JPH05310877A - Carbodiimide copolymer and its production - Google Patents

Carbodiimide copolymer and its production

Info

Publication number
JPH05310877A
JPH05310877A JP4121644A JP12164492A JPH05310877A JP H05310877 A JPH05310877 A JP H05310877A JP 4121644 A JP4121644 A JP 4121644A JP 12164492 A JP12164492 A JP 12164492A JP H05310877 A JPH05310877 A JP H05310877A
Authority
JP
Japan
Prior art keywords
group
isocyanate
solution
carbodiimide
tdi
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.)
Granted
Application number
JP4121644A
Other languages
Japanese (ja)
Other versions
JP2849001B2 (en
Inventor
Hiroshi Takayanagi
弘 高柳
Fumiaki Ichikawa
文明 市川
Hiromi Nakano
博美 中野
Teruhiro Yamaguchi
彰宏 山口
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 Toatsu Chemicals Inc
Original Assignee
Mitsui Toatsu Chemicals 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 Mitsui Toatsu Chemicals Inc filed Critical Mitsui Toatsu Chemicals Inc
Priority to JP4121644A priority Critical patent/JP2849001B2/en
Publication of JPH05310877A publication Critical patent/JPH05310877A/en
Application granted granted Critical
Publication of JP2849001B2 publication Critical patent/JP2849001B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08GMACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G18/00Polymeric products of isocyanates or isothiocyanates
    • C08G18/02Polymeric products of isocyanates or isothiocyanates of isocyanates or isothiocyanates only
    • C08G18/025Polymeric products of isocyanates or isothiocyanates of isocyanates or isothiocyanates only the polymeric products containing carbodiimide groups

Landscapes

  • Chemical & Material Sciences (AREA)
  • Health & Medical Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Medicinal Chemistry (AREA)
  • Polymers & Plastics (AREA)
  • Organic Chemistry (AREA)
  • Polyurethanes Or Polyureas (AREA)
  • Paints Or Removers (AREA)
  • Macromolecular Compounds Obtained By Forming Nitrogen-Containing Linkages In General (AREA)
  • Polymers With Sulfur, Phosphorus Or Metals In The Main Chain (AREA)

Abstract

PURPOSE:To produce a carbodiimide copolymer which is soluble in an org. solvent at a high concn. and gives a soln. with an excellent storage stability by thermally copolymerizing a specific diisocyanate component with an arom. monoisicyanate in the presence of a carbodiimidation catalyst in an org solvent. CONSTITUTION:The copolymer is produced by thermally copolymerizing 100 equivalents of a diisocyanate component comprising 5-95 equivalents of 2,4- tolylene diisocyanate and 95-5 equivalents of 2,6-tolylene diisocyanate with 10-50 equivalents of an arom. monoisocyanate in the presence of a carbodiimidation catalyst in an aprotic solvent of an amt. of 1-5 times the amt. of the diisocyanate component at 80 deg.C. The copolymer comprises 5-95 equivalent % structural units of formula I and 95-5 equivalent % structural units of formula II, has molecular ends blocked by arom. groups, and has a wt. average mol.wt. of at least 10,000.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明は、溶液貯蔵安定性に優れ
たカルボジイミド共重合体およびその製造方法に関する
ものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a carbodiimide copolymer having excellent solution storage stability and a method for producing the same.

【0002】[0002]

【従来の技術】一般に高分子量の芳香族ポリカルボジイ
ミド樹脂は、耐熱性の高い樹脂として知られている(T.
W.Campbell,K.C.Smeltz,J.Org.Chem.,28,2069(1963)。
しかし、各種溶媒に溶け難く、且つ熱流動性が悪いとい
う欠点があるために、優れた耐熱性がありながら実用的
な成形加工は困難であった。また、該文献には2,4−
トリレンジイソシアネートからカルボジイミドを合成中
に、アルコールを添加して末端をカーバメートの形状で
封止して溶媒可溶のポリカルボジイミドを製造する方法
の記載があるが、カーバメートの耐熱性が悪く、実用的
ではなかった。
2. Description of the Related Art Generally, a high molecular weight aromatic polycarbodiimide resin is known as a resin having high heat resistance (T.
W. Campbell, KCSmeltz, J. Org. Chem., 28, 2069 (1963).
However, due to the drawbacks of being difficult to dissolve in various solvents and having poor heat fluidity, it was difficult to perform practical molding while having excellent heat resistance. Moreover, in the document, 2,4-
While synthesizing carbodiimide from tolylene diisocyanate, there is a description of a method for producing a solvent-soluble polycarbodiimide by adding an alcohol and sealing the end in the form of a carbamate, but the heat resistance of the carbamate is poor and practical. Was not.

【0003】J.Appl.Polm.Sci., vol.21,1999 [1977]な
らびに特開昭51ー61599の記載によれば、上記問題点を改
善すべく、特定割合のジフェニルメタン−4,4'−ジイソ
シアネートと、分子量制御剤として有機モノイソシアネ
ートとを、不活性有機溶剤中、カルボジイミド化触媒の
存在下で反応せしめることにより、粉体として単離で
き、加熱加圧下において流動性のあるポリカルボジイミ
ドの製造方法を見い出している。しかしながら、各種溶
媒に高濃度で溶け難いために、積層板の原料となるが如
き実用的なワニス(溶液)として供することはできなか
った。
According to the description of J. Appl. Polm. Sci., Vol. 21, 1999 [1977] and JP-A-51-61599, in order to improve the above problems, a specific proportion of diphenylmethane-4,4 '. -A diisocyanate and an organic monoisocyanate as a molecular weight control agent are reacted in an inert organic solvent in the presence of a carbodiimidization catalyst to be isolated as a powder, which is a polycarbodiimide which is fluid under heat and pressure. We are finding a manufacturing method. However, since it is difficult to dissolve in various solvents at a high concentration, it cannot be provided as a practical varnish (solution) such as a raw material for a laminated plate.

【0004】近年になって、特開昭63ー161031 号公報の
記載によれば、トリレンジイソシアネートに小量のモノ
イソシアネートを添加してテトラクロロエチレン中で重
合することによりポリカルボジイミドワニス(溶液)を
得て、熱硬化性フィルムを製造しているものの、溶液の
安定性に問題があり、また使用する溶媒の使用量や濃度
が限られ、汎用性に欠くという欠点があった。
Recently, according to the description of JP-A-63-161031, a small amount of monoisocyanate is added to tolylene diisocyanate and polymerized in tetrachloroethylene to obtain a polycarbodiimide varnish (solution). Although a thermosetting film is produced, there is a problem in that the stability of the solution is problematic, and the amount and concentration of the solvent used is limited, resulting in lack of versatility.

【0005】一方、特開平2ー292316号公報では、高分子
量ポリカルボジイミド溶液の製造方法が提案されてお
り、10重量%以下の高分子量ポリカルボジイミド溶液
で3週間安定と記載されているが、10重量%以下の低
濃度ではワニスの9割以上が溶媒であるために、該ワニ
スを移動、保管するにも経済性が悪く、溶媒の除去も容
易でないという欠点のために、ワニスとしての汎用性に
乏しく、実用性でなかった。
On the other hand, Japanese Unexamined Patent Publication (Kokai) No. 2-292316 proposes a method for producing a high molecular weight polycarbodiimide solution, which describes that a high molecular weight polycarbodiimide solution of 10% by weight or less is stable for 3 weeks. At a low concentration of less than 10% by weight, more than 90% of the varnish is a solvent, so it is not economical to move and store the varnish, and it is not easy to remove the solvent. Poor and not practical.

【0006】上記従来の技術では、高濃度で溶液貯蔵安
定性のあるワニスの製造方法は未だ見出されておらず、
また特定の溶剤に対する安定性の記述はあるものの汎用
的でなく、例えば、テトラクロロエチレンで安定でもワ
ニス溶媒としてさらに一般的なトルエンには不溶である
ことが多く、汎用的な指標が見あたらなかった。
[0006] In the above conventional technique, a method for producing a varnish having a high concentration and solution storage stability has not been found yet,
In addition, although there is a description of stability with respect to a specific solvent, it is not general-purpose. For example, even if it is stable with tetrachloroethylene, it is often insoluble in toluene which is more general as a varnish solvent, and a general-purpose index was not found.

【0007】[0007]

【発明が解決しようとする課題】本発明の目的は、カル
ボジイミド結合が有する優れた耐熱性を何ら損なうこと
なく、高濃度で有機溶媒に溶解し、溶液中での貯蔵安定
性に優れたカルボジイミド重合体およびその製造方法を
提供することにある。
An object of the present invention is to dissolve a carbodiimide bond at a high concentration in an organic solvent without impairing the excellent heat resistance of the carbodiimide bond and to provide a carbodiimide polymer having excellent storage stability in a solution. An object of the present invention is to provide a united body and a manufacturing method thereof.

