the alcohol is brought into contact with the fermentation liquid before acid precipitation, and extraction is performed while acid precipitation is performed. Examples of alcohols that can be used for this purpose include alicyclic alcohols such as Lopentanol and cyclohexanol, and aromatic alcohols such as benzyl alcohol and methylbenzyl alcohol. The amount of alcohol used for extraction is sufficient to form two layers with the fermentation liquid, and it is preferable not to use too much alcohol, usually 6 to 4 parts by volume per 10 parts by volume of the fermentation liquid. It is preferable to set it as approximately. The alcohol may also be used in combination with other water-insoluble solvents, such as hydrocarbons.

抽出操作は、回分式あるいは連続式で、例えば並流式、
向流式などの方式によって行うことができる。
The extraction operation can be carried out batchwise or continuously, such as parallel flow,
This can be done by a method such as a countercurrent method.

ジカルボン酸を抽′出したアルコール層は、例えば静置
等により水層と分離してから、ジカルボン酸の回収に供
される。ジカルボン酸を回収するにあたっては、単に濃
縮11冷却によってジカルボン′酸を晶析させそもよく
、あるいは少量のアルカリ水溶液と接触させ、ジカルボ
ン酸をアルカリ塩として該アルカリ水溶液層に抽出させ
た後、該アルカリ−水溶液層を分離し、さらに強酸を接
触させて、ジカルボン酸の結晶を晶析させてもよい。後
者の方法においては、アルカリ水溶液としてアルコール
の1/3〜1/2程度の容量の使用で充分であるから、
元の発酵液中の濃度に比較して高濃度のジカルボン酸塩
の溶液か得られることになり、取扱う液量も少なくて済
み、装置、設備用役などの面において有利である。
The alcohol layer from which the dicarboxylic acid has been extracted is separated from the aqueous layer by, for example, standing still, and then used to recover the dicarboxylic acid. In recovering the dicarboxylic acid, the dicarboxylic acid may be simply crystallized by concentration (11) and cooling, or the dicarboxylic acid may be brought into contact with a small amount of aqueous alkali solution, and the dicarboxylic acid is extracted as an alkali salt into the aqueous alkali layer. The alkali-aqueous solution layer may be separated and further brought into contact with a strong acid to crystallize dicarboxylic acid crystals. In the latter method, it is sufficient to use the alkaline aqueous solution in a volume of about 1/3 to 1/2 of the alcohol;
A solution of the dicarboxylic acid salt with a higher concentration than that in the original fermentation liquid can be obtained, and the amount of liquid to be handled can be reduced, which is advantageous in terms of equipment and equipment usage.

次に実施例を挙げて具体的に説明する。Next, a concrete explanation will be given with reference to examples.

実施例1 n−)リゾカンを原料にトルロプシス・キャンディダを
培養して生産したブラシル酸を含む培養物から菌体を除
去した。次にこの上澄液500m1(ブラシル酸を10
.5 g含んでいる)を底部抜取口付き11フラスコに
仕込み、塩酸水溶液を加えPH3,5とし、ブラシル酸
を酸析した。次にジークロへキサノール1som/を加
え50℃に加熱し、攪拌後静置し、分離した2相のうち
水相を除去した。
Example 1 n-) Bacterial cells were removed from a culture containing brassylic acid produced by culturing Torulopsis candida using Rhizocane as a raw material. Next, 500 ml of this supernatant liquid (brassyl acid
.. (containing 5 g) was placed in a No. 11 flask with a bottom outlet, and an aqueous hydrochloric acid solution was added to adjust the pH to 3.5 to precipitate brassylic acid. Next, 1 som/dichlorohexanol was added and heated to 50° C., stirred and left to stand, and among the two separated phases, the aqueous phase was removed.

シクロヘキサノール相を減圧濃縮し、約130〜140
rJのシクロヘキサノールを濡出させた後、冷却し、ブ
ラシル酸を析出させた。そして吸引濾過  −し、乾燥
して9.3gのブラシル酸の結晶を得た。
The cyclohexanol phase was concentrated under reduced pressure, and the
After wetting out rJ cyclohexanol, it was cooled to precipitate brassylic acid. The mixture was filtered with suction and dried to obtain 9.3 g of brassylic acid crystals.

