JP4473148B2 - Method for producing 3,4'-diaminodiphenyl ether - Google Patents
Method for producing 3,4'-diaminodiphenyl ether Download PDFInfo
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- JP4473148B2 JP4473148B2 JP2005019673A JP2005019673A JP4473148B2 JP 4473148 B2 JP4473148 B2 JP 4473148B2 JP 2005019673 A JP2005019673 A JP 2005019673A JP 2005019673 A JP2005019673 A JP 2005019673A JP 4473148 B2 JP4473148 B2 JP 4473148B2
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- diaminodiphenyl ether
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Description
本発明は、機能性ポリアミドやポリイミドの重合用モノマー原料或いは改質添加物等に用いられる3,4’−ジアミノジフェニルエーテルの製造方法に関する。 The present invention relates to a method for producing 3,4'-diaminodiphenyl ether used as a monomer raw material for polymerization of functional polyamide or polyimide, or a modification additive.
3,4’−ジアミノジフェニルエーテルの製造には、3−アミノフェノールと4−クロロニトロベンゼンを縮合させた後、還元する方法が実施されている。又、特殊用途で用いられる3,4’−ジアミノジフェニルエーテルは、高い純度が要求されていることも知られており、純粋な3,4’−ジアミノジフェニルエーテルを得るために様々な提案がなされている。例えば、異性体の割合を少なくするために、原料の4−クロロニトロベンゼンに含まれる2−クロロニトロベンゼンの含有率を0.1質量%以下にする方法が提案されている(特許文献1参照)。又、3,4’−ジアミノジフェニルエーテルの蒸留時における熱分解生成物が、3,4’−ジアミノジフェニルエーテルへ混入するのを防ぐために、蒸留精製前の3,4’−ジアミノジフェニルエーテルを沸点範囲240〜350℃の不活性な有機溶媒に加えて、3,4’−ジアミノジフェニルエーテルの蒸留精製を行う方法が提案されている(特許文献2参照)。 In the production of 3,4'-diaminodiphenyl ether, a method of condensing 3-aminophenol and 4-chloronitrobenzene and then reducing is carried out. In addition, it is known that high purity is required for 3,4'-diaminodiphenyl ether used for special purposes, and various proposals have been made to obtain pure 3,4'-diaminodiphenyl ether. . For example, in order to reduce the proportion of isomers, a method has been proposed in which the content of 2-chloronitrobenzene contained in the raw material 4-chloronitrobenzene is 0.1% by mass or less (see Patent Document 1). Further, in order to prevent the thermal decomposition product during distillation of 3,4'-diaminodiphenyl ether from being mixed into 3,4'-diaminodiphenyl ether, the boiling point range of 240-240 In addition to an inert organic solvent at 350 ° C., a method of performing distillation purification of 3,4′-diaminodiphenyl ether has been proposed (see Patent Document 2).
又、蒸留時における副反応物等の高沸点物の熱分解を抑えるために、塔頂温度60〜150℃、塔頂圧力1.3〜266.6ヘクトパスカルの条件で8時間以内に反応溶媒を留去し、塔頂圧力66.6ヘクトパスカル以下の条件で3,4’−ジアミノジフェニルエーテルを蒸留する方法が提案されている(特許文献3参照)。一方で、特殊な電子材料の分野で使われるポリアミドやポリイミドの重合用モノマー原料には、低塩素濃度の3,4’−ジアミノジフェニルエーテルが要求されている。上記の方法では、塩素成分が混入する可能性が高く、要求を満足する3,4’−ジアミノジフェニルエーテルを得ることは困難である。 In order to suppress thermal decomposition of high-boiling products such as by-products during distillation, the reaction solvent is added within 8 hours under conditions of a tower top temperature of 60 to 150 ° C. and a tower top pressure of 1.3 to 266.6 hectopascals. There has been proposed a method of distilling and distilling 3,4'-diaminodiphenyl ether under conditions of a column top pressure of 66.6 hectopascals or less (see Patent Document 3). On the other hand, 3,4'-diaminodiphenyl ether having a low chlorine concentration is required as a monomer raw material for polymerizing polyamide or polyimide used in the field of special electronic materials. In the above method, it is difficult to obtain 3,4'-diaminodiphenyl ether that satisfies the requirement because the chlorine component is likely to be mixed.
