JPH032171B2 - - Google Patents
Info
- Publication number
- JPH032171B2 JPH032171B2 JP56155604A JP15560481A JPH032171B2 JP H032171 B2 JPH032171 B2 JP H032171B2 JP 56155604 A JP56155604 A JP 56155604A JP 15560481 A JP15560481 A JP 15560481A JP H032171 B2 JPH032171 B2 JP H032171B2
- Authority
- JP
- Japan
- Prior art keywords
- dimethylformamide
- dioxane
- weight ratio
- mixed solvent
- glutamate
- 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
Links
Landscapes
- Synthetic Leather, Interior Materials Or Flexible Sheet Materials (AREA)
- Polyurethanes Or Polyureas (AREA)
- Treatments For Attaching Organic Compounds To Fibrous Goods (AREA)
Description
本発明はポリアミノ酸ウレタン共重合樹脂の製
造法に関する。更に詳しくはジメチルホルムアミ
ドとジオキサンとの混合溶媒中でのポリアミノ酸
ウレタン共重合樹脂の製造法に関する。
従来ポリアミノ酸−ウレタン共重合樹脂(以下
PAuと略称する)はポリアミノ酸樹脂の弾性接
着性の改良を目的に開発され、繊維加工の分野、
特に人造皮革用樹脂として用いられている。
PAuをコーテイングした人造皮革は他の樹脂
(主としてウレタン樹脂)をコーテイングしたも
のに比べて風合いが天然皮革に近く、透湿性、染
色性、耐寒性、耐熱性の優れたものが得られてい
る。しかし樹脂の溶媒がハロゲン系であるため、
人造皮革の工業生産において樹脂をコーテイング
する時、溶媒から発生する微量塩酸がコーテイン
グ装置を腐蝕させたり又溶媒が非水溶性であるた
め湿式加工が不可能である等の問題がある。
従つて汎用品として使用することは不可能であ
る。
本発明の目的はこれらの問題点を解決するた
め、ハロゲン系以外の水溶性溶媒を使用した
PAuの合成法について種々検討した結果、溶媒
としてジメチルホルムアミドとジオキサンとの混
合溶媒を見い出すことにより、流動性良好な
PAu溶液が得られ、従来のハロゲン系溶媒を用
いた前記問題点が解決出来ることを知見し、本発
明に到達した。
本発明の要旨は、ジメチルホルムアミドとジオ
キサンとの重量比95:5〜30:70の混合溶媒中に
光学活性γ−アルキル−グルタメート−N−カル
ボン酸無水物を主体としたα−アミノ酸−N−カ
ルボン酸無水物と末端にイソシアネート基を有す
るウレタンプレポリマーとを混合した後、アミン
類を添加して反応させることを特徴とするポリア
ミノ酸−ウレタン樹脂の製造法および
ジメチルホルムアミドとジオキサンとの重量比
95:5〜30:70の混合溶媒中で末端にイソシアネ
ート基を有するウレタンプレポリマーと水又はア
ミン類とを反応させたものに、光学活性γ−アル
キルグルタメート−N−カルボン酸無水物を主体
としたα−アミノ酸−N−カルボン酸無水物を添
加して反応させることを特徴とするポリアミノ酸
−ウレタン樹脂の製造法並びに、
ジメチルホルムアミドとジオキサンとの重量比
95:5〜30:70の混合溶媒中で末端にイソシアネ
ート基を有するウレタンプレポリマーと水又はア
ミン類とを反応させたものに光学活性γ−アルキ
ルグルタメート−N−カルボン酸無水物を主体と
したα−アミノ酸−N−カルボン酸無水物を反応
させた後、更に末端にイソシアネート基を有する
ウレタンプレポリマーを反応させることを特徴と
するポリアミノ酸ウレタン樹脂の製造法に存す
る。
以下本発明の詳細に説明する。
本発明におけるPAu製造の溶媒組成、すなわ
ちジメチルホルムアミドとジオキサンとの混合溶
媒の組成は重量比でジメチルホルムアミド/ジオ
キサン=95/5〜30/70の範囲であるが、好まし
くは80/20〜50/50更に好ましくは80/20〜60/
40である。ここでジメチルホルムアミド単独すな
わち重量比100/0の場合得られた樹脂溶液は透
明ゲル状で実用的なものでない。また逆にジオキ
サン単独すなわち重量比0/100の場合、白濁ゲ
ル状でこの場合も実用的なものは得られない。
本発明に用いる光学活性γ−アルキル−グルタ
メート−N−カルボン酸無水物(以下において、
N−カルボン酸無水物をNCAと略す)としては、
γ−メチル−L−グルタメートNCA、γ−エチ
ル−L−グルタメートNCA等のγ−アルキル−
L−グルタメートNCAおよびγ−メチル−D−
グルタメートNCA、γ−エチル−D−グルタメ
ートNCA等のγ−アルキル−D−グルタメート
NCAを示し単独又はこれらの混合物が使用され
る。又、γ−アルキル−グルタメートNCAを主
体としたα−アミノ酸NCAとは前記光学活性γ
−アルキル−グルタメートNCAと、他のアミノ
酸NCA例えばグリシンNCA、L−アスパラギン
酸−β−メチルエステルNCA、L−アラニン
NCAおよびD−アラニンNCA等との混合物を意
味し、物性と価格を考慮すると、γ−メチル−L
−グルタメートNCA又はγ−メチル−D−グル
タメートNCAを単独で用いる場合の方が工業的
には有利な場合が多い。
末端にイソシアネート基を有するウレタンプレ
ポリマーとしてはイソシアネートとポリオールを
当量比NCO/OH>1の条件で反応させて得られ
るものであるが、イソシアネート成分としては芳
香族ジイソシアネート、脂肪族ジイソシアネート
および脂環式ジイソシアネートの単独又はこれら
の混合物が用いられる。たとえばトルエン−2,
4−ジイソシアネート、4,4′−ジフエニルメタ
ンジイソシアネート、メタフエニレンジイソシア
ネート、1,6−ヘキサンジイソシアネート、