【0008】[0008]

【課題を解決するための手段】本発明者らは、前記課題
について鋭意検討し、本発明に至った。即ち、本発明
は、 (1) 下記式(1)(化3)で表わされる構造単位を
有する基5〜95当量部および下記式(2)(化3)で
表わされる構造単位を有する基95〜5当量部を含み、
ポリマーの分子の末端が芳香族基で封止され、かつ重量
平均分子量が1万以下であることを特徴とするカルボジ
イミド共重合体、
Means for Solving the Problems The inventors of the present invention have made extensive studies on the above-mentioned problems and have reached the present invention. That is, the present invention includes (1) a group 5 to 95 equivalent parts having a structural unit represented by the following formula (1) (Chemical formula 3) and a group 95 having a structural unit represented by the following formula (2) (Chemical formula 3) Including ~ 5 equivalent parts,
A carbodiimide copolymer characterized in that a polymer molecule end is sealed with an aromatic group and a weight average molecular weight is 10,000 or less,

【0009】[0009]

【化3】 (2) ポリマーの分子末端の芳香族基が、フェニル
基、オルソ−トリル基、メタ−トリル基、パラ−トリル
基、ジメチルフェニル基、クロロフェニル基、トリフル
オロメチルフェニル基、ナフチル基、イソプロピルフェ
ニル基およびジイソプロピルフェニル基からなる群より
選ばれた少なくとも1種である請求項1記載のカルボジ
イミド共重合体、 (3) 5〜95当量部の2,4−トリレンジイソシア
ネートおよび95〜5当量部の2,6−トリレンジイソ
シアネートを含むジイソシアネート成分の総量100当
量部に対して、10〜50当量部の芳香族モノイソシア
ネートとを、カルボジイミド化触媒の存在下、ジイソシ
アネート成分の総量の1〜5倍量の非プロトン性有機溶
媒中で80℃以上の温度で加熱重合させることを特徴と
する請求項1記載のカルボジイミド共重合体の製造方
法、 (4) 非プロトン性有機溶媒が、トルエン、キシレ
ン、パークレンおよびジオキサンからなる群より選ばれ
た少なくとも1種である請求項3記載のカルボジイミド
共重合体の製造方法、 (5) 芳香族モノイソシアネートが、フェニルイソシ
アネート、オルソ−トリルイソシアネート、メタ−トリ
ルイソシアネート、パラ−トリルイソシアネート、ジメ
チルフェニルイソシアネート、クロロフェニルイソシア
ネート、トリフルオロメチルフェニルイソシアネート、
ナフチルイソシアネート、イソプロピルフェニルイソシ
アネートおよびジイソプロピルフェニルイソシアネート
からなる群より選ばれた少なくとも1種である請求項3
記載のカルボジイミド共重合体の製造方法 および (6) 下記式(1)(化4)で表わされる構造単位を
有する基5〜95当量部および下記式(2)(化4)で
表わされる構造単位を有する基95〜5当量部を含み、
ポリマーの分子の末端が芳香族基で封止され、かつ重量
平均分子量が1万以下である請求項1記載のカルボジイ
ミド共重合体を含むことを特徴とするカルボジイミド系
ワニス。
[Chemical 3] (2) The aromatic group at the molecular end of the polymer is a phenyl group, ortho-tolyl group, meta-tolyl group, para-tolyl group, dimethylphenyl group, chlorophenyl group, trifluoromethylphenyl group, naphthyl group, isopropylphenyl group. And at least one selected from the group consisting of diisopropylphenyl groups, (3) 5 to 95 equivalent parts of 2,4-tolylene diisocyanate and 95 to 5 equivalent parts of 2. , 6-tolylene diisocyanate, relative to 100 parts by weight of the total amount of the diisocyanate component, 10 to 50 parts by weight of the aromatic monoisocyanate is added in an amount of 1 to 5 times the total amount of the diisocyanate component in the presence of the carbodiimidization catalyst. Characterized by heat-polymerizing in an aprotic organic solvent at a temperature of 80 ° C. or higher The method for producing a carbodiimide copolymer according to claim 1, (4) The carbodiimide copolymer according to claim 3, wherein the aprotic organic solvent is at least one selected from the group consisting of toluene, xylene, perkylene and dioxane. (5) Aromatic monoisocyanate is phenyl isocyanate, ortho-tolyl isocyanate, meta-tolyl isocyanate, para-tolyl isocyanate, dimethylphenyl isocyanate, chlorophenyl isocyanate, trifluoromethylphenyl isocyanate,
4. At least one selected from the group consisting of naphthyl isocyanate, isopropylphenyl isocyanate and diisopropylphenyl isocyanate.
5. Method for producing carbodiimide copolymer and (6) 5 to 95 equivalent parts of a group having a structural unit represented by the following formula (1) (chemical formula 4) and a structural unit represented by the following formula (2) (chemical formula 4) Including 95 to 5 equivalents of a group having
2. A carbodiimide-based varnish comprising the carbodiimide copolymer according to claim 1, wherein the polymer has a molecular terminal blocked with an aromatic group and a weight average molecular weight of 10,000 or less.

【0010】[0010]

【化4】 である。[Chemical 4] Is.

【0011】本発明のカルボジイミド共重合体は、2,
4−トリレンジイソシアネート(以下2,4−TDIと
略す)に由来する式(1)で表わされる構造単位を有す
る基と、2,6−トリレンジイソシアネート(以下2,
6−TDIと略す)に由来する式(2)で表わされる構
造単位を有する基とを含み、成分の組成比が小さいほど
よりアモルファスになるにも拘らずカルボジイミド結合
の自己架橋温度は殆ど低下しないので、成分の組成比を
適宜選択することにより、所望の加熱時の流動性と溶融
安定幅を有するカルボジイミド共重合体を得ることがで
きる。さらに、ポリマー末端が芳香族基で封止され、分
子量が規制されているので、分子量を適宜選択すること
により、溶液として所望の粘性を有するカルボジイミド
共重合体を得ることができる。
The carbodiimide copolymer of the present invention comprises 2,
A group having a structural unit represented by the formula (1) derived from 4-tolylene diisocyanate (hereinafter abbreviated as 2,4-TDI), and 2,6-tolylene diisocyanate (hereinafter 2,
6-TDI) and a group having a structural unit represented by the formula (2) derived from 6-TDI), and the self-crosslinking temperature of the carbodiimide bond hardly decreases even though the composition becomes smaller as the composition ratio of the components becomes smaller. Therefore, by appropriately selecting the composition ratio of the components, a carbodiimide copolymer having a desired fluidity during heating and a melt stability width can be obtained. Furthermore, since the polymer terminal is sealed with an aromatic group and the molecular weight is regulated, a carbodiimide copolymer having a desired viscosity can be obtained as a solution by appropriately selecting the molecular weight.

【0012】本発明のカルボジイミド共重合体は、ベン
ゼン、トルエン、キシレン、パークレン、ジオキサン、
ジメチルフォルムアミド、ジメチルアセトアミド、N−
メチルピロリドン等の汎用性溶媒に良好に溶解し、特に
溶けにくいトルエン溶媒に対しても15重量%以上溶解
し、しかも室温でゲル化せず、溶液貯蔵安定性に優れる
ことを特徴とするものであり、少なくとも1カ月間以
上、通常は3カ月間以上ゲル化せずに溶液で貯蔵でき
る。また、トルエン、キシレン、パークレン、ジオキサ
ン等の非プロトン性有機溶媒に本発明のカルボジイミド
共重合体を15重量%以上含有する溶液は、所定の濃度
で貯蔵でき、用途に応じて適宜希釈して使用できる。こ
のように、本発明のカルボジイミド共重合体は、従来の
ポリカルボジイドの高濃度で溶液貯蔵安定性が悪いとい
う欠点を克服し、積層板、フィルム等、種々の成形物の
製造に好適なワニスの提供を可能にしたものである。
The carbodiimide copolymer of the present invention comprises benzene, toluene, xylene, perkylene, dioxane,
Dimethylformamide, dimethylacetamide, N-
It is characterized by excellent solubility in a general-purpose solvent such as methylpyrrolidone, 15% by weight or more in a toluene solvent which is particularly difficult to dissolve, does not gel at room temperature, and has excellent solution storage stability. Yes, it can be stored in solution for at least 1 month or longer, usually 3 months or longer without gelation. Further, a solution containing 15% by weight or more of the carbodiimide copolymer of the present invention in an aprotic organic solvent such as toluene, xylene, perkylene, or dioxane can be stored at a predetermined concentration, and can be appropriately diluted before use. it can. As described above, the carbodiimide copolymer of the present invention overcomes the disadvantage that the solution storage stability is poor at high concentrations of conventional polycarbodides, and is a varnish suitable for production of various molded products such as laminates and films. It is possible to provide.

【0013】以下、構成の詳細な説明をする。本発明方
法において使用しうる、2,4−TDI、および2,6
−TDIは、工業的に入手容易な製品をそのまま、ある
いは混合して、所定の成分の組成比として利用できる。
The configuration will be described in detail below. 2,4-TDI and 2,6 which can be used in the method of the present invention
-TDI can be used as a composition ratio of predetermined components as it is or as a mixture of industrially easily available products.

