CN103387754A - Method for producing pigment red 48:2 with excellent heat resistance and migration resistance - Google Patents

Method for producing pigment red 48:2 with excellent heat resistance and migration resistance Download PDF

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CN103387754A
CN103387754A CN2013103457781A CN201310345778A CN103387754A CN 103387754 A CN103387754 A CN 103387754A CN 2013103457781 A CN2013103457781 A CN 2013103457781A CN 201310345778 A CN201310345778 A CN 201310345778A CN 103387754 A CN103387754 A CN 103387754A
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pigment red
resistance
heat resistance
migration
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CN103387754B (en
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杨宗泽
徐亮
陈奇文
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Zhejiang Kelong pigment Technology Co., Ltd.
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Crown Chemical Co Ltd
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Abstract

The invention relates to a method for producing a pigment red 48:2 with excellent heat resistance and migration resistance and belongs to the technical field of fine chemical industries. The method comprises the following process steps of: under an acidic condition, carrying out stirring diazotization reaction on 6-chloro-4-aminotoluene-3-sodium sulfonate and sodium nitrite for 1 hour, then, adding calcium chloride aqueous solution, and continuously carrying out stirring reaction; after the reaction is ended, adding material liquid into a clear alkaline solution of 2-hydroxy-3-naphthoic acid, so as to carry out coupling reaction; and after the reaction is ended, adjusting the pH value of a reaction solution to 7.0, then, adding a mixed assistant aqueous solution into the reaction solution so as to carry out surface modification, then, heating the reaction solution to 95-100 DEG C, carrying out heat-preserved reaction, then, adding water for cooling to below 60 DEG C, filtering, washing with water and drying, thus obtaining the pigment red 48:2. The method has the advantages that the dispersity, heat resistance, solvent resistance and fluidity of the pigment can be improved remarkably, and the coloring effect of the pigment can be improved effectively.

Description

The production method of a kind of pigment red 4 8:2 of superior heat resistance resistance to migration energy
Technical field
The invention belongs to the fine chemical technology field, be specifically related to the production method of a kind of pigment red 4 8:2 of superior heat resistance resistance to migration energy.
Background technology
6-chloro-4-aminotoluene-3-sulfonic acid sodium salt (being called for short 2B acid sodium) is a kind of important pigment dyestuff intermediate.It is the blue light redness as synthetic C.I.P.R.48:2 (everbright fast red BBC) toner of diazo component, is widely used in hard or flexible PVC, LLDPE, LDPE, HDPE, PP plastic cement system, and also applicable in rubber and PU.
The industrialized preparing process that C.I.P.R.48:2 is traditional is: after 2B acid sodium, water high temperatureization is clear, with hydrochloric acid acid out salify, add sodium nitrite in aqueous solution diazotization, coupled reaction is carried out in its diazonium salt and coupling component 2,3 acid, again with the calcium chloride effect, be transformed into the calcium salt color lake, with rosined soap, process before filtration, finally by Overheating Treatment, filtration, washing, drying.The pigmenting power of its preparation is lower, and owing to having introduced rosin, descend to some extent on resistance toheat, heat-resisting 210 ℃ of * 5min in PP, in transport property on PU below 3 grades.
Summary of the invention
Problem for the prior art existence, the object of the invention is to design the technical scheme of the production method of the pigment red 4 8:2 that a kind of superior heat resistance resistance to migration energy is provided, the method can improve dispersiveness, thermotolerance, solvent resistance and the mobility of pigment significantly, and the coloring effect that effectively improves pigment.
The production method of the pigment red 4 8:2 of described a kind of superior heat resistance resistance to migration energy is characterized in that comprising following processing step:
1) under acidic conditions, temperature-10 ℃~5 ℃, after 6-chloro-4-aminotoluene-3-sulfonic acid sodium salt and Sodium Nitrite generation diazotization stirring reaction 1h, add calcium chloride water to proceed stirring reaction;
2) after reaction finishes, at 12~15 ℃ of temperature, the feed liquid that step 1) is obtained is added in the alkaline solution of the 2-hydroxyl of clarification-3-naphthoic acid carries out coupled reaction;
3) after reaction finishes, with step 2) the pH value of the reaction solution that obtains adjusts to 7.0, add the mixed aid aqueous solution to carry out surface modification in this reaction solution again, then this reaction solution is warming up to 95~100 ℃ and carries out insulation reaction, then add below water for cooling to 60 ℃, filter, washing, oven dry, obtain red pigment 48:2.
The production method of the pigment red 4 8:2 of described a kind of superior heat resistance resistance to migration energy, the weight ratio that feeds intake that it is characterized in that the 6-chloro-4-aminotoluene-3-sulfonic acid sodium salt described in described step 1) and calcium chloride is 100:120~250, and the mass concentration of described calcium chloride water is 30%.
The production method of the pigment red 4 8:2 of described a kind of superior heat resistance resistance to migration energy, it is characterized in that mixed aid in described step 3) by the good hyper-dispersant of thermotolerance and Soxylat A 25-7 is composite forms, the weight proportion of described hyper-dispersant and Soxylat A 25-7 is 100:20~200.
The production method of the pigment red 4 8:2 of described a kind of superior heat resistance resistance to migration energy, it is characterized in that in described step 3), hyper-dispersant is super dispersed system CH-M8, CH-3A or CH-2C, described Soxylat A 25-7 is Soxylat A 25-7 O-15, Soxylat A 25-7 O-9 or Soxylat A 25-7 MOA-3.
Described a kind of superior heat resistance resistance to migration can the production method of pigment red 4 8:2, it is characterized in that in described step 3), the weight ratio that feeds intake of 6-chloro-4-aminotoluene-3-sulfonic acid sodium salt and hyper-dispersant is 100:1~15.
 