1,10−デカンメチレンジイソシアネート、1,
4−シクロヘキサンジイソシアネート、3−イソ
シアネートメチル−3,5,5−トリメチルシク
ロヘキシルイソシアネート(イソホロンジイソシ
アネート)等があげられる。
又ポリオール成分としたは通常のウレタン製品
に使用されるポリエーテルグリコール、ポリエス
テルグリコールが使用可能でポリエーテルグリコ
ールとしては、ポリエチレングリコール、ポリプ
ロピレンエーテルグリコール、ポリテトラメチレ
ングリコールおよびビスフエノールAとエチレン
オキサイド又はプロピレンオキサイド等との重付
加反応物等が適当である。
又ポリエステルグリコールとしてはポリカプロ
ラクトングリコールまたはエチレングリコール、
1,4−ブタンジオール等のジオール類とアジピ
ン酸、セバシン酸、コハク酸の二塩基酸との反応
で得られたものが用いられる。これらポリエーテ
ルおよびポリエステルの数平均分子量は200〜300
以上のものが好ましく単独又はその混合物が用い
られる。
本発明の後記の共重合法で用いるアミン類と
しては下記一般式で示されるものが適当である。
The present invention relates to a method for producing a polyamino acid urethane copolymer resin. More specifically, the present invention relates to a method for producing a polyamino acid urethane copolymer resin in a mixed solvent of dimethylformamide and dioxane. Conventional polyamino acid-urethane copolymer resin (hereinafter referred to as
(abbreviated as PAu) was developed for the purpose of improving the elastic adhesion of polyamino acid resin, and is used in the field of textile processing.
It is especially used as a resin for artificial leather. Artificial leather coated with PAu has a texture closer to that of natural leather than those coated with other resins (mainly urethane resin), and has excellent moisture permeability, dyeability, cold resistance, and heat resistance. However, since the resin solvent is halogen-based,
When coating with resin in the industrial production of artificial leather, there are problems such as trace amounts of hydrochloric acid generated from the solvent corroding the coating equipment and wet processing being impossible because the solvent is water-insoluble. Therefore, it is impossible to use it as a general-purpose product. The purpose of the present invention is to solve these problems by using water-soluble solvents other than halogen-based solvents.
As a result of various studies on the synthesis method of PAu, we found a mixed solvent of dimethylformamide and dioxane as a solvent, which has good fluidity.
The inventors discovered that a PAu solution could be obtained and that the problems described above using conventional halogenated solvents could be solved, and the present invention was achieved. The gist of the present invention is to provide an α-amino acid-N-containing compound containing optically active γ-alkyl-glutamate-N-carboxylic acid anhydride as a main component in a mixed solvent of dimethylformamide and dioxane in a weight ratio of 95:5 to 30:70. A method for producing a polyamino acid-urethane resin, which is characterized by mixing a carboxylic acid anhydride and a urethane prepolymer having an isocyanate group at the end, and then adding an amine to react the mixture, and the weight ratio of dimethylformamide and dioxane.
