JP3384420B2 - Method for producing polyaspartate - Google Patents

Method for producing polyaspartate

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Publication number
JP3384420B2
JP3384420B2 JP20187894A JP20187894A JP3384420B2 JP 3384420 B2 JP3384420 B2 JP 3384420B2 JP 20187894 A JP20187894 A JP 20187894A JP 20187894 A JP20187894 A JP 20187894A JP 3384420 B2 JP3384420 B2 JP 3384420B2
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JP
Japan
Prior art keywords
polyaspartate
water
aqueous
aqueous solution
reaction
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
JP20187894A
Other languages
Japanese (ja)
Other versions
JPH0859821A (en
Inventor
達也 服部
健一 森
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
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Filing date
Publication date
Application filed by Ajinomoto Co Inc filed Critical Ajinomoto Co Inc
Priority to JP20187894A priority Critical patent/JP3384420B2/en
Publication of JPH0859821A publication Critical patent/JPH0859821A/en
Application granted granted Critical
Publication of JP3384420B2 publication Critical patent/JP3384420B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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Description

【発明の詳細な説明】 【0001】 【産業上の利用分野】本発明は、アミノ酸系ポリマーで
あるポリアスパラギン酸塩を効率良く製造する方法に関
するものである。本発明の目的化合物であるポリアスパ
ラギン酸塩は水溶性のポリマーであって、香粧品、食
品、医農薬品、製紙、塗料、皮革、フィルム、乳化剤な
どに有効であり、工業上重要な特性を有し、種々の用途
をもつ極めて有用なポリマーである。 【0002】 【従来の技術】これまでに種々のポリアミノ酸が合成さ
れ、様々な分野で利用されている。ポリアミノ酸の製造
方法としては、N−カルボキシ−α−アミノ酸無水物
(NCA)の重合による方法が簡便で一般的であるが、
NCAの製造にホスゲンを使用するため、取り扱いが極
めて難しく、大きく発展していない。 【0003】一方、ポリアスパラギン酸については、ア
スパラギン酸を加熱することにより容易にポリスクシン
イミドが生成し、それを加水分解することにより製造で
きることが知られている。特開平5−506615号公
報には、アスパラギン酸を充填した容器を直接加熱する
ことによリポリスクシンイミドを製造している。しかし
ながら、この方法では、均一に加熱することが困難であ
り、反応を完結するためにには、反応時間を長くする
か、あるいは230℃以上で加熱する必要があり、副反
応が起きやすくなる欠点があった。また、ヨーロッパ特
許公開公報0578449号では、アスパラギン酸をポ
リエチレングリコール中、200℃で15時間加熱した
後、生成したポリスクシンイミドを加水分解してポリア
スパラギン酸塩を製造しているが、反応に用いる溶媒が
水溶性であるため、製品から溶媒を除くことが困難であ
った。 【0004】 【発明が解決しようとする課題】本発明の目的は、副生
物、溶媒等の不純物の少ないポリアスパラギン酸を製造
することのできる簡便で効率のよい製造方法を提供する
ことである。 【0005】 【課題を解決するための手段】本発明者らは、上記課題
を解決するため鋭意検討した結果、非水溶性溶媒を用い
て反応を行うことにより効率よくポリスクシンイミドを
調製することができること、分層及びそれに続く無機ま
たは有機粉体を用いた処理により非水溶性溶媒を製品か
らほぼ完全に除去できることを見いだし、この知見に基
づき本発明を完成した。 【0006】すなわち、本発明は、下記工程(1)〜
(4)を行うことを特徴とするポリアスパラギン酸塩の
製造方法に関する。 (1)アスパラギン酸を非水溶性溶媒中で加熱しポリス
クシンイミドとする工程 (2)アルカリ水溶液を加えて加水分解しポリアスパラ
ギン酸塩とする工程 (3)ポリアスパラギン酸塩水溶液層を非水溶性溶媒層
から分離する工程 (4)ポリアスパラギン酸塩水溶液を無機または有機粉
体で処理する工程 【0007】本発明に用いられる非水溶性溶媒は、水と
混合したときに分層するものであって、沸点が200℃
以上のものであればよく、好ましいものとしては、n−
パラフィン、流動パラフィン等の飽和炭化水素化合物、
シリコーン系オイル、フッ素系オイル等の中で、200
℃以上、好ましくは230℃以上の沸点を有し、さらに
その25℃での粘度が100cP以下、好ましくは20
cP以下の溶媒が望ましい。溶媒の粘度が高いと反応で
発生する水を容易に留去できない。溶媒は2種類以上を
混合して使用してもよい。反応温度としては、200℃
〜230℃が望ましい。反応温度が200℃以下では、
反応が遅く反応効率が悪い。また、230℃以上では、
反応は短時間で終了するものの、副反応のため得られる
ポリアスパラギン酸塩に着色が起こる。 【0008】ポリスクシンイミドの加水分解に使用する
アルカリ水溶液としては、水酸化ナトリウム、水酸化カ
リウムまたは塩基性有機アミンの水溶液等が挙げられ
る。また、加水分解は、通常5℃〜75℃で行われる。 【0009】このようにして得られたポリアスパラギン
酸塩水溶液は、通常用いられる分層方法により非水溶性
溶媒と分離する。分離されたポリアスパラギン酸塩水溶
液には、非水溶性溶媒などの不純物をまだ少量含んでい
るが、無機または有機粉体により処理することにより、
ほぼ完全に除去することができる。無機粉体としては、
セライト、活性白土、酸性白土、合成ゼオライト、シリ
カ、アルミナ等を挙げることができ、有機粉体として
は、活性炭、セルロース粉末、イオン交換樹脂、吸着樹
脂、キレート樹脂等を挙げることができる。処理は、無
機粉体と有機粉体両方を用いて行った方がより好まし
い。また処理方法としては、無機または有機粉体をポリ
アスパラギン酸塩水溶液に添加して攪拌する、ポリアス
パラギン酸塩水溶液を無機または有機粉体を充填したカ
ラムに通すなど、通常用いられる方法により両者を接触
させればよい。 【0010】 【実施例】以下に実施例により、本発明を詳しく説明す
る。 【0011】実施例1 攪拌装置、還流冷却器、温度計を備え付けた1リットル
容量の4つ口フラスコを窒素置換した後、この中にL−
アスパラギン酸133gおよびn−パラフィン(H)2
00g(日本石油製、沸点244〜262℃、粘度2.
20cP)を加えた。これを220℃で4時間反応した
後、50℃まで冷却し、14%水酸化ナトリウム水溶液
286gを加え1時間攪拌した。反応混合物を水層と有
機層に分層させ、水層を取り出した。得られた水層は、
残存のn−パラフィンにより濁っていた。水層をセライ
ト及び活性炭を添加して処理することにより、ポリアス
パラギン酸ナトリウム塩水溶液を得た。この水層は透明
であった。GPC及び13C−NMRからアスパラギン酸
が100%反応したことを確認した。生成したポリアス
パラギン酸塩の分子量はMw=24000、Mw/Mn
=1.5であった。また、2%ポリアスパラギン酸ナト
リウム塩水溶液(pH=7)を調製し、UV透過率を測
定した。その結果を図1に示す。 【0012】比較例1 攪拌装置を備え付けた1リットル容量のフラスコを窒素
