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:
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.