WO2006004056A1 - Process for producing thick aqueous solution of azo and/or azoxystilbene dye - Google Patents

Process for producing thick aqueous solution of azo and/or azoxystilbene dye Download PDF

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WO2006004056A1
WO2006004056A1 PCT/JP2005/012235 JP2005012235W WO2006004056A1 WO 2006004056 A1 WO2006004056 A1 WO 2006004056A1 JP 2005012235 W JP2005012235 W JP 2005012235W WO 2006004056 A1 WO2006004056 A1 WO 2006004056A1
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carbon atoms
trialkylamine
dye
water
amine conversion
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PCT/JP2005/012235
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French (fr)
Japanese (ja)
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Fumitaka Satou
Takao Aizawa
Hiroshi Sugiyama
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Nippon Kayaku Kabushiki Kaisha
Kabushiki Kaisha Nippon Kayaku Tokyo
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Publication of WO2006004056A1 publication Critical patent/WO2006004056A1/en

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    • CCHEMISTRY; METALLURGY
    • C09DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
    • C09BORGANIC DYES OR CLOSELY-RELATED COMPOUNDS FOR PRODUCING DYES, e.g. PIGMENTS; MORDANTS; LAKES
    • C09B56/00Azo dyes containing other chromophoric systems
    • C09B56/04Stilbene-azo dyes
    • CCHEMISTRY; METALLURGY
    • C09DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
    • C09BORGANIC DYES OR CLOSELY-RELATED COMPOUNDS FOR PRODUCING DYES, e.g. PIGMENTS; MORDANTS; LAKES
    • C09B56/00Azo dyes containing other chromophoric systems
    • C09B56/04Stilbene-azo dyes
    • C09B56/06Bis- or polystilbene azo dyes
    • CCHEMISTRY; METALLURGY
    • C09DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
    • C09BORGANIC DYES OR CLOSELY-RELATED COMPOUNDS FOR PRODUCING DYES, e.g. PIGMENTS; MORDANTS; LAKES
    • C09B69/00Dyes not provided for by a single group of this subclass
    • C09B69/02Dyestuff salts, e.g. salts of acid dyes with basic dyes
    • C09B69/04Dyestuff salts, e.g. salts of acid dyes with basic dyes of anionic dyes with nitrogen containing compounds
    • C09B69/045Dyestuff salts, e.g. salts of acid dyes with basic dyes of anionic dyes with nitrogen containing compounds of anionic azo dyes
    • DTEXTILES; PAPER
    • D21PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21HPULP COMPOSITIONS; PREPARATION THEREOF NOT COVERED BY SUBCLASSES D21C OR D21D; IMPREGNATING OR COATING OF PAPER; TREATMENT OF FINISHED PAPER NOT COVERED BY CLASS B31 OR SUBCLASS D21G; PAPER NOT OTHERWISE PROVIDED FOR
    • D21H21/00Non-fibrous material added to the pulp, characterised by its function, form or properties; Paper-impregnating or coating material, characterised by its function, form or properties
    • D21H21/14Non-fibrous material added to the pulp, characterised by its function, form or properties; Paper-impregnating or coating material, characterised by its function, form or properties characterised by function or properties in or on the paper
    • D21H21/28Colorants ; Pigments or opacifying agents