【0014】本発明方法において、2,4−TDIと
2,6−TDIの使用割合は、全量を100モル部とし
た場合、2,4−TDI5〜95モル部と、2,6−T
DI95〜5モル部を使用することが好ましく、さらに
は、2,4−TDI60〜90モル部と、2,6−TD
I40〜10モル部を使用することがより好ましく、こ
の場合カルボジイミド共重合体を30重量%以上含有す
る、より高濃度の溶液を得ることができ、原料も市販の
安価なTDI混合物をそのまま使用できるので、工業的
製法としては、より有用である。2,4−TDI、また
は2,6−TDIを95モル部以上使用すると重合液中
で析出し易くなり、安定な高濃度溶液が得られず、実用
的でなくなる。
In the method of the present invention, the proportions of 2,4-TDI and 2,6-TDI used are, when the total amount is 100 mol parts, 2,4-TDI 5 to 95 mol parts and 2,6-TDI.
It is preferable to use 95 to 5 parts by mol of DI, and further 60 to 90 parts by mol of 2,4-TDI and 2,6-TD.
It is more preferable to use I40 to 10 parts by mol, and in this case, a higher concentration solution containing 30% by weight or more of a carbodiimide copolymer can be obtained, and a commercially available inexpensive TDI mixture can be used as it is as a raw material. Therefore, it is more useful as an industrial production method. When 2,4-TDI or 2,6-TDI is used in an amount of 95 parts by mole or more, precipitation tends to occur in the polymerization solution, and a stable high-concentration solution cannot be obtained, which is not practical.

【0015】この方法において、分子量制御剤として各
種芳香族モノイソシアネートが使用できる。この有機モ
ノイソシアネートとしては、フェニルイソシアネート、
(オルソ、メタ、パラ)−トリルイソシアネート、ジメ
チルフェニルイソシアネート、クロロフェニルイソシア
ネート、トリフルオロメチルフェニルイソシアネート、
ナフチルイソシアネート、イソプロピルフェニルイソシ
アネート、ジイソプロピルフェニルイソシアネート等を
例示することができる。本発明の方法においては、特に
フェニルイソシアネートの使用が望ましく、工業的にも
容易に入手可能である。 この分子量制御剤である芳香
族モノイソシアネートの使用量は、MDI100モル部
に対し10〜50モル部使用できる。10モル部未満で
は、重合度が高すぎて溶媒に溶け難くなり、溶液の貯蔵
安定性も悪くなる。50モル部を越えると、イソシアネ
ートが一部未反応で残り、フェニルイソシアネートから
の副生物であるジフェニルカルボジイミドが多く生成す
るので耐熱性の劣ったポリカルボジイミドしか得られな
い。
In this method, various aromatic monoisocyanates can be used as the molecular weight control agent. As the organic monoisocyanate, phenyl isocyanate,
(Ortho, meta, para) -tolyl isocyanate, dimethylphenyl isocyanate, chlorophenyl isocyanate, trifluoromethylphenyl isocyanate,
Naphthyl isocyanate, isopropyl phenyl isocyanate, diisopropyl phenyl isocyanate, etc. can be illustrated. In the method of the present invention, the use of phenyl isocyanate is particularly desirable, and it is easily available industrially. The amount of the aromatic monoisocyanate used as the molecular weight control agent can be 10 to 50 parts by mol based on 100 parts by mol of MDI. If it is less than 10 parts by mole, the degree of polymerization is too high to make it difficult to dissolve in a solvent, and the storage stability of the solution becomes poor. If the amount exceeds 50 parts by mole, some of the isocyanate remains unreacted and a large amount of diphenylcarbodiimide, which is a by-product from phenylisocyanate, is produced, so that only polycarbodiimide having poor heat resistance can be obtained.

【0016】尚、イソシアネートのカルボジイミド化を
促進する触媒には、種々のものが使用できるが、1−フ
ェニル−2−ホスホレン−1−オキシド、 3−メチル
−1−フェニル−2−ホスホレン−1−オキシド、1−
フェニル−2−ホスホレン−1−スルフィド、1−エチ
ル−2−ホスホレン−1−オキシド、1−エチル−3−
メチル−2−ホスホレン−1−オキシドや、これらの相
当する異性体、3−ホスホレン類が良好である。触媒量
は、イソシアネート全量に対し0.01〜1%の間で使
用できる。
Various catalysts can be used as the catalyst for promoting the carbodiimidization of isocyanate, but 1-phenyl-2-phospholen-1-oxide and 3-methyl-1-phenyl-2-phospholen-1- Oxide, 1-
Phenyl-2-phosphorene-1-sulfide, 1-ethyl-2-phosphorene-1-oxide, 1-ethyl-3-
Methyl-2-phospholen-1-oxide, the corresponding isomers thereof, and 3-phosphorenes are preferable. The catalyst amount can be used in the range of 0.01 to 1% based on the total amount of isocyanate.

【0017】本発明の方法で使用できる重合用の非プロ
トン性有機溶媒は、ベンゼン、トルエン、エチルベンゼ
ン、クメン、キシレン等の芳香族炭化水素溶媒、トリク
レン、パークレン等のハロゲン化炭化水素溶媒、もしく
は、ジオキサン、ジグライム等のエーテル類溶媒、その
他N−メチルピロリドン、ジメチルアセトアミド、ジメ
チルフォルムアミド、ジメチルイミダゾリジノン等が挙
げられるが、溶媒の沸点と反応温度、重合溶液の実用性
を考慮した場合、トルエンを使用することが好ましい。
The aprotic organic solvent for polymerization which can be used in the method of the present invention is an aromatic hydrocarbon solvent such as benzene, toluene, ethylbenzene, cumene or xylene, a halogenated hydrocarbon solvent such as trichlene or perkylene, or Dioxane, ether solvents such as diglyme, and other N-methylpyrrolidone, dimethylacetamide, dimethylformamide, dimethylimidazolidinone and the like, but when considering the boiling point of the solvent and the reaction temperature, the practicality of the polymerization solution, toluene Is preferably used.

【0018】重合は、使用する非プロトン性有機溶媒の
沸点付近の温度で行うことが好ましく、具体的には約8
0℃から150℃の範囲の温度、特に約100℃から1
50℃の範囲の温度で反応を行うことが、反応時間の短
縮および分子量分布の狭いコポリマーが得られるという
点でより好ましい。80℃未満で重合を行なうとイソシ
アネートが完全に反応せずに残り、重合溶液の貯蔵安定
性を損なう。一方、150℃を越えた温度で重合すると
熱架橋の副反応が起こり、ゲル化する場合がある。 重
合の反応時間の終点は、重合溶液をサンプリングして、
IR分析し、残存イソシアネートが0.5%を切る点と
する。残存イソシアネートが0.5%以上あると、溶液
貯蔵中のゲル化を促進し、貯蔵安定性を損なう。
The polymerization is preferably carried out at a temperature near the boiling point of the aprotic organic solvent used, specifically about 8
Temperatures in the range 0 ° C to 150 ° C, especially about 100 ° C to 1
It is more preferable to carry out the reaction at a temperature in the range of 50 ° C. from the viewpoint of shortening the reaction time and obtaining a copolymer having a narrow molecular weight distribution. When the polymerization is carried out at a temperature lower than 80 ° C., the isocyanate does not completely react and remains, impairing the storage stability of the polymerization solution. On the other hand, if the polymerization is carried out at a temperature higher than 150 ° C., a side reaction of thermal crosslinking may occur and gelation may occur. The end point of the reaction time of the polymerization, sampling the polymerization solution,
IR analysis is performed, and the point where the residual isocyanate falls below 0.5% is set. If the residual isocyanate content is 0.5% or more, gelation during solution storage is promoted and storage stability is impaired.

【0019】本発明の方法において得られるカルボジイ
ミド共重合体は重合溶液のままワニスとして使用する。
さらに必要とあらば、そのまま溶媒を60℃以下で減圧
除去するか、ヘキサン、ヘプタン等の飽和炭化水素系の
貧溶媒中で析出、単離して使用できる。本発明のカルボ
ジイミド共重合体の使用にあたっては、活性水素化合物
や多重結合化合物等の硬化剤、炭素繊維やガラス繊維等
の充填剤、酢酸エチルやメチルエチルケトン等の希釈溶
媒、などの添加剤を混合してもよい。
The carbodiimide copolymer obtained by the method of the present invention is used as a varnish as it is as a polymerization solution.
If necessary, the solvent can be directly removed under reduced pressure at 60 ° C. or lower, or can be precipitated and isolated in a saturated hydrocarbon poor solvent such as hexane or heptane for use. In using the carbodiimide copolymer of the present invention, a curing agent such as an active hydrogen compound or a multiple bond compound, a filler such as carbon fiber or glass fiber, a diluent solvent such as ethyl acetate or methyl ethyl ketone, and an additive are mixed. May be.