実施例2 実施例1と同じ装置を用い、培養液5oort+#(ブ
ラシル酸10.5 g 7含む)を同様に酸析し、15
0m#のシクロヘキサノールを加え攪拌抽出する。
Example 2 Using the same apparatus as in Example 1, a culture solution of 5 oort+# (containing 10.5 g of brassylic acid 7) was acid-precipitated in the same manner, and
Add 0 m# of cyclohexanol and stir to extract.

水相を除去した後5N水酸化す) IJウム液IClO
mI!を加え攪拌し水酸化ナトリウムの水相ヘプラシル
酸を淘解させた。次いで塩酸でPH3にして、ブラシル
酸を酸析し回収して9.1gのブラシル酸をえた。
After removing the aqueous phase, 5N hydroxide) IJum solution IClO
mI! was added and stirred to dissolve the heprasylic acid in the aqueous phase of sodium hydroxide. Next, the pH was adjusted to 3 with hydrochloric acid, and brassylic acid was precipitated and recovered to obtain 9.1 g of brassylic acid.

実施例3 実施例1と同じ装置を用い、培養液500m+7/(ブ
ラシル酸19gを含む)を同様に酸析し、400m7?
のベンジルアルコールを加えろ0°Cに加熱し攪拌して
ブラシル酸をベンジルアルコール層へ抽出した。ベンジ
ルアルコール層を分離し5°Cに冷却し、−過後、n−
ヘキサンで洗浄、乾燥して14gのブラシル酸をえた。
Example 3 Using the same apparatus as in Example 1, 500 m+7/(containing 19 g of brassylic acid) of the culture solution was acid-precipitated in the same manner, and 400 m7?
The mixture was heated to 0°C and stirred to extract brassylic acid into the benzyl alcohol layer. The benzyl alcohol layer was separated, cooled to 5°C, and after filtration, n-
Washing with hexane and drying yielded 14 g of brassylic acid.

このブラシル酸中の蛋白質の含量は500 ppmであ
った。
The protein content in this brassylic acid was 500 ppm.

これと同じ培養液を酸析してえたブラシル酸には3,0
00ppmの蛋白質が含まれていた。従って拳法はブラ
シル酸から蛋白を除去する効果が著しいことが明らかに
なった。
Brassylic acid obtained by acid precipitation of the same culture solution has 3,0
It contained 00 ppm of protein. Therefore, it has become clear that Kenpo has a remarkable effect on removing protein from brassylic acid.

実施例4 ブラシル酸の代わりにセバシン酸23 g/ffを含む
培養物を用いた以外は、実施例1と同じ装置を用い、同
様の操作を行って、11.5gのセバシン酸を含む培養
液5’00meから1肌3gのセバシン酸を分離回収し
た。
Example 4 The same apparatus as in Example 1 was used, except that a culture containing 23 g/ff of sebacic acid was used instead of brassylic acid, and the same operation was performed to prepare a culture solution containing 11.5 g of sebacic acid. 3 g of sebacic acid per skin was separated and recovered from 5'00me.

出願人  三井石油化学工業株式会社 代理人  山  口     和Applicant: Mitsui Petrochemical Industries, Ltd. Agent Kazu Yamaguchi

Claims (1)