A urethane prepolymer having terminal isocyanate groups is reacted with water or amines in a mixed solvent of 95:5 to 30:70, and a mixture containing optically active γ-alkylglutamate-N-carboxylic acid anhydride as a main component is added. A method for producing a polyamino acid-urethane resin characterized by adding and reacting α-amino acid-N-carboxylic acid anhydride, and weight ratio of dimethylformamide and dioxane.
A urethane prepolymer having an isocyanate group at the end is reacted with water or amines in a mixed solvent of 95:5 to 30:70, and the resulting product is made mainly of optically active γ-alkylglutamate-N-carboxylic acid anhydride. The present invention relates to a method for producing a polyamino acid urethane resin, which comprises reacting an α-amino acid-N-carboxylic acid anhydride and then reacting a urethane prepolymer having an isocyanate group at its terminal end. The present invention will be explained in detail below. The solvent composition for PAu production in the present invention, that is, the composition of the mixed solvent of dimethylformamide and dioxane, is in a weight ratio of dimethylformamide/dioxane = 95/5 to 30/70, preferably 80/20 to 50/ 50 more preferably 80/20~60/
It is 40. Here, when dimethylformamide is used alone, that is, at a weight ratio of 100/0, the resulting resin solution is in the form of a transparent gel and is not practical. On the other hand, when dioxane is used alone, i.e., at a weight ratio of 0/100, it becomes a cloudy gel and cannot be used for practical purposes. Optically active γ-alkyl-glutamate-N-carboxylic acid anhydride used in the present invention (hereinafter,
N-carboxylic acid anhydride (abbreviated as NCA) is:
γ-alkyl- such as γ-methyl-L-glutamate NCA, γ-ethyl-L-glutamate NCA, etc.
L-glutamate NCA and γ-methyl-D-
γ-alkyl-D-glutamates such as glutamate NCA, γ-ethyl-D-glutamate NCA, etc.
NCAs are used alone or in mixtures. In addition, α-amino acid NCA mainly composed of γ-alkyl-glutamate NCA refers to the optically active γ
-Alkyl-glutamate NCAs and other amino acid NCAs such as glycine NCA, L-aspartic acid-β-methyl ester NCA, L-alanine
It means a mixture of NCA and D-alanine NCA, etc. Considering physical properties and price, γ-methyl-L
It is often industrially more advantageous to use -glutamate NCA or γ-methyl-D-glutamate NCA alone. The urethane prepolymer having isocyanate groups at the terminals is obtained by reacting isocyanate and polyol under the conditions of equivalent ratio NCO/OH>1, but the isocyanate component is aromatic diisocyanate, aliphatic diisocyanate and alicyclic diisocyanate. Diisocyanates alone or mixtures thereof may be used. For example, toluene-2,
4-diisocyanate, 4,4'-diphenylmethane diisocyanate, metaphenylene diisocyanate, 1,6-hexane diisocyanate,
1,10-decane methylene diisocyanate, 1,
Examples include 4-cyclohexane diisocyanate, 3-isocyanate methyl-3,5,5-trimethylcyclohexyl isocyanate (isophorone diisocyanate), and the like. As polyol components, polyether glycols and polyester glycols used in ordinary urethane products can be used. Polyether glycols include polyethylene glycol, polypropylene ether glycol, polytetramethylene glycol, bisphenol A and ethylene oxide or propylene. Polyaddition reaction products with oxides etc. are suitable. Polyester glycols include polycaprolactone glycol or ethylene glycol,
Those obtained by reacting diols such as 1,4-butanediol with dibasic acids such as adipic acid, sebacic acid, and succinic acid are used. The number average molecular weight of these polyethers and polyesters is 200-300
The above compounds are preferably used alone or in combination. As the amines used in the copolymerization method of the present invention described later, those represented by the following general formula are suitable.