又、従来の3,4’−ジアミノジフェニルエーテルの製造方法では、反応溶媒としてジメチルホルムアミドやN−メチルピロリドン等の含窒素有機溶媒が広く用いられているが、縮合反応時には、それらの溶媒が反応した不純物(例えばアミジン誘導体等)を生じる。この不純物は、3,4’−ジアミノジフェニルエーテルの蒸留時に分解して塩素成分を発生させるため、3,4’−ジアミノジフェニルエーテルには塩素成分が微量含まれることとなる。
本発明の目的は、低塩素濃度の3,4’−ジアミノジフェニルエーテルの製造方法を提供するものである。 An object of the present invention is to provide a method for producing 3,4'-diaminodiphenyl ether having a low chlorine concentration.
本発明者らは、上記の目的を達成すべく鋭意検討を試みた結果、3−アミノフェノールと4−クロロニトロベンゼンを縮合させた後、更に還元して、3,4’−ジアミノジフェニルエーテルを製造するに際し、反応溶媒として含窒素有機溶媒を用いずに、ジメチルスルホキシドを用いることで、塩素濃度10ppm以下の3,4’−ジアミノジフェニルエーテルが収率良く得られることを見出し、本発明に到達した。 As a result of intensive studies to achieve the above object, the present inventors condensated 3-aminophenol and 4-chloronitrobenzene, and then reduced to produce 3,4'-diaminodiphenyl ether. At that time, it was found that by using dimethyl sulfoxide without using a nitrogen-containing organic solvent as a reaction solvent, 3,4'-diaminodiphenyl ether having a chlorine concentration of 10 ppm or less can be obtained in good yield, and the present invention has been achieved.
即ち、本発明は以下の構成からなる。
(1)3−アミノフェノールと4−クロロニトロベンゼンを縮合させた後、得られた縮合反応後の溶液を、そのまま更に還元して、3,4’−ジアミノジフェニルエーテルを得るに際し、反応溶媒がジメチルスルホキシドであることを特徴とする3,4’−ジアミノジフェニルエーテルの製造方法。
(2)前記ジメチルスルホキシドの使用量が4−クロロニトロベンゼン100質量部に対し100〜500質量部である(1)に記載の3,4’−ジアミノジフェニルエーテルの製造方法。
That is, the present invention has the following configuration.
(1) After condensing 3-aminophenol and 4-chloronitrobenzene, the resulting solution after the condensation reaction is further reduced as it is to obtain 3,4'-diaminodiphenyl ether, and the reaction solvent is dimethyl sulfoxide. A process for producing 3,4'-diaminodiphenyl ether, characterized in that
(2) The method for producing 3,4'-diaminodiphenyl ether according to (1), wherein the amount of the dimethyl sulfoxide used is 100 to 500 parts by mass with respect to 100 parts by mass of 4-chloronitrobenzene.
本発明により得られた3,4’−ジアミノジフェニルエーテルは、その塩素濃度が低いので、特殊な電子材料の分野に使用されるポリアミドやポリイミドの重合用モノマー原料に使用できる。 Since 3,4'-diaminodiphenyl ether obtained by the present invention has a low chlorine concentration, it can be used as a monomer raw material for polymerization of polyamide and polyimide used in the field of special electronic materials.
以下に、好ましい実施の形態を挙げて本発明を詳細に説明する。
本発明において、4−クロロニトロベンゼンと3−アミノフェノールの縮合反応とそれに引き続いて行う還元反応に用いる溶媒はジメチルスルホキシドである。ジメチルスルホキシドの使用量は4−クロロニトロベンゼン100質量部に対し、100〜500質量部である。100質量部未満では重質物の生成が多くなり収率の低下の原因となるので好ましくなく、500質量部を超えると経済的に不利なので好ましくない。
Hereinafter, the present invention will be described in detail with reference to preferred embodiments.
In the present invention, the solvent used in the condensation reaction of 4-chloronitrobenzene and 3-aminophenol and the subsequent reduction reaction is dimethyl sulfoxide. The amount of dimethyl sulfoxide used is 100 to 500 parts by mass with respect to 100 parts by mass of 4-chloronitrobenzene. If the amount is less than 100 parts by mass, the production of heavy substances increases and the yield is reduced.
