JPS59199717A - Preparation of polyamide - Google Patents

Preparation of polyamide

Info

Publication number
JPS59199717A
JPS59199717A JP7301283A JP7301283A JPS59199717A JP S59199717 A JPS59199717 A JP S59199717A JP 7301283 A JP7301283 A JP 7301283A JP 7301283 A JP7301283 A JP 7301283A JP S59199717 A JPS59199717 A JP S59199717A
Authority
JP
Japan
Prior art keywords
dicarboxylic acid
polyamide
diamine
acid
added
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
JP7301283A
Other languages
Japanese (ja)
Inventor
Mitsuru Ueda
充 上田
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.)
Idemitsu Kosan Co Ltd
Original Assignee
Idemitsu Kosan 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 Idemitsu Kosan Co Ltd filed Critical Idemitsu Kosan Co Ltd
Priority to JP7301283A priority Critical patent/JPS59199717A/en
Publication of JPS59199717A publication Critical patent/JPS59199717A/en
Pending legal-status Critical Current

Links

Abstract

PURPOSE:To obtain polyamide useful as a material in the field of electricity and machinery requiring strength and heat resistance, simply and efficiently, by subjecting directly a dicarboxylic acid as it is and a diamine to polycondensation in the presence of diphosphorus pentoxide without passing the dicarboxylic acid through chlorination process. CONSTITUTION:A dicarboxylic acid (e.g., isophthyalic acid, etc.), a diamine[preferably aromatic diamine such as bis(4-aminophenyl)ether, etc.] and diphosphorus pentoxide (preferably 1-2mol diphosphorus pentoxide based on 1mol dicarboxylic acid) are added to a reaction system, and, if necessary, an alkaline(earth) metal halide (e.g., lighium chloride, etc., preferably 0.5-1.5mol alkaline metal halide based on 1mol dicarboxylic acid) is added to it, and polycondensation is carried out preferably at 60-100 deg.C, to give the desired polyamide.

Description

【発明の詳細な説明】 本発明はポリアミドの製造方法に関し、詳しくはジカル
ボン酸とジアミ/を五酸化ニリンの存在下で直接反応さ
せることにより、効率よくしかも高分子量のポリアミド
を製造する方法に関する。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for producing a polyamide, and more particularly to a method for efficiently producing a high molecular weight polyamide by directly reacting a dicarboxylic acid and a diamine in the presence of diline pentoxide.

一般に、ポリアミド、特に芳香族環を含むポリアミドは
耐熱性にすぐれているため、各種の分野で広く用いられ
ている。このようなポリアミドは、従来ジカルボン酸の
塩化物とジアミンをアルカリの存在下で重縮合すること
によって製造されている0 しかし上記従来法ではジカルボン酸を塩化物として用い
るため、この塩化物を単離する必要があるが、このもの
は加水分解を受けやすいため、単離して保存するのが容
易でないという難点がある。
In general, polyamides, especially polyamides containing aromatic rings, have excellent heat resistance and are therefore widely used in various fields. Such polyamides have conventionally been produced by polycondensing dicarboxylic acid chloride and diamine in the presence of an alkali. However, in the above conventional method, dicarboxylic acid is used as a chloride, so this chloride must be isolated. However, it is difficult to isolate and store because it is easily hydrolyzed.

本発明の目的は、ジカルボン酸の塩化工程を経ることな
く、ジカルボン酸をそのまま直接ジアミンと反応させる
簡単な工程で、効率よくポリアミドを製造する方法を開
発することである。
An object of the present invention is to develop a method for efficiently producing polyamide through a simple process of directly reacting dicarboxylic acid with diamine without going through a dicarboxylic acid salting step.

本発明者はかかる目的を達成すべく鋭意研究を重ねた。The present inventor has conducted extensive research in order to achieve this objective.

その結果、反応系に五酸化ニリンを存在させることによ
り、目的を達成しつることを見出し、本発明を完成する
に至った。すなわち本発明は、ジカルボン酸とジアミン
を五酸化ニリンの存在下に重縮合反応させることを特徴
とするポリアミドの製造方法を提供するものである。
As a result, they discovered that the objective could be achieved by allowing niline pentoxide to exist in the reaction system, and completed the present invention. That is, the present invention provides a method for producing a polyamide, which is characterized by subjecting a dicarboxylic acid and a diamine to a polycondensation reaction in the presence of diline pentoxide.