【式】【formula】
一方ジメチルホルムアミド/ジオキサン(重量
比)=7/3の混合溶媒のかわりにジメチルホル
ムアミド又はジオキサン単独で用いるとゲル化
し、合成中撹拌不可能となつた。
実施例 2
ポリテトラメチレンエーテルグリコール(OH
価56.9)985g、1,6−ヘキサメチレンジイソ
シアネート、168gを90℃で4時間反応させ、末
端にイソシアネート基を有するウレタンプレポリ
マー(NCO当量1179)を得た。該ウレタンプレ
ポリマー85gとγ−メチル−L−グルタメート−
NCA−85gをジメチルホルムアミド/ジオキサ
ン(重量比)=7/3の混合溶媒644gに溶解しか
きまぜながら2%含水ヒドラジン溶液81.1gを加
え30℃で2時間反応を行うと、粘度8000cpsの乳
濁状の流動性良好な溶液を得た。この溶液を乾式
法によりフイルムにすると、無色透明なものが得
られた。フイルム物性を次に示す。
〔測定法は実施例1の方法〕
20%伸長回復率、73%、ヤング率、480Kg/cm2。
100%モジユラス45Kg/cm2。切断強度 320Kg/
cm2。切断伸度 550%
一方、ジメチルホルムアミド/ジオキサン(重
量比)=7/3の混合溶媒のかわりにジメチルホ
ルムアミド又はジオキサン単独で用いるとゲル化
し合成中に撹拌不可能となつた。
実施例 3
ポリテトラメチレンエーテルグリコール(OH
価56.9)1970g、1,6−ヘキサメチレンジイソ
シアネート504gを90℃で5時間反応させ末端に
イソシアネート基を有するウレタンプレポリマー
(NCO当量2340)を得た。該ウレタンプレポリマ
ー85gとγ−メチル−L−グルタメート−
NCA85gをジメチルホルムアミド/ジオキサン
(重量比)=7/3の混合溶媒666gに溶解し、か
きまぜながら2%トリエチルアミン溶液50gを添
加し、30℃で5時間反応を行うと粘度25000cps
(30℃)の乳濁状の流動性良好な溶液を得た。こ
の溶液を乾式法によりフイルムにすると無色透明
なものが得られた。
一方ジメチルホルムアミド/ジオキサン(重量
比)=7/3の混合溶媒のかわりにジメチルホル
ムアミド又はジオキサンを単独で用いると、合成
中にゲル状となり、撹拌不可能となつた。
実施例 4
ポリテトラメチレンエーテルグリコール1930
g、トリレンジイソシアネート348gを70℃で3
時間反応させ末端にイソシアネート基を有するウ
レタンプレポリマー(NCO当量1163)を得た。
該ウレタンプレポリマー85gとγ−メチル−L
−グルタメートNCA85gをジメチルホルムアミ
ド/ジオキサン(重量比)=7/3の混合溶媒644
gに溶解し、かきまぜながら2%含水ヒドラジン
溶液82.2gを加えて30℃で2時間反応を行うと粘
度3500cps(25℃)で乳濁状の流動性良好な溶液を
得た。この樹脂溶液をガラス板上に流延し水に浸
漬すると、ミクロポーラス状の白色のフイルムが
得られた。
実施例 5
実施例3で用いたウレタンプレポリマー57.1g
とγ−メチル−L−グルタメートNCA75.6gを
ジメチルホルムアミド/ジオキサン(重量比)=
7/3の混合溶媒644gに溶解し、かきまぜなが
ら2%含水ヒドラジン溶液91gを加え30℃で2時
間反応を行うと粘度18000cps(25℃)で乳濁状の
流動性良好な溶液を得た。この樹脂溶液をガラス
板上に流延し、水に浸漬すると、ミクロポーラス
状の白色のフイルムが得られた。
一方ジメチルホルムアミド/ジオキサン(重量
比)=7/3の混合溶媒のかわりにジメチルホル
ムアミド又はジオキサンを単独で用いると合成中
にゲル状となり撹拌不可能となつた。
実施例 6
実施例3で用いたウレタンプレポリマー85gと
γ−メチル−L−グルタメートNCA85gをジメ
チルホルムアミド/ジオキサン(重量比)=45/
55の混合溶媒644gに溶解しかきまぜながら2%
含水ヒドラジン91gを加え30℃で2時間反応させ
ると粘度12000cps(25℃)で乳濁状の流動性良好
な溶液を得た。この樹脂溶液をガラス板上に流し
水中に浸漬し、風乾するとミクロポーラスの白色
フイルムを得た。
実施例 7
実施例3で用いたウレタンプレポリマー85gと
γ−メチル−DグルタメートNCA85gをジメチ
ルホルムアミド/ジオキサン(重量比)=7/3
の混合溶媒644g溶解しかきまぜながら2%含水
ヒドラジン91gを加え30℃で2時間反応させると
粘度13000cps(25℃)で乳濁状の流動性良好な溶
液を得た。この樹脂溶液をガラス板上に流し水中
に浸漬し、風乾するとミクロポーラスの白色フイ
ルムを得た。
実施例 8
実施例3で用いたウレタンプレポリマー85gと
γ−エチル−L−グルタメートNCA85gをジメ
チルホルムアミド/ジオキサン(重量比)=7/
3の混合溶媒に加え、かきまぜながら2%含水ヒ
ドラジン溶液91gを添加し35℃で2時間反応させ
ると粘度11000cps(25℃)で乳濁状の流動性良好
な溶液を得た。この樹脂溶液をガラス板上に流し
水中に浸漬し、風乾するとミクロポーラスの白色
フイルムを得た。一方ジメチルホルムアミド/ジ
オキサン(重量比)=7/3の混合溶媒のかわり
にジメチルホルムアミド又はジオキサンを単独で
用いた場合合成中、ゲル状となり撹拌不可能とな
つた。
実施例 9
ポリテトラメチレンエーテルグリコール(OH