Definitions

  • the present invention relates to a method for producing a concentrated aqueous solution of a dye. More specifically, a concentrated aqueous solution excellent in storage stability of yellow azo and Z or azoxystilbene dyes obtained by self-condensation of 4-trotoluene 2-sulfonic acid in the presence of alkali metal hydroxide. Relates to the manufacturing method.
  • Azo and Z or azoxystilbene dyes obtained by condensing 4-trotoluene 2-sulfonic acid in the presence of an alkali metal hydroxide are particularly useful for coloring paper. It is supposed that it has a structural formula represented by the formula (1). (Yu Hosoda, “Theory 'Manufacturing, Dye Chemistry”, published by Gihodo in 1962)
  • an alkali metal salt of a stilbene dye is a two-phase system of nitrobenzene Z water, and firstly a lipophilic ammonia is used using di- or trialkylamine having 12 to 40 carbon atoms.
  • an alkali metal salt of a stilbene dye is a two-phase system of methyl isobutyl ketone Z water, and a lipophilic ammonia is first used using a trialkylamine having 12 to 40 carbon atoms.
  • the stilbene dye is converted to a salt and then formed into a water-soluble alkanol ammonium salt using a mono-, di- or trialkanolamine having 2 to 4 carbon atoms of an alkenol group.
  • a method of obtaining a concentrated water solution of is proposed.
  • Patent Document 1 Japanese Patent Publication No. 6-99644 (Page 14)
  • Patent Document 2 Special Table 2003-501510 (Page 8-15)
  • An object of the present invention is to develop a method for efficiently producing a concentrated aqueous solution of a stilbene dye that eliminates the above-mentioned drawbacks in a conventionally known method in obtaining a concentrated aqueous solution of a stilbene dye.
  • a poorly water-soluble alkali metal salt of a yellow azo and / or azoxystilbene dye obtained by self-condensation of 4-trotoluene 2-sulfonic acid in the presence of an alkali metal hydroxide is converted into a lipophilic ammonia.
  • a method for producing a concentrated aqueous solution excellent in storage stability of the dye by converting into a -um salt (primary amine conversion) and then converting into an alkanol-am salt (secondary amine conversion);
  • the primary amine conversion is carried out by using at least one trialkylamine having 12 to 40 carbon atoms and a system of jetylbenzene and water or at least one trialkylamine having 12 to 40 carbon atoms.
  • the secondary amine conversion is carried out using a system of amine and water, and the trialkylamine and jetylbenzene phase obtained by the primary amine conversion or the trialkylamine phase is used.
  • Mono one carbon atom is 2-4, preparation of concentrated aqueous solutions of said dye to feature that performed by ⁇ Ka ⁇ di one or Toriarukano one Ruamin,
  • a mono-, di- or trialkanolamine having 2 to 4 carbon atoms in the alkanol group is a di- or trialkanolamine having 2 to 4 carbon atoms in the alkanol group.
  • the production method of the present invention is excellent in separability between an aqueous phase containing a water-soluble alkanol ammonium salt of a stilbene dye and a jetylbenzene phase used for conversion to the ammonium salt.
  • Efficient production of concentrated aqueous solutions of stilbene dyes without the need for troublesome processes such as azeotropic distillation to remove jetylbenzene in water (concentrated aqueous solutions) containing water-soluble alkanol ammonium salts of dyes It becomes possible to do.
  • the stilbene dye to be used in the production method of the present invention can be obtained by the method described in the above-mentioned document (Toyo Hosoda, "Theory” Production Dye Chemistry, published by Gihodo, 1962), for example, as follows.
  • the amount of alkali metal hydroxide can vary within a wide range, but crude 4-trotoluene 2-sulfonic acid may have sulfuric acid attached to it, so neutralize the sulfuric acid.
  • this condensation reaction For example, at pH 11 to 13 and at a temperature of 50 to 80 ° C for 5 to 8 hours. The end point of the condensation reaction is confirmed by checking the residual amount of 4-trotoluene 2-sulfonic acid by liquid chromatography.
  • the condensation reaction When the condensation reaction is completed, it may be obtained by filtration to obtain an alkali metal salt of a stilbene dye.
  • the reaction solution is used as it is as a raw material for carrying out the production method of the present invention without separating the alkali metal salt of the stilbene dye. It is preferable to use as
  • Water is added to the separated alkali metal salt of the stilbene dye or the alkali metal salt of the stilbene dye, and an inorganic strong acid, preferably sulfuric acid, is further added and stirred sufficiently to obtain an aqueous suspension or aqueous solution.
  • an inorganic strong acid preferably sulfuric acid
  • the pH of the solution should be 3 to 5, preferably around 4, and the amount of water should be 1 to 5 times, preferably 2 to 4 times by weight with respect to the alkali metal salt of the stilbene dye. Adjust the addition amount of strong acid and water respectively.
  • trialkylamine having 12 to 40 carbon atoms and jetylbenzene are encapsulated in the aqueous suspension or aqueous solution.
  • the amount of addition force of jetylbenzene is usually 20 to 27 parts by weight, preferably 22 to 25 parts by weight, per 100 parts by weight of the aqueous suspension or aqueous solution.
  • the loading of trialkylamines having 12 to 40 carbon atoms is 100 to 110% of the number of moles required to completely convert the sulfonic acid group on the stilbene dye to an ammonium salt. Mol, preferably 100 to 105% mol.
  • the mixture By adjusting the pH to 3-5, preferably around 4, by stirring sulfuric acid, the mixture is stirred for 30 minutes to 2 hours at a temperature of 60-80 ° C to give the corresponding lipophilic ammonia. After complete conversion to salt, it was allowed to stand and contained an inorganic salt with a stilbene dye lipophilic ammonia salt and an excess of a trialkylamine having 12 to 40 carbon atoms and a trialkylamine. Separate into aqueous phase. After removing the lower layer aqueous phase, the inorganic salt is sufficiently removed by washing the jetylbenzene phase preferably once or twice with hot water of 60 to 70 ° C.
  • trialkylamine having 12 to 40 carbon atoms used herein include tri (carbon number 4 to 13) alkyl such as tributylamine, tri-n-octylamine and triisooctylamine.
  • An amine is mentioned, but trialkylamine having 12 to 25 carbon atoms is preferred, and tri-n-octylamine is particularly preferred.
  • n-octylamine In addition, it may contain a similar alkylamine such as dioctyl monon-de-lamine.
  • a stilbene dye in the same manner as in the case of using jetylbenzene by using a large excess of trialkylamine having 12 to 40 carbon atoms without using any jetylbenzene. It is possible to obtain a liquid comprising an amine phase and an aqueous phase containing a lipophilic ammonia salt.
  • the same trialkylamine having 12 to 40 carbon atoms can be used as described above, which is 105% of the number of moles required to convert all the alkali metal salt to the trialkylamine salt. Above, preferably 120-200% trialkylamine is used.
  • the amine solution containing the lipophilic ammonia salt of the stilbene dye is washed with warm water or water to remove inorganic salts contained in the amine solution.
  • a benzene solution containing a lipophilic ammonium salt of a stilbene dye obtained as described above or a trialkylamine solution having 12 to 40 carbon atoms, followed by 2 to 4 carbon atoms of an alkanol group Individual mono-, di- or trialkanolamines are added and stirred and mixed in a temperature range of 60-80 ° C for 1-3 hours.
  • the lipophilic ammonia salt of the stilbene dye is converted to a hydrophilic alkanol ammonium salt, and the jetyl benzene phase or the trialkylamine phase having 12 to 40 carbon atoms is separated and transferred.
  • a jetylbenzene phase or a trialkylamine phase having 12 to 40 carbon atoms and an aqueous phase By leaving it stationary, it is separated into a jetylbenzene phase or a trialkylamine phase having 12 to 40 carbon atoms and an aqueous phase, and then a jetylbenzene phase or a trialkylamine having 12 to 40 carbon atoms.
  • a concentrated aqueous solution containing the stilbene dye alminol ammonium salt is obtained.
  • specific examples of mono-, di- or trialkanolamines having 2 to 4 carbon atoms of the alkanol group which can be used include diisopropanolamine, trihetanolamine, triisopropanolamine, diethanolamine.
  • dialkanoamines such as diethanolamine and diisopropanolamine are preferred, and diethanolamine is particularly preferred. Better!/,.
  • the amount of the alkanolamine is 110% or more of the number of moles required for converting the alkyl ammonium salt of the stilbene dye into its alkyl ammonium salt, preferably 120 to Use 200% alkanolamine.
  • the aqueous phase of the alkanol ammonium salt of the stilbene dye forming the lower layer and the trialkylamine phase of the lipophilic ammonia salt of the stilbene dye forming the upper layer are separated.
  • the trialkylamine solution is added to the upper trialkylamine solution as necessary, and then the alkali metal salt of the stilbene dye is prepared and the following production can be carried out.
  • the aqueous phase and the organic phase Since the good phase separation is performed promptly, it is easy to remove the inorganic salt in the concentrated aqueous solution, and no steps other than phase separation, removal, and washing are required. Usually only one piece is required, and the manufacturing process is greatly simplified.
  • the concentrated aqueous solution of stilbene dye obtained by the production method of the present invention carried out by such a method usually contains 15 to 25% by weight of stilbene dye, and 20% by weight under preferable conditions.
  • the dialkylbenzene containing trialkylamine can be used again after adding the amount of trialkylamine lost to the aqueous phase, if necessary, without purification. .
  • it can be purified by adding a filtration step and an activated carbon treatment-filtration step.
  • an activated carbon treatment and filtration it is preferable to perform an activated carbon treatment and filtration.
  • the concentrated aqueous solution of the stilbene dye obtained by the production method of the present invention is suitable for coloring various substrates, and particularly suitable for dyeing (coloring) size or non-size pulp paper.
  • a method for dyeing a method of adding a stilbene dye according to the present invention to a size press solution in a size press step after paper making, in addition to a known pulp internal addition method, can be employed.
  • the paper is dyed (colored) using the concentrated aqueous solution obtained by the production method of the present invention, it exhibits high directness and build-up property, and at the same time, the color of the waste liquid is excellent.
  • the concentrated aqueous solution obtained by the production method of the present invention exhibits high dyeing suitability for pulp fibers and paper, as well as cellulose fibers and regenerated cellulose fibers.
  • the light benzene phase containing the tri-n-octylammonium salt of the resulting stilbene dye was poured into the upper layer, and the aqueous phase containing the lower inorganic salt was washed away. Next, 3000 parts of 70 ° C water was added to the jetylbenzene phase containing lipophilic ammonia salt, and the mixture was stirred and washed for 30 minutes, and then the lower aqueous phase was removed.
  • Example 2 Instead of using jetylbenzene, instead of using 1050 parts of tri-n-octylamine which is about 50% excess of the amount required to convert all the sulfonic acid groups of the stilbene dyes to ammonium salts. The same procedure as in Example 1 was repeated. 1640 parts of a concentrated aqueous solution of a stilbene dye excellent in storage stability was obtained. This concentrated aqueous solution contained about 343 parts of stilbene dye.
  • Trialkylamines containing similar structures equivalent to 200% of the number of moles required to convert all sulphonic acid groups of stilbene dyes to ammonia salts (tri-n-otatylamin 15% , Di-n-octyl-mono-n-de-force-lamine 35%, mono-n-octyl-di-n-de-de-lamine 35%, tri-n-de-l-ramine 15%) 1400 parts
  • the same procedure as in Example 2 was repeated to obtain 1640 parts of a concentrated aqueous solution of stilbene dye having excellent storage stability. This concentrated aqueous solution contained 343 parts of stilbene dye.

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  • Organic Chemistry (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)

Abstract

A process for efficiently producing a thick aqueous solution of a yellow azo- and/or azoxystilbene dye obtained by the self-condensation of a 4-nitrotoluene-2-sulfonic acid in the presence of an alkali metal hydroxide. The process, which is for producing a thick aqueous solution, comprises converting a sparingly water-soluble alkali metal salt of the azo and/or azoxystilbene dye into an oleophilic ammonium salt (primary amine conversion) and then converting it into an alkanolammonium salt (secondary amine conversion), wherein the primary amine conversion is conducted either in a system comprising a C12-40 trialkylamine, diethylbenzene, and water or in a system comprising a C12-40 trialkylamine and water and the secondary amine conversion is conducted by adding a C2-4 alkanolamine to a phase of the oleophilic ammonium salt. Thus, a thick aqueous solution of the dye is produced.