【0020】本発明の方法の実施態様は、以下のとおり
である。2,4−TDI、2,6−TDI、芳香族モノ
イソシアネート、非プロトン性有機溶媒を重合容器に装
入する。撹はんを行い、均一溶液になった後、非プロト
ン性有機溶媒に溶かしたカルボジイミド化触媒を添加
し、60℃から150℃の温度まで昇温し、この温度で
3時間から8時間重合後、室温まで冷却させカルボジイ
ミド共重合体溶液を得る。このようにして得られたカル
ボジイミド共重合体は溶液のままワニスとして使用す
る。さらに必要とあらば、60℃以下で溶媒を減圧除去
して使用する。このカルボジイミド共重合体は、分子量
約千から約1万の間にあって、コポリマーの5%熱分解
温度は400℃以上有り、トルエンに15重量%以上溶
解し、室温で一ヶ月間以上ゲル化しない特性を有するも
のであり、ワニスとして、積層板、フィルム、複合剤、
繊維処理剤等の、種々の成形物の製造に適したカルボジ
イミド共重合体が得られる。
An embodiment of the method of the present invention is as follows. Charge 2,4-TDI, 2,6-TDI, aromatic monoisocyanate, aprotic organic solvent to a polymerization vessel. After stirring to form a uniform solution, a carbodiimidization catalyst dissolved in an aprotic organic solvent was added, the temperature was raised from 60 ° C to 150 ° C, and polymerization was carried out at this temperature for 3 to 8 hours. Then, it is cooled to room temperature to obtain a carbodiimide copolymer solution. The carbodiimide copolymer thus obtained is used as a varnish as a solution. If necessary, the solvent is removed under reduced pressure at 60 ° C or lower before use. This carbodiimide copolymer has a molecular weight of about 1,000 to about 10,000, has a 5% thermal decomposition temperature of 400 ° C. or higher, dissolves 15% by weight or more in toluene, and does not gel at room temperature for one month or longer. As a varnish, a laminate, a film, a composite agent,
A carbodiimide copolymer suitable for production of various molded products such as a fiber treating agent can be obtained.

【0021】[0021]

【実施例】次に本発明の実施例を示して、さらに具体的
に説明する。ただし、本発明はこれらの実施例に限定さ
れるものではない。また、実施例および比較例において
得られたコポリマーおよび溶液の分析、物性値は以下の
方法で測定した。
EXAMPLES Next, examples of the present invention will be shown and described more specifically. However, the present invention is not limited to these examples. Further, the analysis and physical property values of the copolymers and solutions obtained in Examples and Comparative Examples were measured by the following methods.

【0022】平均分子量および分子量分布:コポリマー
溶液をN−メチルピロリドンで希釈し、GPCを用い
て、分子量分布曲線のカーブを測定し、ポリスチレン、
スタンダードによって重量平均分子量、および分子量分
布を得た。 固形分濃度:コポリマー溶液をガラスシャーレ上に薄く
展開し、130℃で窒素気流下で恒量になるまで乾燥し
て溶媒を除去した後、固形分を秤量し、濃度を換算し
た。 5%分解温度:コポリマー溶液をガラスシャーレ上に薄
く展開し、130℃で乾燥して溶媒を除去した後、熱重
量分析装置(TGA)を用いて空気中、昇温速度10℃
/minで、ポリマーの5%重量損失温度を測定した。 トルエン溶液貯蔵安定性:コポリマーの15重量%トル
エン溶液を透明ガラスビンに入れ、暗所内室温(25
℃)で貯蔵し、定期的に溶液を振り混ぜ、ゲル化の有
無、外観変化を調べた。 重合溶液貯蔵安定性:重合溶液を透明ガラスビンに入れ
上記検査と同様に安定性を調べた。 残存イソシアネート検査:重合溶液の一部を採取し、岩
塩板に挟んで赤外吸収スペクトル測定装置(IR)を用
いて、イソシアネートの特性吸収を定量し、仕込原料イ
ソシアネート量を基準にして、結果を%で表わした(検
出限界0.4%)。
Average molecular weight and molecular weight distribution: The copolymer solution was diluted with N-methylpyrrolidone, the curve of the molecular weight distribution curve was measured using GPC, polystyrene,
The weight average molecular weight and the molecular weight distribution were obtained by the standard. Solid content concentration: The copolymer solution was thinly spread on a glass petri dish, dried at 130 ° C. under a nitrogen stream until a constant weight was obtained to remove the solvent, and then the solid content was weighed to calculate the concentration. 5% decomposition temperature: The copolymer solution was spread thinly on a glass petri dish, dried at 130 ° C to remove the solvent, and then heated in air using a thermogravimetric analyzer (TGA) at a heating rate of 10 ° C.
The 5% weight loss temperature of the polymer was measured in / min. Toluene solution storage stability: A 15 wt% toluene solution of the copolymer was placed in a transparent glass bottle and stored in the dark at room temperature (25
C.) and periodically shaken the solution, and examined for gelation and appearance change. Polymerization solution storage stability: The polymerization solution was placed in a transparent glass bottle and stability was examined in the same manner as in the above test. Residual isocyanate inspection: A part of the polymerization solution was sampled, sandwiched between rock salt plates, and the infrared absorption spectrum measuring device (IR) was used to quantify the characteristic absorption of isocyanate. % (Detection limit 0.4%).

【0023】実施例1 攪拌機、温度計、冷却コンデンサーを備えた300ml セパ
ラブルフラスコ中に、2,4−TDI80モル部と2,
6−TDI20モル部の混合物(商品名;TDI 8
0、三井東圧化学(株)製)22.4g(0.128モル)、フェ
ニルイソシアネート(PhI)2.20g (0.0756モル, T
DI 100モル部に対し14モル部)、乾燥トルエン110 ml
を窒素雰囲気中に装入し、攪拌しながら均一に溶解し
た。次に、重合溶媒と同じ溶媒1mlに希釈した3−メチ
ル−1−フェニル−2−ホスホレン−1−オキシド触媒
0.0913g (0.000475モル、0.37%/TDI)を添加し、攪拌
しながら内温を 110℃まで昇温した。昇温とともに二酸
化炭素の発生が多くなり、内温が80℃をこえたあたりか
ら特に激しく二酸化炭素の発生が観察された。内温が11
0 ℃に達してから 3.5時間重合させた。重合終了後、室
温まで冷却し、透明なカルボジイミド共重合体溶液を得
た。溶液中に残存イソシアネートは検出されなかった
このカルボジイミド共重合体の分析、物性値測定を行な
ったところ、 固形分(%) 15 平均分子量(Mw) 3000 分子量分布(Mw/Mn) 2.3 5%分解温度(℃) 460 溶液安定性 トルエン溶液貯蔵安定性、重合溶
液貯蔵安定性共に、3ヶ月間ゲル化せず。 という結果が得られた。
Example 1 In a 300 ml separable flask equipped with a stirrer, a thermometer and a cooling condenser, 80 parts by mole of 2,4-TDI and 2,
A mixture of 20 parts by mol of 6-TDI (trade name; TDI 8
0, manufactured by Mitsui Toatsu Chemicals, Inc. 22.4 g (0.128 mol), phenylisocyanate (PhI) 2.20 g (0.0756 mol, T)
14 mol parts to 100 mol parts of DI), 110 ml of dry toluene
Was charged in a nitrogen atmosphere and uniformly dissolved with stirring. Next, 3-methyl-1-phenyl-2-phosphorene-1-oxide catalyst diluted in 1 ml of the same solvent as the polymerization solvent
0.0913 g (0.000475 mol, 0.37% / TDI) was added, and the internal temperature was raised to 110 ° C. with stirring. The generation of carbon dioxide increased as the temperature increased, and carbon dioxide generation was observed particularly violently when the internal temperature exceeded 80 ° C. Inner temperature is 11
After reaching 0 ° C, polymerization was carried out for 3.5 hours. After completion of the polymerization, the solution was cooled to room temperature to obtain a transparent carbodiimide copolymer solution. No residual isocyanate was detected in the solution
When this carbodiimide copolymer was analyzed and the physical properties were measured, solid content (%) 15 average molecular weight (Mw) 3000 molecular weight distribution (Mw / Mn) 2.3 5% decomposition temperature (° C) 460 solution stability toluene solution storage Both stability and storage stability of polymerization solution did not gel for 3 months. The result was obtained.

【0024】比較例1 フェニルイソシアネートを添加しない以外は、実施例1
と同様に反応させた結果、重合中にゲル化し、攪拌がで
きなくなった。
Comparative Example 1 Example 1 except that no phenyl isocyanate was added.
As a result of reacting in the same manner as above, gelation occurred during the polymerization and stirring became impossible.

【0025】比較例2 フェニルイソシアネートをTDI100モル部に対し、
5モル部使用する以外は実施例1と同様に重合させた結
果、透明なカルボジイミド共重合体溶液を得たが、3日
以内に重合溶液はゲル化した。
Comparative Example 2 Phenylisocyanate was added to 100 parts by mole of TDI.
Polymerization was performed in the same manner as in Example 1 except that 5 parts by mole was used, and as a result, a transparent carbodiimide copolymer solution was obtained, but the polymerization solution gelled within 3 days.