価56.9)985と4,4′−ジフエニルメタンジイソ
シアネート200gを70℃で5時間反応させ末端に
イソシアネート基を有するウレタンプレポリマー
(NCO当量1850)を得た。
該ウレタンプレポリマー85gとγ−メチル−L
−グルタメートNCA85gをジメチルホルムアミ
ド/ジオキサン(重量比)=60/40、550gに溶解
しかきまぜながら、トリエチルアミン4.6gをジ
メチルホルムアミド/ジオキサン(重量比)=
60/40、45gに溶解したものを添加し、30℃で5
時間反応を行うと粘度15000cps(30℃)の乳濁状
の流動性ある溶液が得られた。
ここでジメチルホルムアミド/ジオキサン(重
量比)60/40の混合溶媒の代わりにジメチルホル
ムアミド単独、ジオキサン単独またはジメチルホ
ルムアミド/ジオキサン(重量比)=10/90の溶
媒を用いると、合成中に白濁ゲル状化した。ま
た、ジメチルホルムアミド/ジメチルエーテル
(重量比)=60/40、およびジメチルホルムアミ
ド/ジエチルエーテル(重量比)=60/40を溶媒
とした場合も白濁ゲル状化した。
実施例 10
ポリテトラメチレンエーテルグリコール(OH
価56.9)985gと4,4′−ジフエニルメタンジイ
ソシアネート250gを70℃で5時間反応させ、末
端にイソシアネート基を有するウレタンプレポリ
マー(NCO当量1255)を得た。
次に、ヒドラジンヒドラート(H2N−NH2・
H2O)2.03gをジメチルホルムアミド/ジオキサ
ン(重量比)=70/30の混合溶媒638gに溶解しか
きまぜながら、前記ウレタンプレポリマー85gを
ジメチルホルムアミド/ジオキサン(重量比)=
70/30の混合溶媒85gに溶解したものをこれに滴
下反応させ、末端にアミノ基を有するウレタン溶
液を得た。
該ウレタン溶液にγ−メチル−L−グルタメー
ト−NCA85gを加えて4時間反応を行い、粘度
8000cps/25℃のPAU溶液を得た。
実施例 11
ヒドラジンヒドラート(H2N−NH2・H2O)
2.9gをジメチルホルムアミド/ジオキサン(重
量比)=70/30の混合溶媒638gに溶解したものを
撹拌し、これに実施例10で用いたウレタンプレポ
リマー(NCO当量1255)85gをジメチルホルム
アミド/ジオキサン(重量比)=70/30の混合溶
媒85gに溶解したものを滴下反応させ、末端にア
ミノ基を有するウレタン溶液を得た。
該ウレタン溶液にγ−メチル−L−グルタメー
ト−NCA85gを加えて2時間反応を行つた後、
これに前記ウレタンプレポリマー56gを同重量の
ジメチルホルムアミド/ジオキサン=70/30の混
合溶媒に溶解したものを加えて反応させ、粘度
12000cps/250℃のPAU溶液を得た。
On the other hand, when dimethylformamide or dioxane alone was used instead of the mixed solvent of dimethylformamide/dioxane (weight ratio) = 7/3, it gelled and became impossible to stir during the synthesis. Example 2 Polytetramethylene ether glycol (OH
985 g of 1,6-hexamethylene diisocyanate (value 56.9) and 168 g of 1,6-hexamethylene diisocyanate were reacted at 90° C. for 4 hours to obtain a urethane prepolymer having isocyanate groups at the terminals (NCO equivalent weight: 1179). 85 g of the urethane prepolymer and γ-methyl-L-glutamate
Dissolve 85g of NCA in 644g of a mixed solvent of dimethylformamide/dioxane (weight ratio) = 7/3, add 81.1g of a 2% hydrated hydrazine solution while stirring, and react at 30°C for 2 hours, resulting in an emulsion with a viscosity of 8000cps. A solution with good fluidity was obtained. When this solution was made into a film by a dry method, a colorless and transparent film was obtained. The physical properties of the film are shown below. [Measurement method is the method of Example 1] 20% elongation recovery rate, 73%, Young's modulus, 480 Kg/cm 2 .