Description

ァゾ及び Z又はァゾキシスチルベン染料の濃厚水溶液の製造法 技術分野  Process for producing concentrated aqueous solutions of azo and Z or azoxystilbene dyes
[0001] 本発明は染料の濃厚水溶液の製造法に関する。更に詳しくは、アルカリ金属水酸 化物の存在下で 4 -トロトルエン 2—スルホン酸を自己縮合させることによって得 られる黄色のァゾ及び Z又はァゾキシスチルベン染料の保存安定性に優れた濃厚 水溶液の製造法に関する。  [0001] The present invention relates to a method for producing a concentrated aqueous solution of a dye. More specifically, a concentrated aqueous solution excellent in storage stability of yellow azo and Z or azoxystilbene dyes obtained by self-condensation of 4-trotoluene 2-sulfonic acid in the presence of alkali metal hydroxide. Relates to the manufacturing method.
背景技術  Background art
[0002] アルカリ金属水酸化物の存在下で 4 -トロトルエン 2—スルホン酸を縮合するこ とによって得られるァゾ及び Z又はァゾキシスチルベン染料は、特に紙の着色に有 用で、次の式(1)で表されるような構造式を有するとされている。(細田豊著「理論'製 造 染料化学」昭和 32年技報堂刊 第 191頁)  [0002] Azo and Z or azoxystilbene dyes obtained by condensing 4-trotoluene 2-sulfonic acid in the presence of an alkali metal hydroxide are particularly useful for coloring paper. It is supposed that it has a structural formula represented by the formula (1). (Yu Hosoda, “Theory 'Manufacturing, Dye Chemistry”, published by Gihodo in 1962)
[0003] [化 1] [0003] [Chemical 1]
Figure imgf000002_0001
Figure imgf000002_0001
[0004] 4 -トロトルエン 2—スルホン酸をアルカリ金属水酸化物の存在下に自己縮合 することによって得られるァゾ及び Z又はァゾキシスチルベン染料(以下これらの染 料を合わせて単にスチルベン染料ということがある)は黄色の染料で、前記したように 特にパルプ、紙用の染料として多用されている。該染料を用いてパルプ、紙等の染 色に供する場合は、その取り扱いの便宜力 水溶液として扱われる力 運搬の効率 を考慮して、巿場では其の濃厚水溶液として取り扱われている。しかしながら該スチ ルベン染料は水に比較的溶解しにくく、該スチルベン染料のアルカリ金属塩の水に 対する溶解度は約 lgZlOOml程度と推定されている。そのため濃厚水溶液を得る 為の種々の工夫が提案されている。例えば、スチルベン染料のアルカノールァミン塩 を形成せしめる方法が行われ、殊に水不溶性のアンモ-ゥム塩に変換し次 、で水可 溶性のアンモ-ゥム塩に変換するという 2段階アミン変換法が有効な方法として提案 されている。具体的には、例えば、特許文献 1では、スチルベン染料のアルカリ金属 塩をニトロベンゼン Z水の 2相系で、先ず 12〜40個の炭素原子を有するジー又はト リアルキルアミンを用いて親油性アンモ-ゥム塩に変換し、次!、でアル力ノール基の 炭素原子が 2〜4個であるモノ—、ジ—又はトリアルカノ—ルァミンを用いて水溶性ァ ルカノールアンモ-ゥム塩を形成せしめることによりスチルベン染料の濃厚水溶液を 得る方法が提案されている。又、特許文献 2においては、スチルベン染料のアルカリ 金属塩をメチルイソブチルケトン Z水の 2相系で、先ず 12〜40個の炭素原子を有す るトリアルキルアミンを用いて親油性アンモ-ゥム塩に変換し、次 、でアル力ノール基 の炭素原子が 2〜4個であるモノ—、ジ—又はトリアルカノ—ルァミンを用いて水溶性 アルカノールアンモ-ゥム塩を形成せしめることにより前記スチルベン染料の濃厚水 溶液を得る方法が提案されて 、る。 [0004] 4-azotoluene 2-sulfonic acid obtained by self-condensation in the presence of an alkali metal hydroxide, azo and Z or azoxystilbene dyes (hereinafter these dyes are simply combined to form a stilbene dye) Is a yellow dye, and as mentioned above, it is frequently used as a dye for pulp and paper. When the dye is used for dyeing pulp, paper, etc., it is handled as a concentrated aqueous solution in the factory, taking into account the convenience of handling and the power transport efficiency. However, the stilbene dye is relatively insoluble in water, and the solubility of the alkali metal salt of the stilbene dye in water is estimated to be about lgZlOOml. Therefore, a concentrated aqueous solution is obtained. Various ideas have been proposed for this purpose. For example, a method of forming an alkanolamine salt of a stilbene dye is carried out, in particular a two-step amine conversion that converts to a water-insoluble ammonia salt and then to a water-soluble ammonia salt. The law has been proposed as an effective method. Specifically, for example, in Patent Document 1, an alkali metal salt of a stilbene dye is a two-phase system of nitrobenzene Z water, and firstly a lipophilic ammonia is used using di- or trialkylamine having 12 to 40 carbon atoms. Convert to um salt and form a water-soluble alkanol ammonium salt using mono-, di- or trialkanolamine in which 2 to 4 carbon atoms are present in the alkyl group. Thus, a method for obtaining a concentrated aqueous solution of a stilbene dye has been proposed. In Patent Document 2, an alkali metal salt of a stilbene dye is a two-phase system of methyl isobutyl ketone Z water, and a lipophilic ammonia is first used using a trialkylamine having 12 to 40 carbon atoms. The stilbene dye is converted to a salt and then formed into a water-soluble alkanol ammonium salt using a mono-, di- or trialkanolamine having 2 to 4 carbon atoms of an alkenol group. A method of obtaining a concentrated water solution of is proposed.
[0005] 特許文献 1:特公平 6— 99644号公報 (第 1 4頁) [0005] Patent Document 1: Japanese Patent Publication No. 6-99644 (Page 14)
特許文献 2:特表 2003 - 501510公報 (第 8— 15頁)  Patent Document 2: Special Table 2003-501510 (Page 8-15)
発明の開示  Disclosure of the invention
発明が解決しょうとする課題  Problems to be solved by the invention
[0006] 4 -トロトルエン 2—スルホン酸を自己縮合することによって得られるァゾ及び Z又はァゾキシスチルベン染料 (スチルベン染料)の濃厚水溶液を得る方法として、 従来公知の前記方法には種々欠点がある。即ち、特許文献 1に記載の方法ではスチ ルベン染料のアルカリ金属塩が先ず水難溶性のアンモ-ゥム塩へ変換されたあと- トロベンゼンで抽出され、次いで水溶性アルカノールアンモ -ゥム塩への変換が行わ れ、染料が有機相力 水相へ抽出されるのである力 この方法においては、ニトロべ ンゼン相と染料の水溶性アルカノールアンモ-ゥム塩を含む水相との分離に長時間 を要するという欠点がある。又、特許文献 2に記載の方法でも、水溶性アル力ノール アンモ-ゥム塩と媒体として使用するメチルイソプチルケトンとの相分離が充分でなく 、そのためメチルイソブチルケトンの一部は水相のアンモ-ゥム塩中に残留するため に、たとえば共沸蒸留により除去する必要があるという難点がある。 [0006] As a method for obtaining concentrated aqueous solutions of azo and Z or azoxystilbene dyes (stilbene dyes) obtained by self-condensation of 4-trotoluene 2-sulfonic acid, there are various disadvantages in the above-mentioned conventional methods. There is. That is, in the method described in Patent Document 1, an alkali metal salt of a stilbene dye is first converted into a poorly water-soluble ammonium salt, then extracted with trobenzene, and then converted into a water-soluble alkanol ammonium salt. The power of the transformation and the extraction of the dye into the organic phase. In this method, the separation of the nitrobenzene phase from the aqueous phase containing the water-soluble alkanol ammonium salt of the dye takes a long time. There is a disadvantage that it takes. Further, even in the method described in Patent Document 2, phase separation between a water-soluble alcoholic ammonium salt and methylisobutyl ketone used as a medium is not sufficient, and therefore, a part of methylisobutylketone is an aqueous phase. To remain in the ammonium salt In addition, there is a difficulty in that it must be removed by azeotropic distillation, for example.
[0007] 本発明の課題はスチルベン染料の濃厚水溶液を得るに当たり、従来知られている 方法における前記したような欠点がなぐスチルベン染料の濃厚水溶液を効率よく製 造する方法を開発することにある。  [0007] An object of the present invention is to develop a method for efficiently producing a concentrated aqueous solution of a stilbene dye that eliminates the above-mentioned drawbacks in a conventionally known method in obtaining a concentrated aqueous solution of a stilbene dye.
