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JPH033720B2 - - Google Patents
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JPH033720B2 - - Google Patents

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Publication number
JPH033720B2
JPH033720B2 JP18555382A JP18555382A JPH033720B2 JP H033720 B2 JPH033720 B2 JP H033720B2 JP 18555382 A JP18555382 A JP 18555382A JP 18555382 A JP18555382 A JP 18555382A JP H033720 B2 JPH033720 B2 JP H033720B2
Authority
JP
Japan
Prior art keywords
amphoteric surfactant
carbon atoms
alcohol
phase
amphoteric
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
Application number
JP18555382A
Other languages
Japanese (ja)
Other versions
JPS5975998A (en
Inventor
Takeshi Myoshi
Hiromi Mitsutake
Isamu Ueno
Hiroshi Yokota
Arahiko Eguchi
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.)
Ajinomoto Co Inc
Original Assignee
Ajinomoto Co Inc
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 Ajinomoto Co Inc filed Critical Ajinomoto Co Inc
Priority to JP18555382A priority Critical patent/JPS5975998A/en
Publication of JPS5975998A publication Critical patent/JPS5975998A/en
Publication of JPH033720B2 publication Critical patent/JPH033720B2/ja
Granted legal-status Critical Current

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Description

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

本発明は両性界面活性剤の精製法に関するもの
である。 両性界面活性剤は一般に皮膚や眼に対する刺激
が温和であり、広範囲のPH域で使用できる等の利
点を有しているが、通常製造由来の塩化ナトリウ
ム、硫酸ナトリウム等の無機塩類の混入が避けら
れず、そのため、特にシヤンプー等の洗浄剤組成
物に於いて以下の問題点がしばしば生じることが
ある。即ち、無機塩類の影響により、低温安定
性が低下する、所定の粘度が安定して得られな
い、乳化破壊が起る等の障害が発生し易いた
め、両性界面活性剤の使用が著しく制限されてい
る。塩類を含まない両性界面活性剤の出現が従来
から要望されてきたが、両性界面活性剤は分子中
に陰イオンと陽イオンに荷電するため、陰イオン
界面活性剤や陽イオン界面活性剤と異なり、pH
を変動させても安定して水中に在存するため、単
離精製が極めて因難である。実験室的には多量の
有機溶媒を加えて塩類を析出せしめて除去する
か、あるいはイオン交換樹脂を用いて脱塩する方
法が考えられるが、これらはいずれも煩雑かつコ
スト面から不利であり、工業的に到底採用されな
い。 本発明者は両性界面活性剤の精製に関し、簡便
かつ工業的に適用し得る精製法について鋭意検討
した結果、無機塩類を含有する両性界面活性剤水
溶液若しくは懸濁液に水に難溶なアルコール、即
ち炭素数4ないし10の飽和あるいは不飽和のアル
コールを加えて抽出することにより、アルコール
相に脱塩された両性界面活性剤が極めて効率的に
抽出されることを見い出し本発明を完成するに至
つた。 次に本発明を更に詳しく述べるならば、本発明
の精製法に於いて適用可能な無機塩類としては、
Na,K,Ca,Mgなどアルカリ金属、アルカリ
土類金属と塩酸、硫酸、硝酸、燐酸、硼酸との無
機塩類であり、使用されるアルコールは炭素数4
ないし10の飽和あるいは不飽和の脂肪族あるいは
脂環式アルコールであり、例えばブタノール、ペ
ンタノール、ヘキサノール、ヘプタノール、オク
タノール、デカノール、2−エチルヘキサノー
ル、2−エチルオクタノール、シクロペンタノー
ル、シクロヘキサノール等が挙げられる。炭素数
3以下のアルコールでは水に易溶なため水相との
分離が困難となり、他方、炭素数が10を超えるア
ルコールは沸点が高くなりすぎ、また低温時に固
形化するなど、取り扱い上の困難が増大するので
好ましくない。 本発明に供される両性界面活性剤としては両性
界面活性剤であれば、いかなるものも適用される
が、特に下記の両性界面活性剤が好適である。 1 一般式〔〕、〔〕で表わされるN−アシル
−α−アミノ酸型 (但し、式中RCOは炭素数8〜22を有する
脂肪酸残基)。 2 一般式〔〕、〔〕で表わされるカルボキシ
ベタイン型