100% modulus 45Kg/ cm2 . Cutting strength 320Kg/
cm2 . Cutting elongation: 550% On the other hand, when dimethylformamide or dioxane alone was used instead of a mixed solvent of dimethylformamide/dioxane (weight ratio) = 7/3, it gelled and became impossible to stir during synthesis. Example 3 Polytetramethylene ether glycol (OH
56.9) and 504 g of 1,6-hexamethylene diisocyanate were reacted at 90°C for 5 hours to obtain a urethane prepolymer having isocyanate groups at the terminals (NCO equivalent: 2340). 85 g of the urethane prepolymer and γ-methyl-L-glutamate
When 85g of NCA was dissolved in 666g of a mixed solvent of dimethylformamide/dioxane (weight ratio) = 7/3, 50g of 2% triethylamine solution was added while stirring, and the reaction was performed at 30°C for 5 hours, resulting in a viscosity of 25000 cps.
(30°C) An emulsion-like solution with good fluidity was obtained. When this solution was made into a film by a dry method, a colorless and transparent film was obtained. On the other hand, when dimethylformamide or dioxane was used alone instead of a mixed solvent of dimethylformamide/dioxane (weight ratio) = 7/3, the mixture became gel-like during synthesis and became impossible to stir. Example 4 Polytetramethylene ether glycol 1930
g, 348 g of tolylene diisocyanate at 70℃
A urethane prepolymer (NCO equivalent weight: 1163) having an isocyanate group at the end was obtained by reacting for a period of time. 85g of the urethane prepolymer and γ-methyl-L
- Glutamate NCA 85g in dimethylformamide/dioxane (weight ratio) = 7/3 mixed solvent 644
82.2 g of a 2% aqueous hydrazine solution was added with stirring, and the reaction was carried out at 30°C for 2 hours to obtain an emulsified solution with a viscosity of 3500 cps (at 25°C) and good fluidity. When this resin solution was cast onto a glass plate and immersed in water, a microporous white film was obtained. Example 5 57.1g of urethane prepolymer used in Example 3
and 75.6 g of γ-methyl-L-glutamate NCA in dimethylformamide/dioxane (weight ratio) =
The mixture was dissolved in 644 g of a 7/3 mixed solvent, and while stirring, 91 g of a 2% hydrous hydrazine solution was added and the reaction was carried out at 30°C for 2 hours to obtain an emulsified solution with a viscosity of 18,000 cps (at 25°C) and good fluidity. When this resin solution was cast onto a glass plate and immersed in water, a microporous white film was obtained. On the other hand, when dimethylformamide or dioxane was used alone instead of the mixed solvent of dimethylformamide/dioxane (weight ratio) = 7/3, it became gel-like during synthesis and became impossible to stir. Example 6 85 g of the urethane prepolymer used in Example 3 and 85 g of γ-methyl-L-glutamate NCA were mixed in dimethylformamide/dioxane (weight ratio) = 45/
Dissolve 2% in 644g of mixed solvent of 55 and stir.
91 g of hydrous hydrazine was added and reacted at 30°C for 2 hours to obtain an emulsion-like solution with good fluidity and a viscosity of 12,000 cps (25°C). This resin solution was poured onto a glass plate, immersed in water, and air-dried to obtain a microporous white film. Example 7 85 g of the urethane prepolymer used in Example 3 and 85 g of γ-methyl-D glutamate NCA were mixed in dimethylformamide/dioxane (weight ratio) = 7/3.