【0026】比較例3 TDI混合物の代わりに、2,4−TDIを使用する以
外は実施例1と同様に重合させた結果、透明なカルボジ
イミド共重合体溶液を得たが、3日以内に重合溶液でコ
ポリマーの一部が析出した。
Comparative Example 3 Polymerization was carried out in the same manner as in Example 1 except that 2,4-TDI was used instead of the TDI mixture, and as a result, a transparent carbodiimide copolymer solution was obtained, but the polymerization was carried out within 3 days. A portion of the copolymer precipitated out of solution.

【0027】実施例2 攪拌機、温度計、冷却コンデンサーを備えた500ml セパ
ラブルフラスコ中に、2,4−TDI80モル部と2,
6−TDI20モル部の混合物(商品名;TDI 8
0、三井東圧化学(株)製)92.1g(0.529モル) 、フェ
ニルイソシアネート9.00g (0.0756モル, TDI 100モ
ル部に対し14モル部) 、乾燥トルエン202mlを窒素雰囲
気中に装入し、攪拌しながら均一に溶解した。次に、重
合溶媒と同じ溶媒5mlに希釈した3−メチル−1−フェ
ニル−2−ホスホレン−1−オキシド触媒 0.359g(0.0
0187モル、0.35%/TDI)を添加し、攪拌しながら内温を
110℃まで昇温した。昇温とともに二酸化炭素の発生が
多くなり、内温が80℃をこえたあたりから特に激しく二
酸化炭素の発生が観察された。内温が 110℃に達してか
ら3.5 時間重合させた。重合終了後、室温まで冷却し、
透明なカルボジイミド共重合体溶液を得た。溶液中に残
存イソシアネートは検出されなかった。このカルボジイ
ミド共重合体の分析、物性値測定を行なったところ、 固形分(%) 30 平均分子量(Mw) 3200 分子量分布(Mw/Mn) 3.1 5%分解温度(℃) 450 溶液安定性 トルエン溶液貯蔵安定性、重合溶
液貯蔵安定性共に、3ヶ月間ゲル化せず。 という結果が得られた。
Example 2 In a 500 ml separable flask equipped with a stirrer, thermometer and cooling condenser, 80 parts by mole of 2,4-TDI and 2,
A mixture of 20 parts by mol of 6-TDI (trade name; TDI 8
0, Mitsui Toatsu Chemicals Co., Ltd. 92.1 g (0.529 mol), phenylisocyanate 9.00 g (0.0756 mol, 14 mol parts to 100 mol parts of TDI), 202 ml of dry toluene were charged in a nitrogen atmosphere and stirred. While uniformly dissolving. Next, 0.359 g (0.03 g) of 3-methyl-1-phenyl-2-phosphorene-1-oxide catalyst diluted with 5 ml of the same solvent as the polymerization solvent.
(0187 mol, 0.35% / TDI) was added and the internal temperature was adjusted while stirring.
The temperature was raised to 110 ° C. The generation of carbon dioxide increased as the temperature increased, and carbon dioxide generation was observed particularly violently when the internal temperature exceeded 80 ° C. Polymerization was carried out for 3.5 hours after the internal temperature reached 110 ° C. After the completion of polymerization, cool to room temperature,
A transparent carbodiimide copolymer solution was obtained. No residual isocyanate was detected in the solution. Analysis of this carbodiimide copolymer and measurement of physical properties revealed that solid content (%) 30 average molecular weight (Mw) 3200 molecular weight distribution (Mw / Mn) 3.1 5% decomposition temperature (° C) 450 solution stability toluene solution storage Both stability and storage stability of polymerization solution did not gel for 3 months. The result was obtained.

【0028】実施例3 攪拌機、温度計、冷却コンデンサーを備えた100ml セパ
ラブルフラスコ中に、2,4−TDI80モル部と2,
6−TDI20モル部の混合物(商品名;TDI 8
0、三井東圧化学(株)製)22.1g(0.127モル) 、フェ
ニルイソシアネート2.13g (0.0179モル, TDI 100モ
ル部に対し、14モル部 )、乾燥トルエン48mlを窒素雰囲
気中に装入し、攪拌しながら均一に溶解した。次に、重
合溶媒と同じ溶媒1mlに希釈した3-メチル−1−フェニ
ル−2−ホスホレン−1−オキシド触媒0.0122g (0.00
0063モル、0.05%/TDI)を添加し、攪拌しながら内温を
110℃まで昇温した。昇温とともに二酸化炭素の発生が
多くなり、内温が80℃をこえたあたりから特に激しく二
酸化炭素の発生が観察された。内温が 110℃に達してか
ら7.1 時間重合させた。重合終了後、室温まで冷却し、
透明なカルボジイミド共重合体溶液を得た。溶液中に残
存イソシアネートは検出されなかった。このカルボジイ
ミド共重合体の分析、物性値測定を行なったところ、 固形分(%) 30 平均分子量(Mw) 3900 分子量分布(Mw/Mn) 3.5 5%分解温度(℃) 450 溶液安定性 トルエン溶液貯蔵安定性、重合溶
液貯蔵安定性共に、3ヶ月間ゲル化せず。 という結果が得られた。
Example 3 In a 100 ml separable flask equipped with a stirrer, a thermometer and a cooling condenser, 80 parts by mole of 2,4-TDI and 2,
A mixture of 20 parts by mol of 6-TDI (trade name; TDI 8
0, Mitsui Toatsu Chemical Co., Ltd. 22.1 g (0.127 mol), 2.13 g of phenyl isocyanate (0.0179 mol, 14 mol parts to 100 mol parts of TDI), 48 ml of dry toluene were charged in a nitrogen atmosphere, It was uniformly dissolved with stirring. Next, 0.0122 g (0.002 g) of 3-methyl-1-phenyl-2-phosphorene-1-oxide catalyst diluted in 1 ml of the same solvent as the polymerization solvent
0063 mol, 0.05% / TDI) was added and the internal temperature was adjusted while stirring.
The temperature was raised to 110 ° C. The generation of carbon dioxide increased as the temperature increased, and carbon dioxide generation was observed particularly violently when the internal temperature exceeded 80 ° C. After the internal temperature reached 110 ° C, polymerization was performed for 7.1 hours. After the completion of polymerization, cool to room temperature,
A transparent carbodiimide copolymer solution was obtained. No residual isocyanate was detected in the solution. When this carbodiimide copolymer was analyzed and the physical properties were measured, solid content (%) 30 average molecular weight (Mw) 3900 molecular weight distribution (Mw / Mn) 3.5 5% decomposition temperature (° C) 450 solution stability toluene solution storage Both stability and storage stability of polymerization solution did not gel for 3 months. The result was obtained.

【0029】実施例4 攪拌機、温度計、冷却コンデンサーを備えた100ml セパ
ラブルフラスコ中に、2,4−TDI80モル部と2,
6−TDI20モル部の混合物(商品名;TDI 8
0、三井東圧化学(株)製)22.8g(0.131モル )、フェ
ニルイソシアネート3.15g (0.0264モル, TDI 100モ
ル部に対し、20モル部) 、乾燥トルエン52mlを窒素雰囲
気中に装入し、攪拌しながら均一に溶解した。次に、重
合溶媒と同じ溶媒1mlに希釈した3−メチル−1−フェ
ニル−2−ホスホレン−1−オキシド触媒0.0128g (0.
000066モル、0.05%/TDI)を添加し、攪拌しながら内温
を110 ℃まで昇温した。昇温とともに二酸化炭素の発生
が多くなり、内温が80℃をこえたあたりから特に激しく
二酸化炭素の発生が観察された。内温が110 ℃に達して
から7 時間重合させた。重合終了後、室温まで冷却し、
透明なカルボジイミド共重合体溶液を得た。溶液中に残
存イソシアネートは検出されなかった。このカルボジイ
ミド共重合体の分析、物性値測定を行なったところ、 固形分(%) 30 平均分子量(Mw) 2800 分子量分布(Mw/Mn) 3.0 5%分解温度(℃) 440 溶液安定性 トルエン溶液貯蔵安定性、重合溶
液貯蔵安定性共に、3ヶ月間ゲル化せず。 という結果が得られた。
Example 4 80 parts by mole of 2,4-TDI and 2, in a 100 ml separable flask equipped with a stirrer, a thermometer and a cooling condenser.
A mixture of 20 parts by mol of 6-TDI (trade name; TDI 8
0, Mitsui Toatsu Chemical Co., Ltd.) 22.8 g (0.131 mol), phenylisocyanate 3.15 g (0.0264 mol, 20 mol parts to 100 mol parts of TDI), 52 ml of dry toluene were charged in a nitrogen atmosphere, It was uniformly dissolved with stirring. Next, 0.0128 g of 3-methyl-1-phenyl-2-phosphorene-1-oxide catalyst diluted with 1 ml of the same solvent as the polymerization solvent (0.
000066 mol, 0.05% / TDI) was added, and the internal temperature was raised to 110 ° C. with stirring. The generation of carbon dioxide increased as the temperature increased, and carbon dioxide generation was observed particularly violently when the internal temperature exceeded 80 ° C. Polymerization was carried out for 7 hours after the internal temperature reached 110 ° C. After the completion of polymerization, cool to room temperature,
A transparent carbodiimide copolymer solution was obtained. No residual isocyanate was detected in the solution. When this carbodiimide copolymer was analyzed and the physical properties were measured, solid content (%) 30 average molecular weight (Mw) 2800 molecular weight distribution (Mw / Mn) 3.0 5% decomposition temperature (° C) 440 solution stability toluene solution storage Both stability and storage stability of polymerization solution did not gel for 3 months. The result was obtained.