The present invention relates to a method for purifying amphoteric surfactants. Amphoteric surfactants generally have the advantage of mild irritation to the skin and eyes and can be used in a wide range of pH ranges, but they usually avoid contamination with inorganic salts such as sodium chloride and sodium sulfate derived from manufacturing. As a result, the following problems often occur, especially in detergent compositions such as shampoo. In other words, the use of amphoteric surfactants is severely restricted because problems such as decreased low-temperature stability, inability to stably obtain a desired viscosity, and demulsification breakage occur due to the influence of inorganic salts. ing. There has long been a desire for the emergence of amphoteric surfactants that do not contain salts, but because amphoteric surfactants have anionic and cationic charges in their molecules, they differ from anionic surfactants and cationic surfactants. , pH
Because it remains stable in water even when the temperature is varied, isolation and purification is extremely difficult. In the laboratory, it is possible to remove salts by adding a large amount of organic solvent to precipitate them, or to desalt them using ion exchange resin, but these methods are both complicated and disadvantageous in terms of cost. It will never be adopted industrially. Regarding the purification of amphoteric surfactants, as a result of intensive studies on purification methods that are simple and industrially applicable, the present inventors found that an amphoteric surfactant aqueous solution or suspension containing inorganic salts contains an alcohol that is sparingly soluble in water, That is, they discovered that the desalted amphoteric surfactant can be extracted extremely efficiently by adding a saturated or unsaturated alcohol having 4 to 10 carbon atoms to the alcohol phase, and have completed the present invention. Ivy. Next, to describe the present invention in more detail, inorganic salts that can be used in the purification method of the present invention include:
These are inorganic salts of alkali metals and alkaline earth metals such as Na, K, Ca, and Mg with hydrochloric acid, sulfuric acid, nitric acid, phosphoric acid, and boric acid, and the alcohol used has 4 carbon atoms.
to 10 saturated or unsaturated aliphatic or alicyclic alcohols, such as butanol, pentanol, hexanol, heptanol, octanol, decanol, 2-ethylhexanol, 2-ethyloctanol, cyclopentanol, cyclohexanol, etc. Can be mentioned. Alcohols with less than 3 carbon atoms are easily soluble in water, making it difficult to separate them from the aqueous phase, while alcohols with more than 10 carbon atoms have too high a boiling point and solidify at low temperatures, making them difficult to handle. is undesirable because it increases As the amphoteric surfactant used in the present invention, any amphoteric surfactant can be used, but the following amphoteric surfactants are particularly suitable. 1 N-acyl-α-amino acid type represented by the general formula [], [] (However, in the formula, RCO is a fatty acid residue having 8 to 22 carbon atoms). 2 Carboxybetaine type represented by the general formula [], []