Concrete reaction equation of the present invention is as follows:
Figure 980186DEST_PATH_IMAGE001
Figure 900869DEST_PATH_IMAGE002
Chemical reagent involved in the present invention is currently available products, all can buy on market.
The production method of the pigment red 4 8:2 of above-mentioned a kind of superior heat resistance resistance to migration energy, reasonable in design, compared with prior art, have following beneficial effect:
1) the present invention is added to calcium chloride water in diazo liquid, the color lake reaction is advanceed to coupled reaction to be carried out simultaneously, the pigment molecule that makes solubility when just starting to form immediately color lake change into insoluble calcium precipitation, transparency and tinting strength improve greatly, and the partially blue phase of form and aspect;
2) the invention provides the using method of the compound auxiliary of the hyper-dispersant of fine heat-resisting performance and Soxylat A 25-7, change the surface polarity of granules of pigments by the synergy of compound auxiliary, substantially exceeded the covered effect sum of independent auxiliary agent, thereby improve pigment thermotolerance, dispersiveness, solvent resistance and mobility, obviously improve simultaneously the resistance to migration application performance of this blue light Pigment red in the PU application, increase economic efficiency;
3) the present invention has removed the use rosined soap process for treating surface of Traditional Industrialization production method, make its resistance toheat in PP reach 230 ℃ of * 5min, more common P.R.48:2 resistance toheat is high 20 ℃, make pigment be more suitable for the application of PU system owing to having removed the rosined soap processing, resistance to migration in the PU system rises to 5 grades, promote application performance, improved economic benefit.
Embodiment
The present invention will be further described below in conjunction with specific embodiment, but embodiment does not limit the scope of the invention.
Embodiment 1:
1) 200Kg6-chloro-4-aminotoluene-3-sulfonic acid sodium salt is added reactor, add 1800Kg water, be warming up to 90~95 ℃, stirring reaction 10~20min; Add concentrated hydrochloric acid in 5min, more than stirring reaction 30min; Then slowly adding 30% sodium nitrite in aqueous solution 250Kg to carry out diazotization reaction at 0 ℃ stirred 1 hour; Again 30% calcium chloride water 800Kg is joined in above diazo liquid;
2) add 2000Kg water in the coupled reaction still, 285Kg liquid caustic soda and 160Kg2,3 acid, stir at 40~50 ℃ of temperature, obtain clear liquor;
3) diazo liquid is injected this coupled reaction still under 12~15 ℃ and carry out coupled reaction, diazo liquid adds rear stirring 3 hours; After this reacting liquid pH value is adjusted to 7.0, with 2Kg CH-M8,4Kg O-15 add in 400Kg water be warming up to more than 90 ℃ molten clear after, slowly be added drop-wise in above reaction solution, after stirring 10~20min, again this reaction solution is warmed up to 95~100 ℃, insulation 30min, then add below water for cooling to 60 ℃, press filtration, washing, oven dry, obtain pigment red 4 8:2 under 80~100 ℃.Output: 385Kg, productive rate: 101.58%, the pigment outward appearance is bright-coloured, easy grinding disperses, and the tinting strength in the PVC medium, up to 110%, can reach 230 ℃ of * 5min on the PP resistance toheat, the PU transport property detection display class 5 of anti-migration level.
Embodiment 2
1) 200Kg6-chloro-4-aminotoluene-3-sulfonic acid sodium salt is added reactor, add 1800Kg water, be warming up to 90~95 ℃, stirring reaction 10~20min; Add concentrated hydrochloric acid in 5min, more than stirring reaction 30min; Then slowly adding 30% sodium nitrite in aqueous solution 250Kg to carry out diazotization reaction at 5 ℃ stirred 1 hour; Again 30% calcium chloride water 1000Kg is joined in above diazo liquid;