課題を解決するための手段  Means for solving the problem
[0008] 本発明者等は前記課題を解決すべく鋭意研究の結果、スチルベン染料の貯蔵安 定性に優れた濃厚水溶液を製造するにあたり、難溶性のアルカリ金属塩を水難溶性 のアンモ-ゥム塩へ変換し、次いで水溶性アルカノールアンモ -ゥム塩に変換するに 当たりジェチルベンゼン Z水又は大量の水難溶性のアンモ-ゥム塩を形成するため の水難溶性ァミンに媒体としての役目をもたせることにより前記課題が解決されること を見出し本発明を完成させるに至った。 [0008] As a result of diligent research to solve the above problems, the present inventors have found that when producing a concentrated aqueous solution having excellent storage stability of a stilbene dye, a hardly soluble alkali metal salt is hardly soluble in water and an amorphous salt. To be converted into water-soluble alkanol ammonium salt, and then to serve as a medium for the poorly water-soluble amine to form Jetylbenzene Z water or a large amount of poorly water-soluble ammonia salt. Thus, the inventors have found that the above problems can be solved, and have completed the present invention.
[0009] 即ち、本発明は  [0009] That is, the present invention provides
(1)アルカリ金属水酸化物の存在下での 4 -トロトルエン 2—スルホン酸の自己 縮合によって得られる黄色のァゾ及び/又はァゾキシスチルベン染料の水難溶性ァ ルカリ金属塩を親油性アンモ-ゥム塩に変換 (一次ァミン変換)し、次いでアルカノ— ルアンモ -ゥム塩に変換 (二次ァミン変換)することによって該染料の貯蔵安定性に 優れた濃厚水溶液を製造する方法にぉ 、て、該一次アミン変換を少なくとも 1種の 1 2〜40個の炭素原子を有するトリアルキルアミン及びジェチルベンゼンと水の系又は 少なくとも 1種の 12〜40個の炭素原子を含有するトリアルキルァミンと水の系を用 ヽ て行 、、又該二次アミン変換を上記一次アミン変換により得られたトリアルキルアミン 及びジェチルベンゼンの相、又はトリアルキルァミンの相、にアル力ノール基の炭素 原子が 2〜4個であるモノ一、ジ一又はトリアルカノ一ルァミンを添カ卩して行うことを特 徴とする前記染料の濃厚水溶液の製造法、  (1) A poorly water-soluble alkali metal salt of a yellow azo and / or azoxystilbene dye obtained by self-condensation of 4-trotoluene 2-sulfonic acid in the presence of an alkali metal hydroxide is converted into a lipophilic ammonia. A method for producing a concentrated aqueous solution excellent in storage stability of the dye by converting into a -um salt (primary amine conversion) and then converting into an alkanol-am salt (secondary amine conversion); The primary amine conversion is carried out by using at least one trialkylamine having 12 to 40 carbon atoms and a system of jetylbenzene and water or at least one trialkylamine having 12 to 40 carbon atoms. The secondary amine conversion is carried out using a system of amine and water, and the trialkylamine and jetylbenzene phase obtained by the primary amine conversion or the trialkylamine phase is used. Mono one carbon atom is 2-4, preparation of concentrated aqueous solutions of said dye to feature that performed by 添Ka 卩 di one or Toriarukano one Ruamin,
(2)—次アミン変換におけるトリアルキルァミンが 12〜25個の炭素原子を有するトリ アルキルァミンである(1)記載の製造法、  (2) The production method according to (1), wherein the trialkylamine in the secondary amine conversion is a trialkylamine having 12 to 25 carbon atoms,
(3) 12〜25個の炭素原子を有するトリアルキルァミンがトリ— n—ォクチルァミンであ る(2)記載の製造法、  (3) The production method according to (2), wherein the trialkylamine having 12 to 25 carbon atoms is tri-n-octylamine.
(4)一次アミン変換を当モル以上大過剰のトリー n—ォクチルァミンと水の系で行う(1 )記載の製造法、 (4) Primary amine conversion is carried out in a system with a large excess of tri-n-octylamine and water in excess of this mole (1 ) Manufacturing method described in the
(5)アル力ノール基の炭素原子が 2〜4個であるモノ—、ジ—又はトリアルカノ—ルァ ミンがアル力ノール基の炭素原子が 2〜4個であるジ—又はトリアルカノールァミンで ある(1)乃至 (4)の 、ずれか一項に記載の製造法、  (5) A mono-, di- or trialkanolamine having 2 to 4 carbon atoms in the alkanol group is a di- or trialkanolamine having 2 to 4 carbon atoms in the alkanol group. The manufacturing method according to any one of (1) to (4),
(6)アル力ノール基の炭素原子が 2〜4個であるジァルカノールアミンがジエタノール ァミンである(5)に記載の製造法、  (6) The production method according to (5), wherein the dialkanolamine having 2 to 4 carbon atoms in the alkanol group is diethanolamine;
(7)—次アミン変換をトリ— n—ォクチルァミンと水の系で行い、又二次アミン変換を ジエタノールアミンを添加して行う(1)乃至(6)のいずれか一項に記載の製造法、 (7) The production method according to any one of (1) to (6), wherein the secondary amine conversion is performed in a tri-n-octylamine and water system, and the secondary amine conversion is performed by adding diethanolamine.
(8)一次アミン変換を前記染料の合成反応液をそのまま使用し、かつ酸性条件下で 行う (1)乃至 (7)の 、ずれか一項に記載の製造法、 (8) The production method according to any one of (1) to (7), wherein primary amine conversion is carried out using the dye synthesis reaction solution as it is and under acidic conditions.
に関する。  About.
発明の効果  The invention's effect
[0010] 本発明の製造法は、スチルベン染料の水溶性アルカノールアンモ-ゥム塩を含む 水相とアンモ-ゥム塩への変換時に使用するジェチルベンゼン相との分離性が優れ るのでスチルベン染料の水溶性アルカノールアンモ-ゥム塩を含む水(濃厚水溶液) 中のジェチルベンゼンを除く為の例えば共沸蒸留等の面倒な工程を必要とせず、ス チルベン染料の濃厚水溶液を効率よく製造することが可能となる。 発明を実施するための最良の形態  [0010] The production method of the present invention is excellent in separability between an aqueous phase containing a water-soluble alkanol ammonium salt of a stilbene dye and a jetylbenzene phase used for conversion to the ammonium salt. Efficient production of concentrated aqueous solutions of stilbene dyes without the need for troublesome processes such as azeotropic distillation to remove jetylbenzene in water (concentrated aqueous solutions) containing water-soluble alkanol ammonium salts of dyes It becomes possible to do. BEST MODE FOR CARRYING OUT THE INVENTION
[0011] 本発明を詳細に説明する。  [0011] The present invention will be described in detail.
[0012] まず、本発明の製造法で対象とするスチルベン染料は前記文献 (細田豊著「理論' 製造 染料化学」昭和 32年技報堂刊 第 191頁)に記載の方法により、例えば次の ようにして製造することが出来る。すなわち、 4 -トロトルエン一 2—スルホン酸をァ ルカリ金属水酸化物、例えば水酸ィ匕カリウム、好ましくは水酸ィ匕ナトリウムの水溶液へ 加える。アルカリ金属水酸ィ匕物の量は広い範囲内において変化させることができるが 、粗製の 4 -トロトルエン 2—スルホン酸には硫酸が付着していることがあるので 、それらの硫酸を中和しても十分な量であるように、 4 -トロトルエン 2—スルホン 酸を基準にして 2〜4倍モル過剰に使用するのが好ましい。また水の量は 4 -トロト ルェン 2—スルホン酸に対して重量比で通常約 5倍である。この縮合反応は例え ば pHl l〜13で、温度 50〜80°Cで、 5〜8時間かけて行われる。縮合反応の終点は 液体クロマトグラフィ で 4 -トロトルエン 2—スルホン酸の残存量をチェックする こと〖こより確認される。縮合反応が終了したなら、濾別してスチルベン染料のアルカリ 金属塩として取得してもよ 、が、スチルベン染料のアルカリ金属塩を分離することなく 反応液をそのまま本発明の製造法を実施するための原料として使用するのが好まし い。 [0012] First, the stilbene dye to be used in the production method of the present invention can be obtained by the method described in the above-mentioned document (Toyo Hosoda, "Theory" Production Dye Chemistry, published by Gihodo, 1962), for example, as follows. Can be manufactured. That is, 4-trotoluene-2-sulfonic acid is added to an aqueous solution of an alkali metal hydroxide such as potassium hydroxide, preferably sodium hydroxide. The amount of alkali metal hydroxide can vary within a wide range, but crude 4-trotoluene 2-sulfonic acid may have sulfuric acid attached to it, so neutralize the sulfuric acid. Even so, it is preferably used in a molar excess of 2 to 4 times based on 4-trotoluene 2-sulfonic acid so that the amount is sufficient. The amount of water is usually about 5 times the weight ratio of 4-trotoluene 2-sulfonic acid. For example, this condensation reaction For example, at pH 11 to 13 and at a temperature of 50 to 80 ° C for 5 to 8 hours. The end point of the condensation reaction is confirmed by checking the residual amount of 4-trotoluene 2-sulfonic acid by liquid chromatography. When the condensation reaction is completed, it may be obtained by filtration to obtain an alkali metal salt of a stilbene dye. However, the reaction solution is used as it is as a raw material for carrying out the production method of the present invention without separating the alkali metal salt of the stilbene dye. It is preferable to use as
[0013] (一次ァミン変換)  [0013] (First-order amine transformation)
分離されたスチルベン染料のアルカリ金属塩またはスチルベン染料のアルカリ金属 塩を含有する反応液に水を加え、更に無機強酸、好ましくは硫酸を加えて十分撹拌 して、水性懸濁液または水溶液を得る。この際、液の pHは 3〜5、好ましくは 4前後に 、また水の量はスチルベン染料のアルカリ金属塩に対して重量比で 1〜5倍、好まし くは 2〜4倍になるようにそれぞれ強酸及び水の添加量を調整する。  Water is added to the separated alkali metal salt of the stilbene dye or the alkali metal salt of the stilbene dye, and an inorganic strong acid, preferably sulfuric acid, is further added and stirred sufficiently to obtain an aqueous suspension or aqueous solution. At this time, the pH of the solution should be 3 to 5, preferably around 4, and the amount of water should be 1 to 5 times, preferably 2 to 4 times by weight with respect to the alkali metal salt of the stilbene dye. Adjust the addition amount of strong acid and water respectively.
[0014] 次いでこの水性懸濁液または水溶液に 12〜40個の炭素原子を有するトリアルキル ァミン及びジェチルベンゼンをカ卩える。ジェチルベンゼンの添力卩量は水性懸濁液ま たは水溶液 100重量部に対して通常 20〜27重量部、好ましくは 22〜25重量部で ある。又 12〜40個の炭素原子を有するトリアルキルァミンの添力卩量はスチルベン染 料上のスルホン酸基を完全にアンモ-ゥム塩に変換するのに必要なモル数の 100〜 110%モル、好ましくは 100〜105%モルである。硫酸をカ卩えることにより、 pH3〜5 、好ましくは 4前後に調整しながら、温度 60〜80°Cの条件で 30分〜 2時間撹拌を行 つてスチルベン染料を対応する親油性アンモ-ゥム塩へ完全に変えた後、静置しス チルベン染料の親油性アンモ-ゥム塩及び過剰の 12〜40個の炭素原子を有するト リアルキルアミンを含むジェチルベンゼン相と無機塩を含有した水相に分離せしめる 。下層の水相を除去した後ジェチルベンゼン相を、好ましくは 60〜70°Cの温水で、 1〜2回洗浄することにより無機塩を十分に除去する。此処において使用される 12〜 40個の炭素原子を有するトリアルキルァミンの具体例としては、トリブチルァミン、トリ —n—ォクチルァミン、トリイソォクチルァミン等のトリ(炭素数 4〜 13)アルキルアミン が挙げられるが、 12〜25個の炭素原子を有するトリアルキルァミンが好ましぐ特にト リー n—ォクチルァミンを使用するのが好ましい。なお、トリー n—ォクチルァミンの中 に、ジー n ォクチル モノー n デ力-ルァミン等の類似アルキルアミンを含有する ものであってもよい。尚、前記アミン変換においてはジェチルベンゼンを全く使用す ることなく 12〜40個の炭素原子を有するトリアルキルアミンを大過剰に使用すること によってもジェチルベンゼンを使用した場合と同様にスチルベン染料の親油性アン モ-ゥム塩を含有するァミン相と水相からなる液を得ることが出来る。この場合は 12 〜40個の炭素原子を有するトリアルキルアミンは上記と同じものが使用でき、それを 、アルカリ金属塩をすベてトリアルキルアミン塩に変換するのに必要なモル数の 105 %以上、好ましくは 120〜200%のトリアルキルアミンを使用する。以下前記同様にス チルベン染料の親油性アンモ-ゥム塩を含有するアミン液を温水、水で洗浄し、アミ ン液中に含まれる無機塩等を除去する。 Next, trialkylamine having 12 to 40 carbon atoms and jetylbenzene are encapsulated in the aqueous suspension or aqueous solution. The amount of addition force of jetylbenzene is usually 20 to 27 parts by weight, preferably 22 to 25 parts by weight, per 100 parts by weight of the aqueous suspension or aqueous solution. Also, the loading of trialkylamines having 12 to 40 carbon atoms is 100 to 110% of the number of moles required to completely convert the sulfonic acid group on the stilbene dye to an ammonium salt. Mol, preferably 100 to 105% mol. By adjusting the pH to 3-5, preferably around 4, by stirring sulfuric acid, the mixture is stirred for 30 minutes to 2 hours at a temperature of 60-80 ° C to give the corresponding lipophilic ammonia. After complete conversion to salt, it was allowed to stand and contained an inorganic salt with a stilbene dye lipophilic ammonia salt and an excess of a trialkylamine having 12 to 40 carbon atoms and a trialkylamine. Separate into aqueous phase. After removing the lower layer aqueous phase, the inorganic salt is sufficiently removed by washing the jetylbenzene phase preferably once or twice with hot water of 60 to 70 ° C. Specific examples of the trialkylamine having 12 to 40 carbon atoms used herein include tri (carbon number 4 to 13) alkyl such as tributylamine, tri-n-octylamine and triisooctylamine. An amine is mentioned, but trialkylamine having 12 to 25 carbon atoms is preferred, and tri-n-octylamine is particularly preferred. In the tree n-octylamine In addition, it may contain a similar alkylamine such as dioctyl monon-de-lamine. In the amine conversion, a stilbene dye can be used in the same manner as in the case of using jetylbenzene by using a large excess of trialkylamine having 12 to 40 carbon atoms without using any jetylbenzene. It is possible to obtain a liquid comprising an amine phase and an aqueous phase containing a lipophilic ammonia salt. In this case, the same trialkylamine having 12 to 40 carbon atoms can be used as described above, which is 105% of the number of moles required to convert all the alkali metal salt to the trialkylamine salt. Above, preferably 120-200% trialkylamine is used. In the same manner as described above, the amine solution containing the lipophilic ammonia salt of the stilbene dye is washed with warm water or water to remove inorganic salts contained in the amine solution.
[0015] (二次ァミン変換)  [0015] (secondary amine transformation)