【式】【formula】

【式】 (但し、式中R1は炭素数8〜22のアルキル
基、又はアルケニル基、R2及びR3、R4はそれ
ぞれ炭素数1ないし3のアルキル基) 3 一般式〔〕、〔〕、〔〕、〔〕で表わされ
るイミダゾリン型 (但し、式中R1は約4ないし18のアルキル
基又はアルケニル基、R2は1ないし4のアル
キレン基、R3はR2又はOH基で置換されたアル
キレン基、Mは水素原子、アルカリ金属、又は
アルカノールアミンから誘導されるカチオン、
そしてGはアニオンである) 4 一般式〔〕及び〔〕で表わされるアミド
アミン型 (但し、式中R1は炭素数約8ないし22のア
ルキル基又はアルケニル基、R2は−
CH2COOM又は−CH2CH2COOM、R3は水素、
−CH2COOM又は−CH2CH2COOM、Mは水
溶性塩を形成するカチオン) (但し、式中R1,R2,R3は一般式〔〕の
記号と同一の意味を表わし、R4は水素、−
CH2COOM又は−CH2CH2COOM、Mは一般
式〔〕の記号と同一の意味を表わす) 5 一般式〔XI〕で表わされるアミドベタイン型 (但し、式中RCOは炭素数8ないし22の脂
肪酸残基R1,R2は炭素数1ないし3のアルキ
ル基) 本発明の精製法に関する操作は極めて簡便で通
常の抽出方法を採用すればよい。即ち、両性界面
活性剤及び無機塩を含有する水溶液著しくは懸濁
液に炭素数4ないし10の飽和あるいは不飽和のア
ルコールを加えて充分に撹拌後、分相したのちア
ルコール相を分取して濃縮することにより脱塩さ
れた両性界面活性剤を得ることができる。 両性界面活性剤と無機塩の水溶液あるいは懸濁
液に対する濃度は特に限定されないが、好ましく
は両者合わせて50%以下が良好な結果を与える。
また本発明の両性界面活性剤の精製の確認は分相
させたアルコール相又はアルコール相の濃縮乾固
物の一定量をとり、原子吸光分析より含有する金
属イオンを定量し、無機塩の含有量を求めること
により行うことができる。一方得られた両性界面
活性剤の定量は分相後のアルコール相あるいはア
ルコール相の一定量をとり、高速液体クロマトグ
ラフイーによつて定量するかあるいはアルコール
相の濃縮乾固物の重量と前述の方法によつて定量
された無機塩の重量の差から求めることができ
る。 以下、実施例により具体的に説明する。 実施例 1 両性界面活性剤10gとNaC1 1.0gをとり、これ
に水100ml加えて溶解若しくは懸濁させた後、n
−ブタノール100ml加えて室温にて約3時間撹拌
する。静置、分相させた後、n−ブタノール相を
とり、再び水100ml加えて抽出しn−BuOH相を
減圧下濃縮乾固する。次いで80℃に加温した乾燥
器に入れ、減圧下充分に乾燥する。乾燥した両性
界面活性剤の回収率は高速液体クロマトグラフイ
ーより、また両性界面活性剤中のNaClの含有率
は原子吸光分析より求めた。結果は表1に示す。
[Formula] (However, in the formula, R 1 is an alkyl group having 8 to 22 carbon atoms or an alkenyl group, and R 2 , R 3 , and R 4 are each an alkyl group having 1 to 3 carbon atoms) 3 General formula [], [ Imidazoline type represented by ], [], [] (However, in the formula, R 1 is about 4 to 18 alkyl or alkenyl groups, R 2 is 1 to 4 alkylene groups, R 3 is R 2 or an alkylene group substituted with an OH group, M is a hydrogen atom, an alkali cations derived from metals or alkanolamines;
and G is an anion) 4 Amidamine type represented by general formulas [] and [] (However, in the formula, R 1 is an alkyl group or alkenyl group having about 8 to 22 carbon atoms, and R 2 is -
CH 2 COOM or −CH 2 CH 2 COOM, R 3 is hydrogen,
-CH 2 COOM or -CH 2 CH 2 COOM, M is a cation that forms a water-soluble salt) (However, in the formula, R 1 , R 2 , R 3 have the same meanings as the symbols in the general formula [], R 4 is hydrogen, -
CH 2 COOM or -CH 2 CH 2 COOM, M has the same meaning as the symbol in general formula []) 5 Amidobetaine type represented by general formula [XI] (However, in the formula, RCO is a fatty acid residue having 8 to 22 carbon atoms, R 1 and R 2 are alkyl groups having 1 to 3 carbon atoms.) The purification method of the present invention is extremely simple and can be performed using a conventional extraction method. good. That is, a saturated or unsaturated alcohol having 4 to 10 carbon atoms is added to an aqueous solution containing an amphoteric surfactant and an inorganic salt, especially a suspension, and after thorough stirring, the phases are separated and the alcohol phase is separated. A desalted amphoteric surfactant can be obtained by concentration. The concentrations of the amphoteric surfactant and the inorganic salt in the aqueous solution or suspension are not particularly limited, but preferably a total of 50% or less gives good results.
In addition, to confirm the purification of the amphoteric surfactant of the present invention, take a certain amount of the phase-separated alcohol phase or concentrated dry product of the alcohol phase, quantify the metal ions contained by atomic absorption spectrometry, and check the inorganic salt content. This can be done by finding . On the other hand, the obtained amphoteric surfactant can be quantified by taking the alcohol phase after phase separation or by taking a certain amount of the alcohol phase and quantifying it by high performance liquid chromatography, or by combining the weight of the concentrated dry product of the alcohol phase with the above-mentioned method. It can be determined from the difference in the weight of the inorganic salt determined by the method. Hereinafter, this will be explained in detail using examples. Example 1 Take 10 g of amphoteric surfactant and 1.0 g of NaC1, add 100 ml of water to dissolve or suspend it, and then
- Add 100 ml of butanol and stir at room temperature for about 3 hours. After standing and phase separation, the n-butanol phase was taken, and 100 ml of water was added again for extraction, and the n-BuOH phase was concentrated to dryness under reduced pressure. Then, it is placed in a dryer heated to 80°C and thoroughly dried under reduced pressure. The recovery rate of the dried amphoteric surfactant was determined by high performance liquid chromatography, and the content of NaCl in the amphoteric surfactant was determined by atomic absorption spectrometry. The results are shown in Table 1.