644 g of the mixed solvent was dissolved, and while stirring, 91 g of 2% hydrazine was added and reacted at 30°C for 2 hours to obtain an emulsion-like solution with good fluidity and a viscosity of 13,000 cps (at 25°C). This resin solution was poured onto a glass plate, immersed in water, and air-dried to obtain a microporous white film. Example 8 85 g of the urethane prepolymer used in Example 3 and 85 g of γ-ethyl-L-glutamate NCA were mixed in dimethylformamide/dioxane (weight ratio) = 7/
In addition to the mixed solvent of No. 3, 91 g of a 2% hydrous hydrazine solution was added with stirring, and the mixture was reacted at 35°C for 2 hours to obtain an emulsion-like solution with good fluidity and a viscosity of 11,000 cps (at 25°C). This resin solution was poured onto a glass plate, immersed in water, and air-dried to obtain a microporous white film. On the other hand, when dimethylformamide or dioxane was used alone instead of the mixed solvent of dimethylformamide/dioxane (weight ratio) = 7/3, the mixture became gelatinous during synthesis and became impossible to stir. Example 9 Polytetramethylene ether glycol (OH
985 and 200 g of 4,4'-diphenylmethane diisocyanate were reacted at 70°C for 5 hours to obtain a urethane prepolymer (NCO equivalent: 1850) having isocyanate groups at the ends. 85g of the urethane prepolymer and γ-methyl-L
- 85g of glutamate NCA was dissolved in 550g of dimethylformamide/dioxane (weight ratio) = 60/40, while stirring, 4.6g of triethylamine was dissolved in dimethylformamide/dioxane (weight ratio) =
Add 45g of 60/40 and heat at 30℃ for 5 minutes.
After a time reaction, a fluid emulsion solution with a viscosity of 15,000 cps (30°C) was obtained. Here, if dimethylformamide alone, dioxane alone, or dimethylformamide/dioxane (weight ratio) = 10/90 is used instead of the mixed solvent of dimethylformamide/dioxane (weight ratio) 60/40, a cloudy gel will form during synthesis. It became. In addition, when dimethylformamide/dimethyl ether (weight ratio) = 60/40 and dimethylformamide/diethyl ether (weight ratio) = 60/40 were used as solvents, a cloudy gel was formed. Example 10 Polytetramethylene ether glycol (OH
985 g of 4,4'-diphenylmethane diisocyanate were reacted at 70°C for 5 hours to obtain a urethane prepolymer (NCO equivalent weight: 1255) having an isocyanate group at the end. Next, hydrazine hydrate (H 2 N−NH 2
While dissolving 2.03 g of dimethylformamide/dioxane (weight ratio) in 638 g of a mixed solvent of dimethylformamide/dioxane (weight ratio) = 70/30 and stirring, 85 g of the urethane prepolymer was dissolved in dimethylformamide/dioxane (weight ratio) = 70/30.
A solution dissolved in 85 g of a 70/30 mixed solvent was added dropwise to the solution to obtain a urethane solution having an amino group at the end. 85 g of γ-methyl-L-glutamate-NCA was added to the urethane solution and reacted for 4 hours to determine the viscosity.
A PAU solution of 8000 cps/25°C was obtained. Example 11 Hydrazine hydrate (H 2 N−NH 2 .H 2 O)
A mixture of 2.9 g of dimethylformamide/dioxane (weight ratio) = 70/30 was stirred, and 85 g of the urethane prepolymer (NCO equivalent: 1255) used in Example 10 was dissolved in dimethylformamide/dioxane (weight ratio). A solution dissolved in 85 g of a mixed solvent (weight ratio) = 70/30 was reacted dropwise to obtain a urethane solution having an amino group at the end. After adding 85 g of γ-methyl-L-glutamate-NCA to the urethane solution and carrying out a reaction for 2 hours,
To this, 56 g of the urethane prepolymer dissolved in the same weight of dimethylformamide/dioxane = 70/30 mixed solvent was added and reacted.
A PAU solution of 12000 cps/250°C was obtained.