本発明の方法で用いることのできるジカルボン酸として
は、特に制限はなく各種のものをあげることができる。
The dicarboxylic acid that can be used in the method of the present invention is not particularly limited, and various types can be used.

具体的には、アジピン酸、ピメリン酸、スペリン酸、ア
ゼライン酸、セバシン酸。
Specifically, adipic acid, pimelic acid, speric acid, azelaic acid, and sebacic acid.

フタル酸、イソフタル酸、テレフタル酸などをあげるこ
とができる。
Examples include phthalic acid, isophthalic acid, and terephthalic acid.

一方、ジアミンとしても様々なものを用いることができ
、エチレンジアミン、トリメチレンジアミン、テトラメ
チレンジアミンなどのアルキレンジアミンあるいは各種
芳香族ジアミンをあげることができる。そのうち特に1
生成物であるポリアミドの耐熱性を考慮すると一芳香族
ジアミンが好ましく具体的には次のような式で表わされ
る化合物をあげることができる。
On the other hand, various diamines can be used, including alkylene diamines such as ethylene diamine, trimethylene diamine, and tetramethylene diamine, and various aromatic diamines. Especially one of them
Considering the heat resistance of the polyamide product, monoaromatic diamines are preferred, and specific examples include compounds represented by the following formulas.

を五酸化ニリンの存在下で反応させることが必要である
。反応系に五酸化ニリンが存在しないとジカルボン酸と
ジアミンとの重縮合反応はほとんど進行しない。ここで
用いる五酸化ニリンの添加量は各種条件に応じて適宜定
めればよいが、一般的には、ジカルボン酸に対して0.
5〜3.0 倍モル、好ましくは1.0〜2.0倍モル
とすればよい。
It is necessary to react in the presence of niline pentoxide. If niline pentoxide is not present in the reaction system, the polycondensation reaction between dicarboxylic acid and diamine will hardly proceed. The amount of diline pentoxide used here may be determined as appropriate depending on various conditions, but generally it is 0.
The amount may be 5 to 3.0 times by mole, preferably 1.0 to 2.0 times by mole.

本発明の方法では、さらに必要に応じて反応系にアルカ
リ金属ハロゲン化物あるいはアルカリ土類金属ハロゲン
化物を加えることも有効である。
In the method of the present invention, it is also effective to add an alkali metal halide or alkaline earth metal halide to the reaction system, if necessary.

このアルカリ金属ハロゲン化物やアルカリ土類金属ハロ
ゲン化物は反応系における原料化合物および初期の反応
生成物の溶解性を高めるのに役立ち、その結果、反応速
度の向上ならびに得られるポリアミドの分子量の増大が
達成されることとなる。
These alkali metal halides and alkaline earth metal halides serve to increase the solubility of the raw material compounds and initial reaction products in the reaction system, thereby increasing the reaction rate and the molecular weight of the resulting polyamide. It will be done.

ここでアルカリ金属ハロゲン化物としては、塩化リチウ
ム、 j′M化カジカリウム化カリウムなどがあり、ま
たアルカリ土類金属ハロゲン化物としては環化カルシウ
ム、塩化マグネシウムなどがあげられる。なおこれらの
アルカリ金属ハロゲン化物あるいはアルカリ土類金属ハ
ロゲン化物の添加量は適宜定めればよいが、通常は原料
化合物の一つであるジカルボン酸に対して0〜2.0倍
モル、好ましくは0.5〜1.5倍モルとすればよい。
Here, examples of the alkali metal halides include lithium chloride and potassium chloride, and examples of the alkaline earth metal halides include calcium cyclide and magnesium chloride. The amount of these alkali metal halides or alkaline earth metal halides to be added may be determined as appropriate, but is usually 0 to 2.0 times the mole of dicarboxylic acid, which is one of the raw material compounds, preferably 0. The amount may be .5 to 1.5 times the mole.