【表】【table】

【表】 ※1 定量法:高速液体クロマトグラフイー
法にて測定した。
〔条件〕 カラム:Fenesil C18(4φ×25cm) 温度:40℃ 流量:10ml/min 圧力:70Kg/cm2 波長:210nm 溶媒:0.03M−NaH2PO4/MeOH(1:9) ※2 定量法:重量法にて測定した。n−ブタノ
ール相を濃縮乾固後、充分に乾燥したのち、
重量を測定し原子吸光分析より得られる
NaCl量を差し引いた値を回収率とした。 実施例 2 両性界面活性剤10gとNa2SO4 2.0gをとり、こ
れに水100ml加えて溶解若しくは懸濁させた後、
シクロヘキサノール100mlを加えて実施例1と同
様な操作を行い、両性界面活性剤中に含有される
Na2SO4を求めた。結果は表2に示す。
[Table] *1 Quantitative method: Measured using high performance liquid chromatography.
[Conditions] Column: Fenesil C 18 (4φ x 25cm) Temperature: 40℃ Flow rate: 10ml/min Pressure: 70Kg/cm 2 wavelength: 210nm Solvent: 0.03M-NaH 2 PO 4 /MeOH (1:9) *2 Quantification Method: Measured by gravimetric method. After concentrating the n-butanol phase to dryness and thoroughly drying it,
Obtained by measuring weight and atomic absorption spectrometry
The value obtained by subtracting the amount of NaCl was defined as the recovery rate. Example 2 Take 10 g of amphoteric surfactant and 2.0 g of Na 2 SO 4 and add 100 ml of water to dissolve or suspend it.
Add 100 ml of cyclohexanol and perform the same operation as in Example 1 to remove the
Na 2 SO 4 was determined. The results are shown in Table 2.

【表】【table】

【表】 実施例 3 両性界面活性剤10gとNa2SO4 2.5gとり、これ
に水25ml加えて溶解若しくは懸濁させた後ヘキシ
ルアルコール125ml加えて実施例1と同様な操作
を行い、両性界面活性剤の回収率及び両性界面活
性剤中に含有されるNa2SO4を求めた。結果は表
3に示す。
[Table] Example 3 Take 10 g of an amphoteric surfactant and 2.5 g of Na 2 SO 4 , add 25 ml of water to dissolve or suspend it, then add 125 ml of hexyl alcohol and perform the same operation as in Example 1 to obtain an amphoteric interface. The recovery rate of the active agent and the Na 2 SO 4 contained in the amphoteric surfactant were determined. The results are shown in Table 3.