本発明において、4−クロロニトロベンゼンと3−アミノフェノールとの縮合反応は、縮合剤であるアルカリ金属炭酸塩を用いてジメチルスルホキシド中で行う。アルカリ金属炭酸塩は炭酸カリウム及び炭酸ナトリウムの使用が好ましい。アルカリ金属炭酸塩の使用量は4−クロロニトロベンゼン1モルに対して1〜3倍量のモル数の使用が好ましい。炭酸アルカリ金属塩を過剰に使用することで塩素成分の低減が可能となる。上記縮合反応の反応温度は130〜160℃で行い、反応時間は4〜12時間である。 In the present invention, the condensation reaction of 4-chloronitrobenzene and 3-aminophenol is carried out in dimethyl sulfoxide using an alkali metal carbonate that is a condensing agent. The alkali metal carbonate is preferably potassium carbonate or sodium carbonate. The amount of alkali metal carbonate used is preferably 1 to 3 times the number of moles per mole of 4-chloronitrobenzene. The chlorine component can be reduced by using an excessive amount of alkali metal carbonate. The reaction temperature for the condensation reaction is 130 to 160 ° C., and the reaction time is 4 to 12 hours.
上記で得られた縮合反応後の溶液を、反応生成物を単離することなくそのまま還元反応に用いることができる。 The solution after the condensation reaction obtained above can be directly used for the reduction reaction without isolating the reaction product.
還元反応の方法は、前記縮合反応物に(a)触媒の存在下、水素ガスを吹き込んで還元する方法と(b)触媒の存在下、ヒドラジンを加えて反応させる直接還元方法とがあるが、ヒドラジンによる直接還元法が好ましい。 The reduction reaction method includes (a) a reduction method by blowing hydrogen gas into the condensation reaction product in the presence of a catalyst and (b) a direct reduction method in which hydrazine is added and reacted in the presence of a catalyst. A direct reduction method with hydrazine is preferred.
ヒドラジンによる直接還元反応に使用する触媒としては三価の鉄化合物を使用するのが好ましい。三価の鉄化合物は酸化鉄(III)粉体、塩化鉄(III)及び水酸化鉄(III)等を例示できる。具体的には、塩化鉄(III)と活性炭を用いるのが好ましい。上記還元触媒の存在下、上記縮合反応後の溶液にヒドラジンを添加して直接還元を行う。上記直接還元反応の反応温度は50〜110℃で行い、反応時間は1〜8時間である。又、ヒドラジンの添加量は4−クロロニトロベンゼン1モルに対し1〜4倍量のモル数の使用量が好ましい。 As a catalyst used for the direct reduction reaction with hydrazine, it is preferable to use a trivalent iron compound. Examples of the trivalent iron compound include iron (III) oxide powder, iron (III) chloride, and iron (III) hydroxide. Specifically, it is preferable to use iron (III) chloride and activated carbon. In the presence of the reduction catalyst, hydrazine is added to the solution after the condensation reaction to perform direct reduction. The reaction temperature of the direct reduction reaction is 50 to 110 ° C., and the reaction time is 1 to 8 hours. The amount of hydrazine added is preferably 1 to 4 times the number of moles used per mole of 4-chloronitrobenzene.
次に、直接還元反応で発生した水を留去し、還元触媒及び無機塩をろ別して除去し、粗3,4’−ジアミノジフェニルエーテルのジメチルスルホキシド溶液を得る。そして、この溶液を通常の条件で減圧濃縮し、引き続き3,4’−ジアミノジフェニルエーテルの蒸留精製を行う。このようにして得られた3,4’−ジアミノジフェニルエーテルは塩素濃度が低いので、特殊な電子材料の分野で使われるポリアミドやポリイミドの重合用モノマー原料として使用できる。 Next, water generated by the direct reduction reaction is distilled off, and the reduction catalyst and the inorganic salt are removed by filtration to obtain a dimethyl sulfoxide solution of crude 3,4'-diaminodiphenyl ether. Then, this solution is concentrated under reduced pressure under normal conditions, followed by distillation purification of 3,4'-diaminodiphenyl ether. Since the 3,4'-diaminodiphenyl ether thus obtained has a low chlorine concentration, it can be used as a monomer raw material for polymerization of polyamide and polyimide used in the field of special electronic materials.