上記のようにして得られたスチルベン染料の親油性アンモ-ゥム塩を含有するジェ チルベンゼン液又は 12〜40個の炭素原子を有するトリアルキルアミン液に次いでァ ルカノール基の炭素原子が 2〜4個であるモノー、ジ—またはトリアルカノールァミン を加えて、 60〜80°Cの温度範囲で 1〜3時間撹拌、混合する。スチルベン染料の親 油性アンモ-ゥム塩は親水性のアルカノールアンモ -ゥム塩に変換され、ジェチル ベンゼン相又は 12〜40個の炭素原子を有するトリアルキルアミン相カも分離、移動 する。静置しておくことによりジェチルベンゼン相又は 12〜40個の炭素原子を有す るトリアルキルアミン相と水相に分離させ、ジェチルベンゼン相又は 12〜40個の炭 素原子を有するトリアルキルアミン相を除去することにより、スチルベン染料のアル力 ノールアンモ-ゥム塩を含有する濃厚水溶液が得られる。ここにおいて、使用しうるァ ルカノール基の炭素原子が 2〜4個であるモノー、ジ—またはトリアルカノールァミン の具体例としては、ジイソプロパノ一ルァミン、トリェタノ一ルァミン、トリイソプロパノ一 ルァミン、ジエタノールァミン、 n—プロパノールァミン等があげられ力 本発明におい ては、ジエタノールァミン、ジイソプロパノールァミン等のジ一アルカノ一ルァミンを用 V、るのが好ましぐ特にジエタノールアミンを用いるのが好まし!/、。  Next, a benzene solution containing a lipophilic ammonium salt of a stilbene dye obtained as described above or a trialkylamine solution having 12 to 40 carbon atoms, followed by 2 to 4 carbon atoms of an alkanol group. Individual mono-, di- or trialkanolamines are added and stirred and mixed in a temperature range of 60-80 ° C for 1-3 hours. The lipophilic ammonia salt of the stilbene dye is converted to a hydrophilic alkanol ammonium salt, and the jetyl benzene phase or the trialkylamine phase having 12 to 40 carbon atoms is separated and transferred. By leaving it stationary, it is separated into a jetylbenzene phase or a trialkylamine phase having 12 to 40 carbon atoms and an aqueous phase, and then a jetylbenzene phase or a trialkylamine having 12 to 40 carbon atoms. By removing the alkylamine phase, a concentrated aqueous solution containing the stilbene dye alminol ammonium salt is obtained. Here, specific examples of mono-, di- or trialkanolamines having 2 to 4 carbon atoms of the alkanol group which can be used include diisopropanolamine, trihetanolamine, triisopropanolamine, diethanolamine. In the present invention, dialkanoamines such as diethanolamine and diisopropanolamine are preferred, and diethanolamine is particularly preferred. Better!/,.
[0016] アルカノールァミンの量はスチルベン染料のアルキルアンモ-ゥム塩をそのアル力 ノ—ルアンモ -ゥム塩に変換するのに必要なモル数の 110%以上、好ましくは 120〜 200%のアルカノ一ルァミンを使用する。 [0016] The amount of the alkanolamine is 110% or more of the number of moles required for converting the alkyl ammonium salt of the stilbene dye into its alkyl ammonium salt, preferably 120 to Use 200% alkanolamine.
[0017] 二次アミン変換後には、下層を形成するスチルベン染料のアルカノールアンモ-ゥ ム塩の水相と上層を形成するスチルベン染料の親油性アンモ-ゥム塩のトリアルキル ァミン相に分離する。下層の水相を分離したのち上層のトリアルキルアミン液に、必 要によりトリアルキルアミンを追カ卩した上で、スチルベン染料のアルカリ金属塩をカロえ て次の製造を行うことが出来る。  [0017] After the secondary amine conversion, the aqueous phase of the alkanol ammonium salt of the stilbene dye forming the lower layer and the trialkylamine phase of the lipophilic ammonia salt of the stilbene dye forming the upper layer are separated. After the lower aqueous phase is separated, the trialkylamine solution is added to the upper trialkylamine solution as necessary, and then the alkali metal salt of the stilbene dye is prepared and the following production can be carried out.
[0018] 水不溶性のジェチルベンゼンを、有機相に使用することにより、親油性のアンモ- ゥム塩の形成中及び親水性のアルカノールアンモ -ゥム塩の形成中に、水相と有機 相の間の良好な相分離がすみやかに行われるので、濃厚水溶液中の無機塩の除去 が容易であり、相分離、除去、洗浄以外の工程が必要でないので、これらに必要とさ れる反応容器も通常 1個で済み、製造工程が大幅に簡略化される。このような方法で 実施される本発明の製造法で得られたスチルベン染料の濃厚水溶液にはスチルベ ン染料が通常 15〜25重量%、好ましい条件下では 20重量%含有される。  [0018] By using water-insoluble jetylbenzene in the organic phase, during the formation of the lipophilic ammonium salt and during the formation of the hydrophilic alkanol ammonium salt, the aqueous phase and the organic phase Since the good phase separation is performed promptly, it is easy to remove the inorganic salt in the concentrated aqueous solution, and no steps other than phase separation, removal, and washing are required. Usually only one piece is required, and the manufacturing process is greatly simplified. The concentrated aqueous solution of stilbene dye obtained by the production method of the present invention carried out by such a method usually contains 15 to 25% by weight of stilbene dye, and 20% by weight under preferable conditions.
[0019] 本発明の製造法においては、トリアルキルアミンを含むジェチルベンゼンは精製し ないでも、必要により水相に失われたトリアルキルァミンの量を追加した後、再度使用 が可能である。本発明の製造法においては、必要により、濾過工程、活性炭処理— 濾過工程を加えることにより精製することも可能である。特に濃厚水溶液中に 12〜4 0個の炭素原子を有するトリアルキルァミン、ジェチルベンゼンが残留して 、る懸念 があるときには活性炭処理を施し濾過を行うことが好まし ヽ。  [0019] In the production method of the present invention, the dialkylbenzene containing trialkylamine can be used again after adding the amount of trialkylamine lost to the aqueous phase, if necessary, without purification. . In the production method of the present invention, if necessary, it can be purified by adding a filtration step and an activated carbon treatment-filtration step. In particular, when there is a concern that trialkylamine having 12 to 40 carbon atoms and jetylbenzene remain in a concentrated aqueous solution, it is preferable to perform an activated carbon treatment and filtration.
[0020] 本発明の製造法で得られるスチルベン染料の濃厚水溶液は種々の基材の着色用 に適し、特にサイズ又は無サイズのパルプ紙の染色 (着色)に適している。染色する 方法としては、それ自体公知のパルプ内添法の他、抄紙後のサイズプレス工程でサ ィズプレス液に本願発明におけるスチルベン染料を加えて着色する等の方法が採用 できる。本発明の製造法で得られる濃厚水溶液を用いて紙を染色 (着色)した場合、 高い直接性、ビルドアップ性を示すと同時に其の廃液の着色度がすぐれている。尚、 本発明の製造法で得られた濃厚水溶液はパルプ、紙の染色 (着色)のほか、セル口 ース繊維、再生セルロース繊維に対しても高い染色適性を示す。  [0020] The concentrated aqueous solution of the stilbene dye obtained by the production method of the present invention is suitable for coloring various substrates, and particularly suitable for dyeing (coloring) size or non-size pulp paper. As a method for dyeing, a method of adding a stilbene dye according to the present invention to a size press solution in a size press step after paper making, in addition to a known pulp internal addition method, can be employed. When the paper is dyed (colored) using the concentrated aqueous solution obtained by the production method of the present invention, it exhibits high directness and build-up property, and at the same time, the color of the waste liquid is excellent. The concentrated aqueous solution obtained by the production method of the present invention exhibits high dyeing suitability for pulp fibers and paper, as well as cellulose fibers and regenerated cellulose fibers.
実施例 [0021] 以下実施例により本発明を更に詳細に説明する。実施例において、部は重量部をExample [0021] The present invention will be described in more detail with reference to the following examples. In an embodiment, parts are parts by weight.
、%は重量%をそれぞれ意味する。 ,% Means% by weight.
[0022] 実施例 1 [0022] Example 1
ガラスフラスコを 800部の水でみたし、次に 48%水酸ィ匕ナトリウム水溶液 480部を 温度が 50°Cを越えないようにして加える。次に 50°Cに加熱し、次いで 406部の 4 ニトロトルエン— 2—スルホン酸を約 1時間 30分でカ卩える。その間自然昇温させ約 1 時間で 76°C付近まで上昇させた。その混合物を 77〜79°Cで約 4時間撹拌する。そ の反応混合物の ρΗは約 13である。反応液にはスチルベン染料のナトリウム塩が約 1 0%含有されている。  Look at the glass flask with 800 parts of water, and then add 480 parts of 48% aqueous sodium hydroxide so that the temperature does not exceed 50 ° C. It is then heated to 50 ° C. and then 406 parts of 4-nitrotoluene-2-sulfonic acid are added in about 1 hour 30 minutes. During that time, the temperature was raised naturally and increased to around 76 ° C in about 1 hour. The mixture is stirred at 77-79 ° C for about 4 hours. The ρΗ of the reaction mixture is about 13. The reaction solution contains about 10% of a sodium salt of a stilbene dye.