【表】【table】

【表】 実施例 4 Na,Na−ジメチルリジン塩酸塩4.21g(20ミリ
モル)に水40mlとアセトン40mlを加えて室温にて
撹拌し溶解する。次いでラウロイルクロライド
4.81g(22ミリモル)を10%−NaOHにてpH11.0
付近に保ちながらゆつくり適下してシヨツテンバ
ウマン反応を行う。10%−HClにて中和後、反応
液は徐々に加温して常圧にてアセトンを完全に留
去した後、n−ブタノール70mlを加えて室温にて
充分に撹拌し、抽出する。静置、分相後n−ブタ
ノール相をとり、再び水50ml加えて同様に撹拌し
たのち静置分相して得たn−ブタノール相を減圧
下濃縮乾固し、乾燥してN〓−ラウロイル−N〓,
N〓−ジメチルリジンを6.9g、収率97%を得た。
尚、結晶中のNaClの含有率は1%以下であつた。
[Table] Example 4 40 ml of water and 40 ml of acetone are added to 4.21 g (20 mmol) of N a , N a -dimethyllysine hydrochloride and dissolved by stirring at room temperature. Then lauroyl chloride
4.81g (22mmol) in 10%-NaOH pH 11.0
While keeping it nearby, slowly lower the dose to perform the Schotten-Baumann reaction. After neutralization with 10% HCl, the reaction solution is gradually heated and acetone is completely distilled off at normal pressure, and then 70 ml of n-butanol is added and thoroughly stirred at room temperature for extraction. After standing and phase separation, take the n-butanol phase, add 50 ml of water again, stir in the same way, leave to separate the phases, and concentrate the obtained n-butanol phase to dryness under reduced pressure. −N〓、
6.9 g of N-dimethyllysine was obtained in a yield of 97%.
Note that the content of NaCl in the crystals was 1% or less.

Claims (1)

【特許請求の範囲】 1 無機塩類を含有する両性界面活性剤水溶液若
しくは懸濁液を精製する際に、抽出溶媒として炭
素数4ないし10の飽和あるいは不飽和アルコール
を用いることを特長とする両性界面活性剤の精製
法。 2 アルコールがブタノール、ペンタノール、ヘ
キサノール、ヘプタノール、オクタノール、デカ
ノール、2−エチルオクタノール、シクロペンタ
ノール又はシクロヘキサノールである特許請求の
範囲第1項に記載の精製法。
[Claims] 1. An amphoteric interface characterized by using a saturated or unsaturated alcohol having 4 to 10 carbon atoms as an extraction solvent when purifying an amphoteric surfactant aqueous solution or suspension containing inorganic salts. Method for purifying activators. 2. The purification method according to claim 1, wherein the alcohol is butanol, pentanol, hexanol, heptanol, octanol, decanol, 2-ethyl octanol, cyclopentanol, or cyclohexanol.
JP18555382A 1982-10-22 1982-10-22 Purification of amphoteric surfactant Granted JPS5975998A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP18555382A JPS5975998A (en) 1982-10-22 1982-10-22 Purification of amphoteric surfactant

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP18555382A JPS5975998A (en) 1982-10-22 1982-10-22 Purification of amphoteric surfactant

Publications (2)

Publication Number Publication Date
JPS5975998A JPS5975998A (en) 1984-04-28
JPH033720B2 true JPH033720B2 (en) 1991-01-21

Family

ID=16172816

Family Applications (1)

Application Number Title Priority Date Filing Date
JP18555382A Granted JPS5975998A (en) 1982-10-22 1982-10-22 Purification of amphoteric surfactant

Country Status (1)

Country Link
JP (1) JPS5975998A (en)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS63130129A (en) * 1986-11-18 1988-06-02 Kao Corp Surfactant and its preparation
DE10117222B4 (en) * 2001-04-06 2004-12-30 Goldschmidt Ag Process for the preparation of glycine derivatives

Also Published As

Publication number Publication date
JPS5975998A (en) 1984-04-28

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