【0030】実施例5 攪拌機、温度計、冷却コンデンサーを備えた 500mlセパ
ラブルフラスコ中に、2,4−TDI65モル部と2,
6−TDI35モル部の混合物(商品名;TDI 6
5、三井東圧化学(株)製)91.3g(0.524モル) 、フェ
ニルイソシアネート8.91g (0.0748モル, TDI 100モ
ル部に対し、14モル部) 、乾燥トルエン200 mlを窒素雰
囲気中に装入し、攪拌しながら均一に溶解した。次に、
重合溶媒と同じ溶媒6mlに希釈した3−メチル−1−フ
ェニル−2−ホスホレン−1−オキシド触媒 0.350g
(0.00182モル、0.35%/TDI)を添加し、攪拌しながら内
温を110℃まで昇温した。昇温とともに二酸化炭素の発
生が多くなり、内温が80℃をこえたあたりから特に激し
く二酸化炭素の発生が観察された。内温が 110℃に達し
てから7時間重合させた。重合終了後、室温まで冷却
し、透明なカルボジイミド共重合体溶液を得た。溶液中
に残存イソシアネートは検出されなかった。このカルボ
ジイミド共重合体の分析、物性値測定を行なったとこ
ろ、 固形分(%) 30 平均分子量(Mw) 3100 分子量分布(Mw/Mn) 3.3 5%分解温度(℃) 440 溶液安定性 トルエン溶液貯蔵安定性、重合溶
液貯蔵安定性共に、3ヶ月間ゲル化せず。 という結果が得られた。
Example 5 In a 500 ml separable flask equipped with a stirrer, a thermometer and a cooling condenser, 65 parts by mole of 2,4-TDI and 2,
A mixture of 35 parts by mol of 6-TDI (trade name: TDI 6
5. Mitsui Toatsu Chemicals Co., Ltd. 91.3 g (0.524 mol), phenylisocyanate 8.91 g (0.0748 mol, 14 mol parts to 100 mol parts of TDI), 200 ml of dry toluene were charged in a nitrogen atmosphere. , Dissolved uniformly while stirring. next,
0.350 g of 3-methyl-1-phenyl-2-phosphorene-1-oxide catalyst diluted in 6 ml of the same solvent as the polymerization solvent
(0.00182 mol, 0.35% / TDI) was added, and the internal temperature was raised to 110 ° C. with stirring. The generation of carbon dioxide increased as the temperature increased, and carbon dioxide generation was observed particularly violently when the internal temperature exceeded 80 ° C. Polymerization was carried out for 7 hours after the internal temperature reached 110 ° C. After completion of the polymerization, the solution was cooled to room temperature to obtain a transparent carbodiimide copolymer solution. No residual isocyanate was detected in the solution. Analysis of this carbodiimide copolymer and measurement of physical properties revealed that solid content (%) 30 average molecular weight (Mw) 3100 molecular weight distribution (Mw / Mn) 3.3 5% decomposition temperature (° C) 440 solution stability toluene solution storage Both stability and storage stability of polymerization solution did not gel for 3 months. The result was obtained.

【0031】実施例6 攪拌機、温度計、冷却コンデンサーを備えた100ml セパ
ラブルフラスコ中に、2,4−TDI80モル部と2,
6−TDI20モル部の混合物(商品名;TDI 8
0、三井東圧化学(株)製)22.5g(0.129モル) 、フェ
ニルイソシアネート2.17g(0.01822モル, TDI 100モ
ル部に対し、14モル部) 、乾燥パークレン49 ml を窒素
雰囲気中に装入し、攪拌しながら均一に溶解した。次
に、重合溶媒と同じ溶媒1mlに希釈した3−メチル−1
−フェニル−2−ホスホレン−2−オキシド触媒0.0125
g (0.000065モル、0.05%/TDI)を添加し、攪拌しなが
ら内温を110℃まで昇温した。昇温とともに二酸化炭素
の発生が多くなり、内温が80℃をこえたあたりから特に
激しく二酸化炭素の発生が観察された。内温が 110℃に
達してから7時間重合させた。重合終了後、室温まで冷
却し、透明なカルボジイミド共重合体溶液を得た。溶液
中に残存イソシアネートは微量検出されたが、0.4 %以
下であった。このカルボジイミド共重合体の分析、物性
値測定を行なったところ、 固形分(%) 19 平均分子量(Mw) 2300 分子量分布(Mw/Mn) 2.4 5%分解温度(℃) 435 溶液安定性 トルエン溶液貯蔵安定性、重合溶
液貯蔵安定性共に、1ヶ月間ゲル化せず。 という結果が得られた。
Example 6 In a 100 ml separable flask equipped with a stirrer, thermometer and cooling condenser, 80 parts by mole of 2,4-TDI and 2,
A mixture of 20 parts by mol of 6-TDI (trade name; TDI 8
0, Mitsui Toatsu Chemical Co., Ltd.) 22.5 g (0.129 mol), phenylisocyanate 2.17 g (0.01822 mol, 14 mol parts to 100 mol parts of TDI), dry Perkren 49 ml was charged in a nitrogen atmosphere. , Dissolved uniformly while stirring. Next, 3-methyl-1 diluted in 1 ml of the same solvent as the polymerization solvent.
-Phenyl-2-phosphorene-2-oxide catalyst 0.0125
g (0.000065 mol, 0.05% / TDI) was added, and the internal temperature was raised to 110 ° C. with stirring. The generation of carbon dioxide increased as the temperature increased, and carbon dioxide generation was observed particularly violently when the internal temperature exceeded 80 ° C. Polymerization was carried out for 7 hours after the internal temperature reached 110 ° C. After completion of the polymerization, the solution was cooled to room temperature to obtain a transparent carbodiimide copolymer solution. A trace amount of residual isocyanate was detected in the solution, but it was 0.4% or less. When this carbodiimide copolymer was analyzed and the physical properties were measured, the solid content (%) 19 average molecular weight (Mw) 2300 molecular weight distribution (Mw / Mn) 2.4 5% decomposition temperature (° C) 435 solution stability toluene solution storage Both stability and storage stability of polymerization solution did not gel for 1 month. The result was obtained.

【0032】実施例7 攪拌機、温度計、冷却コンデンサーを備えた 100mlセパ
ラブルフラスコ中に、2,4−TDI80モル部と2,
6−TDI20モル部の混合物(商品名;TDI 8
0、三井東圧化学(株)製)25.4g(0.129モル) 、フェ
ニルイソシアネート2.49g(0.0209モル, TDI 100モ
ル部に対し、14モル部) 、乾燥パークレン40mlを窒素雰
囲気中に装入し、攪拌しながら均一に溶解した。次に、
重合溶媒と同じ溶媒1mlに希釈した3-メチル−1−フェ
ニル−2−ホスホレン−1−オキシド触媒 0.014g (0.
000073モル、0.05%/TDI)を添加し、攪拌しながら内温
を110 ℃まで昇温した。昇温とともに二酸化炭素の発生
が多くなり、内温が80℃をこえたあたりから特に激しく
二酸化炭素の発生が観察された。内温が 110℃に達して
から 7.5時間重合させた。重合終了後、室温まで冷却
し、透明なカルボジイミド共重合体溶液を得た。溶液中
に残存イソシアネートは微量検出されたが、0.4%以下
であった。このカルボジイミド共重合体の分析、物性値
測定を行なったところ、 固形分(%) 25 平均分子量(Mw) 3200 分子量分布(Mw/Mn) 2.9 5%分解温度(℃) 435 溶液安定性 トルエン溶液貯蔵安定性、重合溶
液貯蔵安定性共に、1ヶ月間ゲル化せず。 という結果が得られた。
Example 7 In a 100 ml separable flask equipped with a stirrer, thermometer and cooling condenser, 80 parts by mole of 2,4-TDI and 2,
A mixture of 20 parts by mol of 6-TDI (trade name; TDI 8
0, Mitsui Toatsu Chemical Co., Ltd. 25.4 g (0.129 mol), phenylisocyanate 2.49 g (0.0209 mol, TDI 100 mol parts, 14 mol parts), dry Perkren 40 ml were charged in a nitrogen atmosphere, It was uniformly dissolved with stirring. next,
0.014 g of 3-methyl-1-phenyl-2-phosphorene-1-oxide catalyst diluted with 1 ml of the same solvent as the polymerization solvent (0.
000073 mol, 0.05% / TDI) was added, and the internal temperature was raised to 110 ° C. with stirring. The generation of carbon dioxide increased as the temperature increased, and carbon dioxide generation was observed particularly violently when the internal temperature exceeded 80 ° C. After the internal temperature reached 110 ° C, polymerization was performed for 7.5 hours. After completion of the polymerization, the solution was cooled to room temperature to obtain a transparent carbodiimide copolymer solution. A trace amount of residual isocyanate was detected in the solution, but it was 0.4% or less. When this carbodiimide copolymer was analyzed and the physical properties were measured, solid content (%) 25 average molecular weight (Mw) 3200 molecular weight distribution (Mw / Mn) 2.9 5% decomposition temperature (° C) 435 solution stability toluene solution storage Both stability and storage stability of polymerization solution did not gel for 1 month. The result was obtained.