2) add 2000Kg water in reactor, 285Kg liquid caustic soda and 180Kg2,3 acid, stir at 40~50 ℃ of temperature, obtain clear liquor;
3) diazo liquid is injected this coupled reaction still under 12~15 ℃ and carry out coupled reaction, diazo liquid adds rear stirring 3 hours; After this reacting liquid pH value is adjusted to 7.0, with 10Kg CH-3A, 10Kg O-9 add in 400Kg water be warming up to more than 90 ℃ molten clear after, slowly be added drop-wise in above reaction solution, after stirring 10-20min, again this reaction solution is warmed up to 95~100 ℃, insulation 30min, cooling, press filtration, washing, oven dry, obtain pigment red 4 8:2 under 80~100 ℃.Output: 403Kg, productive rate: 102.54%, the pigment outward appearance is bright-coloured, easy grinding disperses, and the tinting strength in the PVC medium, up to 105%, can reach 230 ℃ of * 5min on the PP resistance toheat, the PU transport property detection display class 5 of anti-migration level.
Embodiment 3
1) 200Kg6-chloro-4-aminotoluene-3-sulfonic acid sodium salt is added reactor, add 1800Kg water, be warming up to 90~95 ℃, stirring reaction 10~20min; Add concentrated hydrochloric acid in 5min, more than stirring reaction 30min; Then slowly adding 30% sodium nitrite in aqueous solution 250Kg to carry out diazotization reaction at 0 ℃ stirred 1 hour; Again 30% calcium chloride water 1200Kg is joined in above diazo liquid;
2) add 2000Kg water in reactor, 285Kg liquid caustic soda and 200Kg2,3 acid, stir at 40~50 ℃ of temperature, obtain clear liquor;
3) diazo liquid is injected this coupled reaction still under 12~15 ℃ and carry out coupled reaction, diazo liquid adds rear stirring 3 hours; After this reacting liquid pH value is adjusted to 7.0, with 12Kg CH-2C, 18Kg MOA-3 add in 400Kg water be warming up to more than 90 ℃ molten clear after, slowly be added drop-wise in above reaction solution, after stirring 10~20min, again this reaction solution is warmed up to 95~100 ℃, insulation 30min, cooling, press filtration, washing, oven dry, obtain pigment red 4 8:2 under 80~100 ℃.Output: 418Kg, productive rate: 103.72%, the pigment outward appearance is bright-coloured, easy grinding disperses, and the tinting strength in the PVC medium, up to 108%, can reach 230 ℃ of * 5min on the PP resistance toheat, the PU transport property detection display class 5 of anti-migration level.
Embodiment 4
1) 200Kg6-chloro-4-aminotoluene-3-sulfonic acid sodium salt is added reactor, add 1800Kg water, be warming up to 90~95 ℃, stirring reaction 10~20min; Add concentrated hydrochloric acid in 5min, more than stirring reaction 30min; Then slowly adding 30% sodium nitrite in aqueous solution 250Kg to carry out diazotization reaction at 0 ℃ stirred 1 hour; Again 30% calcium chloride water 1650Kg is joined in above diazo liquid;
2) add 2000Kg water in reactor, 285Kg liquid caustic soda and 200Kg2,3 acid, stir at 40~50 ℃ of temperature, obtain clear liquor;
3) diazo liquid is injected this coupled reaction still under 12~15 ℃ and carry out coupled reaction, diazo liquid adds rear stirring 3 hours; After this reacting liquid pH value is adjusted to 7.0, with 20Kg CH-M8,4Kg MOA-3 add in 400Kg water be warming up to more than 90 ℃ molten clear after, slowly be added drop-wise in above reaction solution, after stirring 10~20min, again this reaction solution is warmed up to 95~100 ℃, insulation 30min, cooling, press filtration, washing, oven dry, obtain pigment red 4 8:2 under 80~100 ℃.Output: 411Kg, productive rate: 103.53%, the pigment outward appearance is bright-coloured, easy grinding disperses, and the tinting strength in the PVC medium, up to 108%, can reach 230 ℃ of * 5min on the PP resistance toheat, the PU transport property detection display class 5 of anti-migration level.