以下に実施例及び比較例を挙げて本発明を詳細に説明するが、本発明はこれに限定されるものではない。尚、以下において純度の「%」は質量基準である。
<実施例1>
[I.3−アミノ−4’−ニトロジフェニルエーテルの合成]
4−クロロニトロベンゼン157gと、3−アミノフェノール109gと、炭酸カリウム76gと、ジメチルスルホキシド266gとを仕込み、150℃で8時間反応させた。
Hereinafter, the present invention will be described in detail with reference to examples and comparative examples, but the present invention is not limited thereto. In the following, “%” of purity is based on mass.
<Example 1>
[I. Synthesis of 3-amino-4′-nitrodiphenyl ether]
157 g of 4-chloronitrobenzene, 109 g of 3-aminophenol, 76 g of potassium carbonate, and 266 g of dimethyl sulfoxide were charged and reacted at 150 ° C. for 8 hours.
[II.3,4’−ジアミノジフェニルエーテルの合成]
得られた反応液に、活性炭32gと塩化鉄(III)8gを加え、80℃に加温した。次に、99gのヒドラジン一水和物を3時間かけて滴下し、さらに2時間熟成させた。次に、水を留去し、生成した塩(塩化カリウム)と活性炭をろ別し、3,4’−ジアミノジフェニルエーテル溶液を得た。
[II. Synthesis of 3,4′-diaminodiphenyl ether]
To the obtained reaction solution, 32 g of activated carbon and 8 g of iron (III) chloride were added and heated to 80 ° C. Next, 99 g of hydrazine monohydrate was added dropwise over 3 hours and aged for 2 hours. Next, water was distilled off, and the produced salt (potassium chloride) and activated carbon were separated by filtration to obtain a 3,4′-diaminodiphenyl ether solution.
[III.濃縮・蒸留]
3,4’−ジアミノジフェニルエーテル溶液を減圧度66.6ヘクトパスカル、100℃で減圧濃縮を行った。次に、2.6〜3.9ヘクトパスカルに圧力を下げ、蒸留温度205〜210℃で3,4’−ジアミノジフェニルエーテルの蒸留を行い、150gの3,4’−ジアミノジフェニルエーテルを得た。収率は、4−クロロニトロベンゼン基準で75%であった。
[III. Concentration / distillation]
The 3,4′-diaminodiphenyl ether solution was concentrated under reduced pressure at 100 ° C. under a reduced pressure of 66.6 hectopascals. Next, the pressure was reduced to 2.6 to 3.9 hectopascals, and 3,4′-diaminodiphenyl ether was distilled at a distillation temperature of 205 to 210 ° C. to obtain 150 g of 3,4′-diaminodiphenyl ether. The yield was 75% based on 4-chloronitrobenzene.
得られた3,4’−ジアミノジフェニルエーテルについて、ガスクロマトグラフ法により分析したところ、純度は99.2%であった。又、3,4’−ジアミノジフェニルエーテルについて、硝酸銀による電位差滴定を行ったところ、塩素イオン濃度は5ppmであった。 When the obtained 3,4'-diaminodiphenyl ether was analyzed by gas chromatography, the purity was 99.2%. Further, when 3,4'-diaminodiphenyl ether was subjected to potentiometric titration with silver nitrate, the chlorine ion concentration was 5 ppm.
<比較例1>
反応溶媒として、ジメチルスルホキシドの代わりにジメチルホルムアミドを用いた以外は、実施例1と同様な操作を行った。
<Comparative Example 1>
The same operation as in Example 1 was performed except that dimethylformamide was used in place of dimethyl sulfoxide as a reaction solvent.
得られた3,4’−ジアミノジフェニルエーテルについて、ガスクロマトグラフ法により分析したところ、純度は99.2%であった。又、3,4’−ジアミノジフェニルエーテルについて、硝酸銀による電位差滴定を行ったところ、塩素イオン濃度は110ppmであった。 When the obtained 3,4'-diaminodiphenyl ether was analyzed by gas chromatography, the purity was 99.2%. Further, when potentiometric titration with silver nitrate was performed on 3,4'-diaminodiphenyl ether, the chlorine ion concentration was 110 ppm.
本発明で得られる3,4’−ジアミノジフェニルエーテルは、塩素の混入が極めて少なく、特殊な電子材料の分野で使われるポリアミドやポリイミドの重合用モノマー原料として使用できる。
The 3,4′-diaminodiphenyl ether obtained in the present invention is extremely low in chlorine and can be used as a monomer raw material for polymerization of polyamide and polyimide used in the field of special electronic materials.
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