【0033】比較例4 フェニルイソシアネートを添加しない以外は、パークレ
ン中で実施例7と同様に重合させた結果、透明なカルボ
ジイミド共重合体溶液を得たが、3日以内に重合溶液は
ゲル化した。
Comparative Example 4 Polymerization was carried out in the same manner as in Example 7 except that phenylisocyanate was not added. As a result, a transparent carbodiimide copolymer solution was obtained, but the polymerization solution gelled within 3 days. ..

【0034】実施例8 攪拌機、温度計、冷却コンデンサーを備えた100ml セパ
ラブルフラスコ中に、2,4−TDI80モル部と2,
6−TDI20モル部の混合物(商品名;TDI 8
0、三井東圧化学(株)製) 19.11g(0.110モル) 、フ
ェニルイソシアネート6.55g (0.0550モル, TDI 100
モル部に対し、50モル部) 、乾燥パークレン51 ml を窒
素雰囲気中に装入し、攪拌しながら均一に溶解した。次
に、重合溶媒と同じ溶媒1mlに希釈した3−メチル−1
−フェニル−2−ホスホレン−1−オキシド触媒0.0747
g (0.000389モル、0.35%/TDI)を添加し、攪拌しなが
ら内温を 110℃まで昇温した。昇温とともに二酸化炭素
の発生が多くなり、内温が80℃をこえたあたりから特に
激しく二酸化炭素の発生が観察された。内温が110 ℃に
達してから 3.5時間重合させた。重合終了後、室温まで
冷却し、透明なカルボジイミド共重合体溶液を得た。溶
液中に残存イソシアネートは微量検出されたが、0.4 %
以下であった。このカルボジイミド共重合体の分析、物
性値測定を行なったところ、 固形分(%) 25 平均分子量(Mw) 1300 分子量分布(Mw/Mn) 2.0 5%分解温度(℃) 420 溶液安定性 トルエン溶液貯蔵安定性、重合溶
液貯蔵安定性共に、1ヶ月間ゲル化せず。 という結果が得られた。
Example 8 80 parts by mole of 2,4-TDI and 2, in a 100 ml separable flask equipped with a stirrer, a thermometer and a cooling condenser.
A mixture of 20 parts by mol of 6-TDI (trade name; TDI 8
0, manufactured by Mitsui Toatsu Chemicals, Inc. 19.11 g (0.110 mol), phenylisocyanate 6.55 g (0.0550 mol, TDI 100)
(50 mol parts relative to the mol parts) and 51 ml of dried Percene were charged in a nitrogen atmosphere and uniformly dissolved while stirring. Next, 3-methyl-1 diluted in 1 ml of the same solvent as the polymerization solvent.
-Phenyl-2-phosphorene-1-oxide catalyst 0.0747
g (0.000389 mol, 0.35% / TDI) was added, and the internal temperature was raised to 110 ° C. with stirring. The generation of carbon dioxide increased as the temperature increased, and carbon dioxide generation was observed particularly violently when the internal temperature exceeded 80 ° C. Polymerization was carried out for 3.5 hours after the internal temperature reached 110 ° C. After completion of the polymerization, the solution was cooled to room temperature to obtain a transparent carbodiimide copolymer solution. A trace amount of residual isocyanate was detected in the solution, but 0.4%
It was below. When the carbodiimide copolymer was analyzed and the physical properties were measured, solid content (%) 25 average molecular weight (Mw) 1300 molecular weight distribution (Mw / Mn) 2.0 5% decomposition temperature (° C) 420 solution stability toluene solution storage Both stability and storage stability of polymerization solution did not gel for 1 month. The result was obtained.

【0035】実施例10 攪拌機、温度計、冷却コンデンサーを備えた100ml セパ
ラブルフラスコ中に、2,4−TDI80モル部と2,
6−TDI20モル部の混合物(商品名;TDI 8
0、三井東圧化学(株)製)23.1g(0.133モル) 、フェ
ニルイソシアネート2.37g (0.0199モル, TDI 100モ
ル部に対し、15モル部) 、乾燥ジオキサン51 ml を窒素
雰囲気中に装入し、攪拌しながら均一に溶解した。次
に、重合溶媒と同じ溶媒1mlに希釈した3−メチル−1
−フェニル−2−ホスホレン−1−オキシド触媒 0.091
g(0.00047モル、0.36%/TDI)を添加し、攪拌しながら
内温を100℃まで昇温した。昇温とともに二酸化炭素の
発生が多くなり、内温が80℃をこえたあたりから特に激
しく二酸化炭素の発生が観察された。内温が100 ℃に達
してから5時間重合させた。重合終了後、室温まで冷却
し、透明なカルボジイミド共重合体溶液を得た。溶液中
に残存イソシアネートは微量検出されたが、0.4%以下
であった。このカルボジイミド共重合体の分析、物性値
測定を行なったところ、 固形分(%) 27 平均分子量(Mw) 3300 分子量分布(Mw/Mn) 3.0 5%分解温度(℃) 430 溶液安定性 トルエン溶液貯蔵安定性、重合溶
液貯蔵安定性共に、1ヶ月間ゲル化せず。 という結果が得られた。
Example 10 In a 100 ml separable flask equipped with a stirrer, a thermometer and a cooling condenser, 80 parts by mole of 2,4-TDI and 2,
A mixture of 20 parts by mol of 6-TDI (trade name; TDI 8
0, Mitsui Toatsu Chemical Co., Ltd., 23.1 g (0.133 mol), phenylisocyanate 2.37 g (0.0199 mol, 15 mol parts to 100 mol parts of TDI), and dry dioxane 51 ml were charged in a nitrogen atmosphere. , Dissolved uniformly while stirring. Next, 3-methyl-1 diluted in 1 ml of the same solvent as the polymerization solvent.
-Phenyl-2-phosphorene-1-oxide catalyst 0.091
g (0.00047 mol, 0.36% / TDI) was added, and the internal temperature was raised to 100 ° C. with stirring. The generation of carbon dioxide increased as the temperature increased, and carbon dioxide generation was observed particularly violently when the internal temperature exceeded 80 ° C. Polymerization was carried out for 5 hours after the internal temperature reached 100 ° C. After completion of the polymerization, the solution was cooled to room temperature to obtain a transparent carbodiimide copolymer solution. A trace amount of residual isocyanate was detected in the solution, but it was 0.4% or less. When this carbodiimide copolymer was analyzed and the physical properties were measured, solid content (%) 27 Average molecular weight (Mw) 3300 Molecular weight distribution (Mw / Mn) 3.0 5% Decomposition temperature (° C) 430 Solution stability Storage in toluene solution Both stability and storage stability of polymerization solution did not gel for 1 month. The result was obtained.

【0036】実施例11 攪拌機、温度計、冷却コンデンサーを備えた100ml セパ
ラブルフラスコ中に、2,4−TDI80モル部と2,
6−TDI20モル部の混合物(商品名;TDI 8
0、三井東圧化学(株)製)22.1g(0.127モル)、フェ
ニルイソシアネート5.11g (0.0429モル, TDI 100モ
ル部に対し、34モル部) 、乾燥キシレン54ml を窒素雰
囲気中に装入し、攪拌しながら均一に溶解した。次に、
重合溶媒と同じ溶媒1mlに希釈した3-メチル−1−フェ
ニル−2−ホスホレン−1−オキシド触媒 0.087g(0.0
0045モル、0.36%/TDI)を添加し、攪拌しながら内温を
110℃まで昇温した。昇温とともに二酸化炭素の発生が
多くなり、内温が80℃をこえたあたりから特に激しく二
酸化炭素の発生が観察された。内温が 110℃に達してか
ら 3.5時間重合させた。重合終了後、室温まで冷却し、
透明なカルボジイミド共重合体溶液を得た。溶液中に残
存イソシアネートは検出されなかった。このカルボジイ
ミド共重合体の分析、物性値測定を行なったところ、 固形分(%) 29 平均分子量(Mw) 1900 分子量分布(Mw/Mn) 3.0 5%分解温度(℃) 435 溶液安定性 トルエン溶液貯蔵安定性、重合溶
液貯蔵安定性共に、1ヶ月間ゲル化せず。 という結果が得られた。
Example 11 In a 100 ml separable flask equipped with a stirrer, a thermometer and a cooling condenser, 80 parts by mole of 2,4-TDI and 2,
A mixture of 20 parts by mol of 6-TDI (trade name; TDI 8
0, Mitsui Toatsu Chemical Co., Ltd.) 22.1 g (0.127 mol), phenylisocyanate 5.11 g (0.0429 mol, 34 mol parts to 100 mol parts of TDI), 54 ml of dry xylene were charged in a nitrogen atmosphere, It was uniformly dissolved with stirring. next,
3-methyl-1-phenyl-2-phosphorene-1-oxide catalyst diluted with 1 ml of the same solvent as the polymerization solvent 0.087 g (0.0
(0045 mol, 0.36% / TDI) was added and the internal temperature was increased while stirring.
The temperature was raised to 110 ° C. The generation of carbon dioxide increased as the temperature increased, and carbon dioxide generation was observed particularly violently when the internal temperature exceeded 80 ° C. After the internal temperature reached 110 ° C, polymerization was performed for 3.5 hours. After the completion of polymerization, cool to room temperature,
A transparent carbodiimide copolymer solution was obtained. No residual isocyanate was detected in the solution. When the carbodiimide copolymer was analyzed and the physical properties were measured, solid content (%) 29 average molecular weight (Mw) 1900 molecular weight distribution (Mw / Mn) 3.0 5% decomposition temperature (° C) 435 solution stability toluene solution storage Both stability and storage stability of polymerization solution did not gel for 1 month. The result was obtained.