Claims (5)

  1. A superior heat resistance resistance to migration can the production method of pigment red 4 8:2, it is characterized in that comprising following processing step:
    1) under acidic conditions, temperature-10 ℃~5 ℃, after 6-chloro-4-aminotoluene-3-sulfonic acid sodium salt and Sodium Nitrite generation diazotization stirring reaction 1h, add calcium chloride water to proceed stirring reaction;
    2) after reaction finishes, at 12~15 ℃ of temperature, the feed liquid that step 1) is obtained is added in the alkaline solution of the 2-hydroxyl of clarification-3-naphthoic acid carries out coupled reaction;
    3) after reaction finishes, with step 2) the pH value of the reaction solution that obtains adjusts to 7.0, add the mixed aid aqueous solution to carry out surface modification in this reaction solution again, then this reaction solution is warming up to 95~100 ℃ and carries out insulation reaction, then add below water for cooling to 60 ℃, filter, washing, oven dry, obtain red pigment 48:2.
  2. A kind of superior heat resistance resistance to migration as claimed in claim 1 can the production method of pigment red 4 8:2, it is characterized in that the calcium chloride solution described in described step 1) joins in diazo liquid, the weight ratio that feeds intake of 6-chloro-4-aminotoluene-3-sulfonic acid sodium salt and calcium chloride is 100:120~250, and the mass concentration of described calcium chloride water is 30%.
  3. A kind of superior heat resistance resistance to migration as claimed in claim 1 can the production method of pigment red 4 8:2, it is characterized in that mixed aid in described step 3) by the good hyper-dispersant of thermotolerance and Soxylat A 25-7 is composite forms, the weight proportion of described hyper-dispersant and Soxylat A 25-7 is 100:20~200.
  4. As claim 1,3 described a kind of superior heat resistance resistances to migration can the production method of pigment red 4 8:2, it is characterized in that in described step 3), hyper-dispersant is CH-M8, CH-3A or CH-2C, described Soxylat A 25-7 is Soxylat A 25-7 O-15, Soxylat A 25-7 O-9 or Soxylat A 25-7 MOA-3.
  5. A kind of superior heat resistance resistance to migration as claimed in claim 1 can the production method of pigment red 4 8:2, it is characterized in that in described step 3), the weight ratio that feeds intake of 6-chloro-4-aminotoluene-3-sulfonic acid sodium salt and hyper-dispersant is 100:1~15.
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Cited By (7)