[0023] 次に上記で得られた反応液に、約 30分を要して 85部の濃硫酸を加える。硫酸の添 加が終わると反応液の pHは 7〜8となる。この反応液を 30°Cにおいて、さらに 30分 間撹拌した。次に別に準備してあるガラスフラスコに 700部のジェチルベンゼンと 70 0部のトリ一 n—ォクチルァミンをカ卩えることにより得られた混合物の中に、前記反応 液の全量を加え、約 70°Cで約 1時間撹拌した。その間混合物に濃硫酸を加えて、約 pH4に調整、維持した。撹拌を止めるとジェチルベンゼン相と水相に直ちに分離し た。生成したスチルベン染料のトリー n—ォクチルアンモ-ゥム塩を含む軽!ヽジェチ ルベンゼン相は上層に、そして下層の無機塩を含む水相は流し出した。次に親油性 アンモ-ゥム塩を含むジェチルベンゼン相に 70°Cの水 3000部を加え、 30分間撹拌 洗浄した後、下層の水相を除去した。  Next, 85 parts of concentrated sulfuric acid is added to the reaction solution obtained above in about 30 minutes. When the addition of sulfuric acid is completed, the pH of the reaction solution becomes 7-8. This reaction solution was further stirred at 30 ° C. for 30 minutes. Next, in a separately prepared glass flask, 700 parts of jetylbenzene and 700 parts of tri-n-octylamine were added, and the total amount of the reaction mixture was added to the mixture. Stir for about 1 hour at ° C. Meanwhile, concentrated sulfuric acid was added to the mixture to adjust and maintain the pH at about 4. When the stirring was stopped, it separated into a jetylbenzene phase and an aqueous phase immediately. The light benzene phase containing the tri-n-octylammonium salt of the resulting stilbene dye was poured into the upper layer, and the aqueous phase containing the lower inorganic salt was washed away. Next, 3000 parts of 70 ° C water was added to the jetylbenzene phase containing lipophilic ammonia salt, and the mixture was stirred and washed for 30 minutes, and then the lower aqueous phase was removed.
[0024] 次に親油性アンモ-ゥム塩を含むジェチルベンゼン相に 330部の 80%ジエタノー ルァミン水溶液を投入し、 70°Cで 2時間撹拌を行った。スチルベン染料のトリー n— ォクチルアンモ -ゥム塩はジエタノールアンモ-ゥム塩に変換され下層に分離、移動 する。スチルベン染料のジェタノ—ルアンモ-ゥム塩を含有する水相を分離し、水相 に 20部の活性炭を加えて撹拌後濾過する。これにより水相中に微量残留して 、るトリ n ォクチルァミン及びジェチルベンゼンが除去される。 80〜 90°Cの温度で水分 を蒸発させて、濃度を調整し、フィルタ—でろ過して、 1640部のスチルベン染料の濃 厚水溶液を得た。この濃厚水溶液にはスチルベン染料が約 343部含有されて 、た。  [0024] Next, 330 parts of an 80% aqueous ethanolamine solution was added to the jetylbenzene phase containing the lipophilic ammonia salt, and the mixture was stirred at 70 ° C for 2 hours. The stilbene dye tree n-octyl ammonium salt is converted to diethanol ammonium salt and separated and transferred to the lower layer. Separate the aqueous phase containing the stilbene dye jetanol ammonium salt, add 20 parts of activated carbon to the aqueous phase, stir and filter. As a result, tri-n-octylamine and jetylbenzene are removed in a small amount in the aqueous phase. Water was evaporated at a temperature of 80 to 90 ° C., the concentration was adjusted, and the mixture was filtered through a filter to obtain 1640 parts of a concentrated aqueous solution of stilbene dye. This concentrated aqueous solution contained about 343 parts of stilbene dye.
[0025] 実施例 2 ジェチルベンゼンを使用しな 、代わりに、スチルベン染料のすべてのスルホン酸基 をアンモ-ゥム塩に換えるのに必要な量の約 50%過剰であるトリ— n—ォクチルアミ ン 1050部を使用して実施例 1におけるのと同じ手順を繰り返した。貯蔵安定性に優 れたスチルベン染料の濃厚水溶液 1640部を得た。この濃厚水溶液にはスチルベン 染料が約 343部含有されて ヽた。 [0025] Example 2 Instead of using jetylbenzene, instead of using 1050 parts of tri-n-octylamine which is about 50% excess of the amount required to convert all the sulfonic acid groups of the stilbene dyes to ammonium salts. The same procedure as in Example 1 was repeated. 1640 parts of a concentrated aqueous solution of a stilbene dye excellent in storage stability was obtained. This concentrated aqueous solution contained about 343 parts of stilbene dye.
[0026] 実施例 3 [0026] Example 3
70。Cの水 2150咅にスチノレベン染料のナトリウム塩 645咅 (4—ニトロトノレエン— 2— スルホン酸 406部より製造された)を加えて 30分撹拌して均一な分散液を得た。次に 全スルホン酸基をァミン塩に変換するのに必要とされるモル数の 150%に相当する 1 050部のトリ— n—ォクチルァミン 1050部を加え以下実施例 2と同様な操作を行って 貯蔵安定性に優れたスチルベン染料の濃厚水溶液 1640部を得た。この濃厚水溶 液にはスチルベン染料が約 343部含有されていた。  70. To 2150 liters of C water was added 645 liters of sodium salt of stynoleben dye (prepared from 406 parts of 4-nitrotonolene-2-sulfonic acid) and stirred for 30 minutes to obtain a uniform dispersion. Next, 1050 parts of tri-n-octylamine corresponding to 150% of the number of moles required to convert all sulfonic acid groups to the amine salt was added, and the same operation as in Example 2 was performed. 1640 parts of a concentrated aqueous solution of a stilbene dye having excellent storage stability was obtained. This concentrated aqueous solution contained about 343 parts of stilbene dye.
[0027] 実施例 4 [0027] Example 4
スチルベン染料の総てのスルホン酸基をアンモ-ゥム塩に換えるのに必要とされる モル数の 200%に相当する類似構造物を含んだトリアルキルアミン類(トリ— n—オタ チルァミン 15%、ジ一 n—ォクチルーモノ一 n—デ力-ルァミン 35%、モノ一 n—オタ チル—ジ— n—デ力-ルァミン 35%、トリ— n—デ力-ルァミン 15%) 1400部を使用 して実施例 2におけるのと同じ手順を繰り返して、貯蔵安定性に優れたスチルベン染 料の濃厚水溶液 1640部を得た。この濃厚水溶液にはスチルベン染料が 343部含有 されていた。  Trialkylamines containing similar structures equivalent to 200% of the number of moles required to convert all sulphonic acid groups of stilbene dyes to ammonia salts (tri-n-otatylamin 15% , Di-n-octyl-mono-n-de-force-lamine 35%, mono-n-octyl-di-n-de-de-lamine 35%, tri-n-de-l-ramine 15%) 1400 parts The same procedure as in Example 2 was repeated to obtain 1640 parts of a concentrated aqueous solution of stilbene dye having excellent storage stability. This concentrated aqueous solution contained 343 parts of stilbene dye.
[0028] 応用例 [0028] Application examples
染料ポットの中にパルプ 2部(乾燥重量)を投入後、水 40部、実施例 1で得た濃厚 水溶液 2. 0部を 500部に希釈した溶液カゝらその 20部をそれぞれ投入し、得られた混 合物を室温で 15分撹拌し、混合物が均質になるようにした。次に 1%サイズ剤 (FRサ ィズ 1900 ミサヮセラミックケミカル (株)製) 2部をカ卩えて 10分間撹拌し、続いて 3% 硫酸アルミニウム 2部をカロえて 15分間攪拌した。この溶液を使用して、 JISP-8209 ( パルプ試験用手すき紙調製法)に記載の方法に準じて抄紙、乾燥を行いペーパー シートを得た。このようにして得られた紙は、良好な湿潤堅牢度を有する深い黄色に 染色されていた。 After adding 2 parts (dry weight) of pulp into the dye pot, 40 parts of water and 20 parts of the concentrated solution obtained by diluting 2.0 parts of the concentrated aqueous solution obtained in Example 1 to 500 parts were added. The resulting mixture was stirred at room temperature for 15 minutes to make the mixture homogeneous. Next, 2 parts of a 1% sizing agent (FR size 1900 manufactured by Misa Ceramic Chemical Co., Ltd.) was added and stirred for 10 minutes, and then 2 parts of 3% aluminum sulfate was added and stirred for 15 minutes. Using this solution, papermaking and drying were performed according to the method described in JISP-8209 (Paper Test Handsheet Preparation Method) to obtain a paper sheet. The paper thus obtained has a deep yellow color with good wet fastness It was stained.