Claims (1)
比95:5〜30:70の混合溶媒中に光学活性γ−ア
ルキル−グルタメート−N−カルボン酸無水物を
主体としたα−アミノ酸−N−カルボン酸無水物
と末端にイソシアネート基を有するウレタンプレ
ポリマーとを混合した後、アミン類を添加して反
応させることを特徴とするポリアミノ酸ウレタン
樹脂の製造法。 2 ジメチルホルムアミドとジオキサンとの重量
比95:5〜30:70の混合溶媒中で末端にイソシア
ネート基を有するウレタンプレポリマーと水又は
アミン類とを反応させたものに、光学活性γ−ア
ルキル−グルタメート−N−カルボン酸無水物を
主体としたα−アミノ酸−N−カルボン酸無水物
を添加して反応させることを特徴とするポリアミ
ノ酸ウレタン樹脂の製造法。 3 ジメチルホルムアミドとジオキサンとの重量
比95:5〜30:70の混合溶媒中で末端にイソシア
ネート基を有するウレタンプレポリマーと水又は
アミン類とを反応させたものに光学活性γ−アル
キル−グルタメート−N−カルボン酸無水物を主
体としたα−アミノ酸−N−カルボン酸無水物を
反応させた後、更に末端にイソシアネート基を有
するウレタンプレポリマーを反応させることを特
徴とするポリアミノ酸ウレタン樹脂の製造法。[Scope of Claims] 1. α-Amino acid-N mainly composed of optically active γ-alkyl-glutamate-N-carboxylic acid anhydride in a mixed solvent of dimethylformamide and dioxane in a weight ratio of 95:5 to 30:70. - A method for producing a polyamino acid urethane resin, which comprises mixing a carboxylic acid anhydride and a urethane prepolymer having an isocyanate group at the terminal, and then adding an amine to react the mixture. 2 Optically active γ-alkyl-glutamate is reacted with water or amines and a urethane prepolymer having an isocyanate group at the end in a mixed solvent of dimethylformamide and dioxane in a weight ratio of 95:5 to 30:70. A method for producing a polyamino acid urethane resin, which comprises adding and reacting an α-amino acid-N-carboxylic anhydride mainly consisting of -N-carboxylic anhydride. 3 Optically active γ-alkyl-glutamate is reacted with water or amines and a urethane prepolymer having an isocyanate group at the end in a mixed solvent of dimethylformamide and dioxane in a weight ratio of 95:5 to 30:70. Production of polyamino acid urethane resin characterized by reacting α-amino acid-N-carboxylic acid anhydride mainly composed of N-carboxylic acid anhydride, and then reacting with a urethane prepolymer having isocyanate groups at the terminals. Law.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP56155604A JPS5857420A (en) | 1981-09-30 | 1981-09-30 | Manufacturing method of polyamino acid urethane resin |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP56155604A JPS5857420A (en) | 1981-09-30 | 1981-09-30 | Manufacturing method of polyamino acid urethane resin |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS5857420A JPS5857420A (en) | 1983-04-05 |
| JPH032171B2 true JPH032171B2 (en) | 1991-01-14 |
Family
ID=15609650
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP56155604A Granted JPS5857420A (en) | 1981-09-30 | 1981-09-30 | Manufacturing method of polyamino acid urethane resin |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS5857420A (en) |
Families Citing this family (10)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS5936132A (en) * | 1982-08-23 | 1984-02-28 | Seiko Kasei Kk | Novel surface-treating agent |
| JPS60173176A (en) * | 1984-02-17 | 1985-09-06 | ユニチカ株式会社 | Production of moisture permeable water-proof cloth |
| JPS60181366A (en) * | 1984-02-20 | 1985-09-17 | ユニチカ株式会社 | Production of moisture pervious waterproof fabric |
| JPS6140315A (en) * | 1984-07-31 | 1986-02-26 | Mitsubishi Chem Ind Ltd | Method for producing polyamino acid urethane resin |
| JPS61138778A (en) * | 1984-12-07 | 1986-06-26 | Unitika Ltd | Breathable waterproofing cloth and its production |
| JPH0678416B2 (en) * | 1985-12-17 | 1994-10-05 | 三菱化成株式会社 | Method for producing polyamino acid urethane resin |
| JPH0351360Y2 (en) * | 1987-06-10 | 1991-11-01 | ||
| DE3800434A1 (en) * | 1988-01-09 | 1989-07-20 | Bayer Ag | HEAT-CURABLE COATING COMPOSITION BASED ON POLYURETHANE URBAN |
| NO921919L (en) * | 1991-06-01 | 1992-12-02 | Bayer Ag | COATING AGENT FOR WATER-PERMATIBLE COATING AND PROCEDURE FOR PREPARING THEREOF |
| DE4125454A1 (en) * | 1991-08-01 | 1993-02-04 | Bayer Ag | COATING AGENTS AND THEIR USE FOR PRODUCING WATER VAPOR-PERMEABLE COATINGS |
Family Cites Families (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS5210917A (en) * | 1975-07-15 | 1977-01-27 | Matsushita Electric Works Ltd | Eaves trough |
-
1981
- 1981-09-30 JP JP56155604A patent/JPS5857420A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS5857420A (en) | 1983-04-05 |
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