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Publication number Priority date Publication date Assignee Title
CN104962101A (en) * 2015-06-26 2015-10-07 嘉兴科隆化工有限公司 Industrial production method for safe and environment-friendly red-light yellow pigment PY191:1 for food plastic packaging
CN106084882A (en) * 2016-06-23 2016-11-09 嘉兴科隆化工有限公司 A kind of plastic cement industrialized preparing process of low PAHs content safety and environmental protection C lake red CAN'T pigment 53:1
CN106084875A (en) * 2016-06-13 2016-11-09 嘉兴科隆化工有限公司 The industrialized production of the paratonere PR 48:2 of a kind of excellence resistance to migration heat resistance and detection method
CN106634040A (en) * 2016-08-30 2017-05-10 上虞市东海化工有限公司 Preparation method of red pigment
CN111675922A (en) * 2020-06-22 2020-09-18 浙江东海新材料科技有限公司 Environment-friendly organic pigment applied to agricultural seed coating and preparation process thereof
CN113429805A (en) * 2021-06-24 2021-09-24 鞍山市五色石新材料科技有限公司 Production method of high-performance mixed crystal pigment taking C.I. pigment red 168 as main body
CN113462189A (en) * 2021-06-25 2021-10-01 杭州映山花颜料化工有限公司 Preparation method of azo pigment

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CN102399453A (en) * 2010-09-14 2012-04-04 南通锦悦服装设计有限公司 Preparation method of fast scarlet 48:1 organic pigment
CN102838883A (en) * 2012-09-25 2012-12-26 山东宇虹新颜料股份有限公司 Preparation method for C.I. paratonere 49:1

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CN102399453A (en) * 2010-09-14 2012-04-04 南通锦悦服装设计有限公司 Preparation method of fast scarlet 48:1 organic pigment
CN102838883A (en) * 2012-09-25 2012-12-26 山东宇虹新颜料股份有限公司 Preparation method for C.I. paratonere 49:1

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Cited By (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104962101A (en) * 2015-06-26 2015-10-07 嘉兴科隆化工有限公司 Industrial production method for safe and environment-friendly red-light yellow pigment PY191:1 for food plastic packaging
CN106084875A (en) * 2016-06-13 2016-11-09 嘉兴科隆化工有限公司 The industrialized production of the paratonere PR 48:2 of a kind of excellence resistance to migration heat resistance and detection method
CN106084882A (en) * 2016-06-23 2016-11-09 嘉兴科隆化工有限公司 A kind of plastic cement industrialized preparing process of low PAHs content safety and environmental protection C lake red CAN'T pigment 53:1
CN106634040A (en) * 2016-08-30 2017-05-10 上虞市东海化工有限公司 Preparation method of red pigment
CN111675922A (en) * 2020-06-22 2020-09-18 浙江东海新材料科技有限公司 Environment-friendly organic pigment applied to agricultural seed coating and preparation process thereof
CN113429805A (en) * 2021-06-24 2021-09-24 鞍山市五色石新材料科技有限公司 Production method of high-performance mixed crystal pigment taking C.I. pigment red 168 as main body
CN113429805B (en) * 2021-06-24 2022-07-01 鞍山市五色石新材料科技有限公司 Production method of high-performance mixed crystal pigment taking C.I. pigment red 168 as main body
CN113462189A (en) * 2021-06-25 2021-10-01 杭州映山花颜料化工有限公司 Preparation method of azo pigment
CN113462189B (en) * 2021-06-25 2023-04-25 杭州映山花颜料化工有限公司 Preparation method of azo pigment

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