【0037】[0037]

【発明の効果】本発明方法により製造されたカルボジイ
ミド共重合体は、従来方法で得られるポリカルボジイミ
ドの溶液での貯蔵安定性、特に高濃度での貯蔵安定性が
悪いという欠点を克服し、ポリカルボジイミドのその優
れた耐熱性を失うことなく簡単な操作でしかも大量にカ
ルボジイミド共重合体を生産しうる工業的な実施を可能
にしたものであり、産業上の利用価値は極めて大きい。
INDUSTRIAL APPLICABILITY The carbodiimide copolymer produced by the method of the present invention overcomes the drawback that the storage stability of the polycarbodiimide obtained by the conventional method in a solution, particularly the storage stability at a high concentration, is poor. The carbodiimide enables industrial production in which a large amount of carbodiimide copolymer can be produced by a simple operation without losing the excellent heat resistance of carbodiimide, and has an extremely great industrial utility value.

───────────────────────────────────────────────────── フロントページの続き (72)発明者 山口 彰宏 神奈川県横浜市栄区笠間町1190番地 三井 東圧化学株式会社内 ─────────────────────────────────────────────────── ─── Continuation of front page (72) Inventor Akihiro Yamaguchi 1190 Kasama-cho, Sakae-ku, Yokohama-shi, Kanagawa Mitsui Toatsu Chemical Co., Ltd.

Claims (6)

【特許請求の範囲】[Claims] 【請求項1】 下記式(1)(化1)で表わされる構造
単位を有する基5〜95当量部および下記式(2)(化
1)で表わされる構造単位を有する基95〜5当量部を
含み、ポリマーの分子の末端が芳香族基で封止され、か
つ重量平均分子量が1万以下であることを特徴とするカ
ルボジイミド共重合体。 【化1】
1. A group of 5 to 95 equivalent parts having a structural unit represented by the following formula (1) (chemical formula 1) and a group of 95 to 5 equivalent parts having a structural unit represented by the following formula (2) (chemical formula 1). A carbodiimide copolymer characterized by containing a polymer having a terminal of a polymer molecule sealed with an aromatic group and having a weight average molecular weight of 10,000 or less. [Chemical 1]
【請求項2】 ポリマーの分子末端の芳香族基が、フェ
ニル基、オルソ−トリル基、メタ−トリル基、パラ−ト
リル基、ジメチルフェニル基、クロロフェニル基、トリ
フルオロメチルフェニル基、ナフチル基、イソプロピル
フェニル基およびジイソプロピルフェニル基からなる群
より選ばれた少なくとも1種である請求項1記載のカル
ボジイミド共重合体。
2. The aromatic group at the molecular end of the polymer is a phenyl group, ortho-tolyl group, meta-tolyl group, para-tolyl group, dimethylphenyl group, chlorophenyl group, trifluoromethylphenyl group, naphthyl group, isopropyl group. The carbodiimide copolymer according to claim 1, which is at least one selected from the group consisting of a phenyl group and a diisopropylphenyl group.
【請求項3】 5〜95当量部の2,4−トリレンジイ
ソシアネートおよび95〜5当量部の2,6−トリレン
ジイソシアネートを含むジイソシアネート成分の総量1
00当量部に対して、10〜50当量部の芳香族モノイ
ソシアネートとを、カルボジイミド化触媒の存在下、ジ
イソシアネート成分の総量の1〜5倍量の非プロトン性
有機溶媒中で80℃以上の温度で加熱重合させることを
特徴とする請求項1記載のカルボジイミド共重合体の製
造方法。
3. A total amount of a diisocyanate component comprising 5 to 95 equivalent parts of 2,4-tolylene diisocyanate and 95 to 5 equivalent parts of 2,6-tolylene diisocyanate.
With respect to 00 equivalents, 10 to 50 equivalents of aromatic monoisocyanate, in the presence of a carbodiimidization catalyst, in an aprotic organic solvent in an amount of 1 to 5 times the total amount of diisocyanate components, at a temperature of 80 ° C. or higher. The method for producing a carbodiimide copolymer according to claim 1, wherein the polymerization is performed by heating.
【請求項4】 非プロトン性有機溶媒が、トルエン、キ
シレン、パークレンおよびジオキサンからなる群より選
ばれた少なくとも1種である請求項3記載のカルボジイ
ミド共重合体の製造方法。
4. The method for producing a carbodiimide copolymer according to claim 3, wherein the aprotic organic solvent is at least one selected from the group consisting of toluene, xylene, perkylene and dioxane.
【請求項5】 芳香族モノイソシアネートが、フェニル
イソシアネート、オルソ−トリルイソシアネート、メタ
−トリルイソシアネート、パラ−トリルイソシアネー
ト、ジメチルフェニルイソシアネート、クロロフェニル
イソシアネート、トリフルオロメチルフェニルイソシア
ネート、ナフチルイソシアネート、イソプロピルフェニ
ルイソシアネートおよびジイソプロピルフェニルイソシ
アネートからなる群より選ばれた少なくとも1種である
請求項3記載のカルボジイミド共重合体の製造方法。
5. The aromatic monoisocyanate is phenyl isocyanate, ortho-tolyl isocyanate, meta-tolyl isocyanate, para-tolyl isocyanate, dimethylphenyl isocyanate, chlorophenyl isocyanate, trifluoromethylphenyl isocyanate, naphthyl isocyanate, isopropylphenyl isocyanate and diisopropyl. The method for producing a carbodiimide copolymer according to claim 3, which is at least one selected from the group consisting of phenyl isocyanate.
【請求項6】 下記式(1)(化2)で表わされる構造
単位を有する基5〜95当量部および下記式(2)(化
2)で表わされる構造単位を有する基95〜5当量部を
含み、ポリマーの分子の末端が芳香族基で封止され、か
つ重量平均分子量が1万以下である請求項1記載のカル
ボジイミド共重合体を含むことを特徴とするカルボジイ
ミド系ワニス。 【化2】
6. A group having a structural unit represented by the following formula (1) (Chemical formula 2) in an amount of 5 to 95 equivalent parts and a group having a structural unit represented by a following formula (2) (Chemical formula 2) in an amount of 5 to 5 equivalent units. A carbodiimide-based varnish containing the carbodiimide copolymer according to claim 1, wherein the polymer has a molecular terminal blocked with an aromatic group and a weight average molecular weight of 10,000 or less. [Chemical 2]
JP4121644A 1992-05-14 1992-05-14 Carbodiimide copolymer and method for producing the same Expired - Fee Related JP2849001B2 (en)

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Application Number Priority Date Filing Date Title
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JP2849001B2 JP2849001B2 (en) 1999-01-20

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Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO1998041551A1 (en) * 1997-03-19 1998-09-24 Nitto Denko Corporation Aromatic polycarbodiimides and films thereof
EP0881243A1 (en) * 1997-05-19 1998-12-02 Nisshinbo Industries, Inc. Curing agent for powder coatings, powder coating composition comprising said curing agent, and powder coating film
US7018718B2 (en) 2003-03-26 2006-03-28 Nitto Denko Corporation Adhesive film for underfill and semiconductor device using the same
US7034101B2 (en) 2003-03-07 2006-04-25 Nitto Denko Corporation Polycarbodiimide copolymer and production method thereof

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO1998041551A1 (en) * 1997-03-19 1998-09-24 Nitto Denko Corporation Aromatic polycarbodiimides and films thereof
EP0881243A1 (en) * 1997-05-19 1998-12-02 Nisshinbo Industries, Inc. Curing agent for powder coatings, powder coating composition comprising said curing agent, and powder coating film
US7034101B2 (en) 2003-03-07 2006-04-25 Nitto Denko Corporation Polycarbodiimide copolymer and production method thereof
US7018718B2 (en) 2003-03-26 2006-03-28 Nitto Denko Corporation Adhesive film for underfill and semiconductor device using the same

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