Claims

請求の範囲 The scope of the claims
[1] アルカリ金属水酸化物の存在下での 4 -トロトルエン 2—スルホン酸の自己縮合 によって得られる黄色のァゾ及び/又はァゾキシスチルベン染料の水難溶性アル力 リ金属塩を親油性アンモ-ゥム塩に変換 (一次ァミン変換)し、次いでアルカノ—ルァ ンモニゥム塩に変換 (二次ァミン変換)することによって該染料の貯蔵安定性に優れ た濃厚水溶液を製造する方法にぉ 、て、該一次アミン変換を少なくとも 1種の 12〜4 0個の炭素原子を有するトリアルキルアミン及びジェチルベンゼンと水の系又は少な くとも 1種の 12〜40個の炭素原子を含有するトリアルキルァミンと水の系を用いて行 V、、又該二次アミン変換を上記一次アミン変換により得られたトリアルキルアミン及び ジェチルベンゼンの相、又はトリアルキルァミンの相、にアル力ノール基の炭素原子 力^〜 4個であるモノ一、ジ一又はトリアルカノ一ルァミンを添カ卩して行うことを特徴と する前記染料の濃厚水溶液の製造法。  [1] Yellow azo and / or azoxy stilbene dyes obtained by self-condensation of 4-trotoluene 2-sulfonic acid in the presence of alkali metal hydroxide. According to a method for producing a concentrated aqueous solution excellent in storage stability of the dye by converting to an ammonium salt (primary amine conversion) and then converting to an alkanol ammonium salt (secondary amine conversion). The primary amine transformation with at least one trialkylamine having 12 to 40 carbon atoms and a system of jetylbenzene and water or at least one trialkyl containing 12 to 40 carbon atoms. Using a system of amine and water, and the secondary amine conversion into the trialkylamine and jetylbenzene phase obtained by the primary amine conversion or the trialkylamine phase, Carbon atoms force ^ ~ mono one is four, the preparation of concentrated aqueous solutions of the dye, which comprises carrying out by 添Ka 卩 di one or Toriarukano one Ruamin.
[2] 一次アミン変換におけるトリアルキルァミンが 12〜25個の炭素原子を有するトリアル キルァミンである請求項 1記載の製造法。  [2] The process according to claim 1, wherein the trialkylamine in the primary amine conversion is a trialkylamine having 12 to 25 carbon atoms.
[3] 12〜25個の炭素原子を有するトリアルキルァミンがトリ— n—ォクチルァミンである請 求項 2記載の製造法。  [3] The process according to claim 2, wherein the trialkylamine having 12 to 25 carbon atoms is tri-n-octylamine.
[4] 一次アミン変換を当モル以上大過剰のトリ— n—ォクチルァミンと水の系で行う請求 項 1記載の製造法。  [4] The production method according to claim 1, wherein the primary amine conversion is carried out in a system of tri-n-octylamine and water in a large excess of an equimolar amount or more.
[5] アル力ノール基の炭素原子が 2〜4個であるモノ—、ジ—又はトリアルカノ—ルァミン がアル力ノール基の炭素原子が 2〜4個であるジ—又はトリアルカノ—ルァミンである 請求項 1乃至請求項 4のいずれか一項に記載の製造法。  [5] A mono-, di- or trialkanolamine having 2 to 4 carbon atoms of an aranol group is a di- or trialkanolamine having 2 to 4 carbon atoms of an alkanol group. The production method according to any one of claims 1 to 4.
[6] アル力ノール基の炭素原子が 2〜4個であるジァルカノールァミンがジエタノールアミ ンである請求項 5に記載の製造法。 6. The process according to claim 5, wherein the dialkanolamine having 2 to 4 carbon atoms in the aranol group is diethanolamine.
[7] 一次アミン変換をトリ— n—ォクチルァミンと水の系で行い、又二次アミン変換をジェ タノールアミンを添加して行う請求項 1乃至請求項 6のいずれか一項に記載の製造法 [7] The process according to any one of claims 1 to 6, wherein the primary amine conversion is performed in a tri-n-octylamine and water system, and the secondary amine conversion is performed by adding ethanolamine.
[8] 一次アミン変換を前記染料の合成反応液をそのまま使用し、かつ酸性条件下で行う 請求項 1乃至請求項 7のいずれか一項に記載の製造法。 [8] The production method according to any one of [1] to [7], wherein the primary amine conversion is performed under the acidic condition using the dye synthesis reaction solution as it is.
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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN110373040A (en) * 2019-07-30 2019-10-25 于克兢 A kind of azoxy and azo stibene dyestuff preparation method

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Publication number Priority date Publication date Assignee Title
JPS5796052A (en) * 1980-12-02 1982-06-15 Basf Ag Manufacture of less electrolyte sulfonic acid group-containing coloring matter
JPS61115959A (en) * 1984-11-12 1986-06-03 チバ‐ガイギ アクチエンゲゼルシヤフト Production of concentrated storage stable aqueous solution of yellow azo- and azoxy-stylbene dye

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5796052A (en) * 1980-12-02 1982-06-15 Basf Ag Manufacture of less electrolyte sulfonic acid group-containing coloring matter
JPS61115959A (en) * 1984-11-12 1986-06-03 チバ‐ガイギ アクチエンゲゼルシヤフト Production of concentrated storage stable aqueous solution of yellow azo- and azoxy-stylbene dye

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN110373040A (en) * 2019-07-30 2019-10-25 于克兢 A kind of azoxy and azo stibene dyestuff preparation method
CN110373040B (en) * 2019-07-30 2021-05-14 洛阳美伦色彩科技有限公司 Preparation method of azoxy and azostilbene dye

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