【特許請求の範囲】 (リ 発酵法によりジカルボン酸を製造する方法におい
て、ジカルボン酸を塩として含有する発酵液からジカル
ボン酸を分離取得するにあたり予め菌体を分離した発酵
液に強酸を作用させてジカルボン酸を遊離させ、該遊離
したジカルボン酸を前記発酵液と2層を形成するに充分
な量の脂環族アルコールおよびまたは芳。 香族アルコール中に抽出させ、該抽出した゛脂/ 環族アルコールおよびまたは芳香族アルコール層からジ
カルボン酸を回収することを特徴とするジカルボン酸の
分離方法。 (2)脂環族アルコールおよびまたは芳香族アルコール
層からジカルボン酸を回収するに際し、脂環族アルコー
ルおよびまたは芳香族アルコール溶液とアルカリ水溶液
を接触させてジカルボン酸をアルカリ水溶液に抽出し、
しかる後抽出液に強酸を一作用させてジカルボン酸を析
出させることを特徴とする特許請求の範囲(1)記載の
方法。
[Claims] (Li) In a method for producing dicarboxylic acid by a fermentation method, in order to separate and obtain dicarboxylic acid from a fermentation liquid containing dicarboxylic acid as a salt, a strong acid is applied to the fermentation liquid from which bacterial cells have been separated in advance. An alicyclic alcohol and/or aromatic in an amount sufficient to liberate a dicarboxylic acid and form a two-layered layer with the liberated dicarboxylic acid with the fermentation liquid. A method for separating dicarboxylic acid characterized by recovering dicarboxylic acid from an alcohol and/or aromatic alcohol layer. (2) When recovering dicarboxylic acid from an alicyclic alcohol and/or aromatic alcohol layer, alicyclic alcohol and Alternatively, the dicarboxylic acid is extracted into the alkaline aqueous solution by contacting the aromatic alcohol solution and the alkaline aqueous solution,
The method according to claim (1), characterized in that the extract is then treated with a strong acid to precipitate the dicarboxylic acid.
JP18311181A 1981-11-17 1981-11-17 Separation of dicarboxylic acid Pending JPS5886090A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP18311181A JPS5886090A (en) 1981-11-17 1981-11-17 Separation of dicarboxylic acid

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP18311181A JPS5886090A (en) 1981-11-17 1981-11-17 Separation of dicarboxylic acid

Publications (1)

Publication Number Publication Date
JPS5886090A true JPS5886090A (en) 1983-05-23

Family

ID=16129961

Family Applications (1)

Application Number Title Priority Date Filing Date
JP18311181A Pending JPS5886090A (en) 1981-11-17 1981-11-17 Separation of dicarboxylic acid

Country Status (1)

Country Link
JP (1) JPS5886090A (en)

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102476990A (en) * 2010-11-29 2012-05-30 中国石油化工股份有限公司 Method for extracting and refining long-chain dicarboxylic acid crude product
CN102617320A (en) * 2012-02-08 2012-08-01 上海凯赛生物技术研发中心有限公司 Method for treating reaction solution containing long chain dicarboxylate
CN103242156A (en) * 2012-02-08 2013-08-14 上海凯赛生物技术研发中心有限公司 Method for treating a reaction solution containing a long-chain dicarboxylate
CN103804174A (en) * 2012-11-08 2014-05-21 中国石油化工股份有限公司 Organic acid refining method
CN105074000A (en) * 2013-04-01 2015-11-18 Cj第一制糖株式会社 Method for purifying quinolinic acid

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102476990A (en) * 2010-11-29 2012-05-30 中国石油化工股份有限公司 Method for extracting and refining long-chain dicarboxylic acid crude product
CN102617320A (en) * 2012-02-08 2012-08-01 上海凯赛生物技术研发中心有限公司 Method for treating reaction solution containing long chain dicarboxylate
CN103242156A (en) * 2012-02-08 2013-08-14 上海凯赛生物技术研发中心有限公司 Method for treating a reaction solution containing a long-chain dicarboxylate
CN103804174A (en) * 2012-11-08 2014-05-21 中国石油化工股份有限公司 Organic acid refining method
CN105074000A (en) * 2013-04-01 2015-11-18 Cj第一制糖株式会社 Method for purifying quinolinic acid
EP2982759A4 (en) * 2013-04-01 2016-08-24 Cj Cheiljedang Corp Method for purifying quinolinic acid
CN105074000B (en) * 2013-04-01 2018-12-21 Cj第一制糖株式会社 The method for refining quinolinic acid

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