本発明の方法を実施するにあたっては、反応系に前述し
たジカルボン酸、ジアミンおよび五酸化ニリンを加え、
さらに必要に応じてアルカリ金属ハロゲン化物、アルカ
リ土類金属ハロゲン化物を加えて所定温度、通常Fi、
20〜130℃、好ましくは60〜100℃にて反応を
行なえばよい。この反応、つまりジカルボン酸とジ゛ア
ミンとの重縮合反応は1無溶媒下で行なってもよいが、
通常はN−メチル−2−ピロリドン、へ午サメチルホス
ホルアミド1.ピリジン等の溶媒中にて進行する。
In carrying out the method of the present invention, the above-mentioned dicarboxylic acid, diamine and diline pentoxide are added to the reaction system,
Further, if necessary, an alkali metal halide or an alkaline earth metal halide is added and heated to a predetermined temperature, usually Fi.
The reaction may be carried out at 20-130°C, preferably 60-100°C. This reaction, that is, the polycondensation reaction between dicarboxylic acid and diamine, may be carried out without a solvent.
Usually N-methyl-2-pyrrolidone, hexamethylphosphoramide 1. Proceed in a solvent such as pyridine.

本発明の方法によれば、極めて簡略化された製造工程で
、また非常に安価な原料化合物から効率よくポリアミド
を得ることができ、しかもこのポリアミドは、重合度5
0〜200.固有粘度0.15〜0.85 di/y程
度の比較的分子量の大きいものである。
According to the method of the present invention, it is possible to efficiently obtain polyamide from very inexpensive raw material compounds through an extremely simplified production process, and furthermore, this polyamide has a polymerization degree of 5.
0-200. It has a relatively large molecular weight with an intrinsic viscosity of about 0.15 to 0.85 di/y.

従って、本発明の方法によって製造されるポリアミドは
、強度および耐熱性の要求される電機。
Therefore, the polyamide produced by the method of the present invention can be used in electrical appliances that require strength and heat resistance.

機械分野の各種の素材として有効に利用される。Effectively used as a variety of materials in the mechanical field.

次に本発明の実施例を示す。Next, examples of the present invention will be shown.

実施例1 20m/!の三角フラスコ中に1五酸化二す71.23
56 F (8,71ミリモル)とN−メチル−2−ピ
ロリドン5 mlを入れ、攪拌して溶解させた。
Example 1 20m/! Dis 1pentoxide 71.23 in an Erlenmeyer flask
56 F (8.71 mmol) and 5 ml of N-methyl-2-pyrrolidone were added and stirred to dissolve.

次いでイソフタル酸0・4820 t (2,gミリモ
ル)を加え、80℃で1時間反応させた後、塩化リチウ
ム0.245f(5,8ミリモル)を加えて80℃で1
時間反応させた。次に、ビス(4−アミノフエ−1: 
/I/ ) !−テ# 0.5803 f (2,9ミ
リモル)を加えて80℃において24時間重縮合反応さ
せた。その後、反応生成物をNaHOO3の1%水溶液
500mA’中に入れ、濾別した後、水洗し、減圧乾燥
してポリアミドを得た。この場合のポリマー収率は99
%であり、またその固有粘度(濃硫酸中0.5グ/dl
l 、  30℃にて測定。以下同じ。)は0゜28a
J/rであった。
Next, 0.4820 t (2.g mmol) of isophthalic acid was added and reacted at 80°C for 1 hour, and then 0.245f (5.8 mmol) of lithium chloride was added and reacted at 80°C for 1 hour.
Allowed time to react. Next, bis(4-aminophe-1:
/I/ )! -TE# 0.5803 f (2.9 mmol) was added and a polycondensation reaction was carried out at 80°C for 24 hours. Thereafter, the reaction product was placed in a 1% aqueous solution of NaHOO3 at 500 mA', filtered, washed with water, and dried under reduced pressure to obtain a polyamide. The polymer yield in this case is 99
%, and its intrinsic viscosity (0.5 g/dl in concentrated sulfuric acid)
l, measured at 30°C. same as below. ) is 0°28a
It was J/r.

実施例2 実施例1において、イソフタル酸の代わりにアジピン酸
2−9ミ’)モルを用いたこと以外は実施例1と同様に
してポリアミドを得た。この場合のポリマー収率は97
%であり、その固有粘度は0・85d1/2であった。
Example 2 A polyamide was obtained in the same manner as in Example 1, except that 2-9 mmol of adipic acid was used instead of isophthalic acid. The polymer yield in this case is 97
%, and its intrinsic viscosity was 0.85 d1/2.

実施例3 実施例1において、イソフタル酸の代わりにセバシン酸
2.9 ミIJモルを用いたこと以外は実施例1と同様
にしてポリアミドを得た。この場合のポリマー収率は9
6%であり、その固有粘度は0.45d1./lであっ
た。
Example 3 A polyamide was obtained in the same manner as in Example 1 except that 2.9 mmol of sebacic acid was used instead of isophthalic acid. The polymer yield in this case is 9
6%, and its intrinsic viscosity is 0.45d1. /l.