置換した後、その中にL−アスパラギン酸133gを加
えた。これを245℃で4時間反応した後、50℃まで
冷却し、14%水酸化ナトリウム水溶液286gを加え
1時間攪拌した。さらに、得られた水溶液から、2%ポ
リアスパラギン酸ナトリウム塩水溶液(pH=7)を調
製し、UV透過率を測定した(図1)。GPC測定の結
果、ポリアスパラギン酸の分子量、分子量分布とも実施
例1とほぼ同じであった。 【0013】比較例2 反応温度を200℃としたほかは実施例1と同様にして
ポリアスパラギン酸ナトリウム塩水溶液を調製した。G
PC測定したところ未反応アスパラギン酸が50%以上
残っていた。ポリアスパラギン酸の分子量は実施例1と
ほぼ同じであった。 【0014】 【発明の効果】本発明により、不純物の少ないポリアス
パラギン酸塩を効率的に製造することが可能となった。
Description: BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for efficiently producing an amino acid-based polymer, polyaspartate. The polyaspartic acid salt, which is the object compound of the present invention, is a water-soluble polymer, and is effective in cosmetics, foods, medicines and agrochemicals, papermaking, paints, leather, films, emulsifiers, etc., and has industrially important properties. It is a very useful polymer that has various uses. 2. Description of the Related Art Various polyamino acids have been synthesized and used in various fields. As a method for producing a polyamino acid, a method based on polymerization of N-carboxy-α-amino acid anhydride (NCA) is simple and generally used.
Since phosgene is used in the production of NCA, it is extremely difficult to handle and has not developed much. On the other hand, it is known that polyaspartic acid can be easily produced by heating aspartic acid to produce polysuccinimide and hydrolyzing it. Japanese Patent Application Laid-Open No. 5-506615 discloses the production of lipoliskcinimide by directly heating a container filled with aspartic acid. However, in this method, it is difficult to heat uniformly, and in order to complete the reaction, it is necessary to lengthen the reaction time or to heat at 230 ° C. or more, which is a disadvantage that a side reaction easily occurs. was there. In European Patent Publication No. 0 578 449, after aspartic acid is heated in polyethylene glycol at 200 ° C. for 15 hours, the produced polysuccinimide is hydrolyzed to produce a polyaspartic acid salt. It was difficult to remove the solvent from the product due to its water solubility. [0004] An object of the present invention is to provide a simple and efficient production method capable of producing polyaspartic acid having few impurities such as by-products and solvents. The present inventors have conducted intensive studies to solve the above-mentioned problems, and as a result, it has been found that polyisuccinimide can be efficiently prepared by performing a reaction using a water-insoluble solvent. The present inventors have found that the water-insoluble solvent can be almost completely removed from the product by separation and subsequent treatment with an inorganic or organic powder, and the present invention has been completed based on this finding. That is, the present invention provides the following steps (1) to
(4) A method for producing a polyaspartate, characterized by performing (4). (1) Step of heating aspartic acid in a water-insoluble solvent to form polysuccinimide (2) Step of adding an aqueous alkali solution to hydrolyze to form polyaspartate (3) Step of converting the aqueous layer of polyaspartate to water-insoluble Step of separating from the solvent layer (4) Step of treating the aqueous solution of polyaspartate with an inorganic or organic powder The water-insoluble solvent used in the present invention separates when mixed with water. And the boiling point is 200 ° C
Any of the above may be used, and preferred is n-
Saturated hydrocarbon compounds such as paraffin and liquid paraffin,
Among silicone oils, fluorine oils, etc., 200
° C, preferably 230 ° C or higher, and has a viscosity at 25 ° C of 100 cP or lower, preferably 20 cP or lower.
Solvents below cP are desirable. If the viscosity of the solvent is high, water generated in the reaction cannot be easily distilled off. Two or more solvents may be used as a mixture. The reaction temperature is 200 ° C