実施例4 実施例1において、イソフタル酸の代わりにアジピン酸
2.9ミリモル、ビス(4−アミノフェニル)エーテル
の代わりにビス(4−アミノフェニル)メタン2.9ミ
リモルを用いたこと以外は実施例1と同様にしてポリア
ミドを得た。この場合のポリマー収率は98%であり、
その固有粘度は0.33 di/?であった。
Example 4 Same as Example 1 except that 2.9 mmol of adipic acid was used instead of isophthalic acid and 2.9 mmol of bis(4-aminophenyl)methane was used instead of bis(4-aminophenyl) ether. A polyamide was obtained in the same manner as in Example 1. The polymer yield in this case is 98%,
Its intrinsic viscosity is 0.33 di/? Met.

実施例5 実施例1において、イソフタル酸の代わりにセパ7ン酸
2.9ミリモル、ビス(4−アミノフェニル)エーテル
の代わりにビス(4−アミノフェニル)スルホン2.9
 ミIJモルを用いたこと以外は実施例1と同様にして
ポリアミドを得た。この場合のポリマー収率は99%で
あり、その固有粘度は0.31 dl−/lであった。
Example 5 In Example 1, 2.9 mmol of sepa7ic acid was used instead of isophthalic acid, and 2.9 mmol of bis(4-aminophenyl) sulfone was used instead of bis(4-aminophenyl) ether.
A polyamide was obtained in the same manner as in Example 1 except that IJmol was used. The polymer yield in this case was 99% and its intrinsic viscosity was 0.31 dl-/l.

実施例6 実施例1において、イソフタル酸の代わりにアジピン酸
2.9ミリモル、ビス(4−アミノフェニル)エーテル
の代わりにビス(4−アミノフェニル)スルフィド2.
9ミリモルを用いたこと以外は実施例1と同様にしてポ
リアミドを得た。この場合のポリマー収率は99%であ
り一その固有粘度は0.24 d、Jl−/fであった
Example 6 In Example 1, 2.9 mmol of adipic acid was substituted for isophthalic acid, and 2.9 mmol of bis(4-aminophenyl) sulfide was substituted for bis(4-aminophenyl) ether.
A polyamide was obtained in the same manner as in Example 1 except that 9 mmol was used. The polymer yield in this case was 99% and its intrinsic viscosity was 0.24 d, Jl-/f.

特許出願人 出光興産株式会社Patent applicant: Idemitsu Kosan Co., Ltd.

Claims (2)

【特許請求の範囲】[Claims] (1)ジカルボン酸とジアミンを五酸化ニリンの存在下
に重縮合反応させることを特徴とするポリアミドの製造
方法。
(1) A method for producing polyamide, which comprises subjecting a dicarboxylic acid and a diamine to a polycondensation reaction in the presence of diline pentoxide.
(2)反応系にア、シカリ金属ノ・ロゲン化物またはア
ルカリ土類金属ノ・ロゲン化物を加える特許請求の範囲
第1項記載の方法。
(2) The method according to claim 1, in which a. silica metal chloride or alkaline earth metal chloride is added to the reaction system.
JP7301283A 1983-04-27 1983-04-27 Preparation of polyamide Pending JPS59199717A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP7301283A JPS59199717A (en) 1983-04-27 1983-04-27 Preparation of polyamide

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP7301283A JPS59199717A (en) 1983-04-27 1983-04-27 Preparation of polyamide

Publications (1)

Publication Number Publication Date
JPS59199717A true JPS59199717A (en) 1984-11-12

Family

ID=13505995

Family Applications (1)

Application Number Title Priority Date Filing Date
JP7301283A Pending JPS59199717A (en) 1983-04-27 1983-04-27 Preparation of polyamide

Country Status (1)

Country Link
JP (1) JPS59199717A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN110983364A (en) * 2019-12-20 2020-04-10 湖南七纬科技有限公司 High-hydrophilicity diaphragm for electrolyzed water and preparation method thereof

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN110983364A (en) * 2019-12-20 2020-04-10 湖南七纬科技有限公司 High-hydrophilicity diaphragm for electrolyzed water and preparation method thereof

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