~ 230 ° C is desirable. When the reaction temperature is 200 ° C. or less,
The reaction is slow and the reaction efficiency is poor. At 230 ° C or higher,
Although the reaction is completed in a short time, the resulting polyaspartate is colored due to a side reaction. [0008] Examples of the aqueous alkali solution used for the hydrolysis of polysuccinimide include aqueous solutions of sodium hydroxide, potassium hydroxide and basic organic amines. The hydrolysis is usually performed at 5 ° C to 75 ° C. The aqueous solution of polyaspartate thus obtained is separated from a water-insoluble solvent by a commonly used separation method. The separated polyaspartate aqueous solution still contains a small amount of impurities such as a water-insoluble solvent, but by treating with an inorganic or organic powder,
It can be almost completely removed. As inorganic powder,
Celite, activated clay, acid clay, synthetic zeolite, silica, alumina and the like can be mentioned. As the organic powder, activated carbon, cellulose powder, ion exchange resin, adsorption resin, chelate resin and the like can be mentioned. The treatment is more preferably performed using both inorganic powder and organic powder. In addition, as a treatment method, an inorganic or organic powder is added to an aqueous solution of polyaspartate and agitated, and the aqueous solution of polyaspartate is passed through a column filled with inorganic or organic powder, and both are used by a commonly used method. What is necessary is just to make contact. The present invention will be described in detail with reference to the following examples. Example 1 A 1-liter four-necked flask equipped with a stirrer, a reflux condenser, and a thermometer was purged with nitrogen.
133 g of aspartic acid and n-paraffin (H) 2
00g (manufactured by Nippon Petroleum, boiling point: 244 to 262 ° C, viscosity: 2.
20 cP) was added. This was reacted at 220 ° C. for 4 hours, cooled to 50 ° C., 286 g of 14% aqueous sodium hydroxide solution was added, and the mixture was stirred for 1 hour. The reaction mixture was separated into an aqueous layer and an organic layer, and the aqueous layer was taken out. The resulting water layer is
It was cloudy due to residual n-paraffin. The aqueous layer was treated with celite and activated carbon to obtain an aqueous solution of sodium polyaspartate. This aqueous layer was transparent. It was confirmed by GPC and 13 C-NMR that aspartic acid had reacted 100%. The molecular weight of the produced polyaspartate is Mw = 24000, Mw / Mn
= 1.5. In addition, a 2% aqueous solution of sodium polyaspartate (pH = 7) was prepared, and the UV transmittance was measured. The result is shown in FIG. Comparative Example 1 After a 1-liter flask equipped with a stirrer was purged with nitrogen, 133 g of L-aspartic acid was added thereto. This was reacted at 245 ° C. for 4 hours, then cooled to 50 ° C., 286 g of 14% aqueous sodium hydroxide solution was added, and the mixture was stirred for 1 hour. Further, a 2% aqueous solution of sodium polyaspartate (pH = 7) was prepared from the obtained aqueous solution, and the UV transmittance was measured (FIG. 1). As a result of GPC measurement, the molecular weight and molecular weight distribution of polyaspartic acid were almost the same as those in Example 1. Comparative Example 2 An aqueous solution of sodium polyaspartate was prepared in the same manner as in Example 1 except that the reaction temperature was 200 ° C. G
As a result of PC measurement, 50% or more of unreacted aspartic acid remained. The molecular weight of polyaspartic acid was almost the same as in Example 1. According to the present invention, it has become possible to efficiently produce polyaspartate containing less impurities.

【図面の簡単な説明】 【図1】2%ポリアスパラギン酸ナトリウム塩水溶液の
透過率を示す。
BRIEF DESCRIPTION OF THE DRAWINGS FIG. 1 shows the transmittance of a 2% aqueous solution of sodium polyaspartate.

Claims (1)

(57)【特許請求の範囲】 【請求項1】下記工程(1)〜(4)を行うことを特徴
とするポリアスパラギン酸塩の製造方法。 (1)アスパラギン酸を非水溶性溶媒中で加熱しポリス
クシンイミドとする工程 (2)アルカリ水溶液を加えて加水分解しポリアスパラ
ギン酸塩とする工程 (3)ポリアスパラギン酸塩水溶液層を非水溶性溶媒層
から分離する工程 (4)ポリアスパラギン酸塩水溶液を無機または有機粉
体で処理する工程
(57) [Claims] (1) A method for producing a polyaspartate, which comprises performing the following steps (1) to (4). (1) Step of heating aspartic acid in a water-insoluble solvent to form polysuccinimide (2) Step of adding an aqueous alkali solution to hydrolyze to form polyaspartate (3) Step of converting the aqueous layer of polyaspartate to water-insoluble Step of separating from solvent layer (4) Step of treating polyaspartate aqueous solution with inorganic or organic powder
JP20187894A 1994-08-26 1994-08-26 Method for producing polyaspartate Expired - Lifetime JP3384420B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP20187894A JP3384420B2 (en) 1994-08-26 1994-08-26 Method for producing polyaspartate

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP20187894A JP3384420B2 (en) 1994-08-26 1994-08-26 Method for producing polyaspartate

Publications (2)

Publication Number Publication Date
JPH0859821A JPH0859821A (en) 1996-03-05
JP3384420B2 true JP3384420B2 (en) 2003-03-10

Family

ID=16448366

Family Applications (1)

Application Number Title Priority Date Filing Date
JP20187894A Expired - Lifetime JP3384420B2 (en) 1994-08-26 1994-08-26 Method for producing polyaspartate

Country Status (1)

Country Link
JP (1) JP3384420B2 (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2011102293A1 (en) 2010-02-18 2011-08-25 三井化学株式会社 Processes for production of polyaspartic acid precursor polymer and polyaspartic acid salts
WO2019189837A1 (en) 2018-03-30 2019-10-03 三井化学株式会社 Anti-redeposition agent and detergent composition
WO2022059486A1 (en) 2020-09-15 2022-03-24 三井化学株式会社 Powder cosmetic and cosmetic composition

Families Citing this family (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5635447A (en) * 1996-03-22 1997-06-03 Donlar Corporation Polyorganic acids and their analogues to enhance herbicide effectiveness
US5939522A (en) * 1997-09-05 1999-08-17 Donlar Corporation Production of polysuccinimide and polyaspartate in thioether solvents
EP0926184A1 (en) * 1997-12-25 1999-06-30 Mitsui Chemicals, Inc. Process for production of polyamino acid derivative
WO2001048056A1 (en) * 1999-12-28 2001-07-05 Mitsui Chemicals, Incorporated Process for producing crosslinked polyaspartic acid (salt)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2011102293A1 (en) 2010-02-18 2011-08-25 三井化学株式会社 Processes for production of polyaspartic acid precursor polymer and polyaspartic acid salts
US9096720B2 (en) 2010-02-18 2015-08-04 Mitsui Chemicals, Inc. Methods for producing polyaspartic acid precursor polymer and polyaspartic acid salt
WO2019189837A1 (en) 2018-03-30 2019-10-03 三井化学株式会社 Anti-redeposition agent and detergent composition
WO2022059486A1 (en) 2020-09-15 2022-03-24 三井化学株式会社 Powder cosmetic and cosmetic composition

Also Published As

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