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Treatment method of triglycidyl isocyanurate production waste liquid

A technology of glycidyl ester and tri-isocyanurate, which is applied in the field of treatment of waste liquid produced by triglycidyl isocyanurate, can solve the problems that waste liquid cannot be directly discharged, and there is no research on methanol waste liquid treatment, so as to reduce treatment Cost, reduced power consumption, improved distillation efficiency

Active Publication Date: 2022-07-01
ANHUI UNIVERSITY OF TECHNOLOGY
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

Therefore, the above two waste liquids cannot be discharged directly
[0004] At present, the treatment of TGIC production wastewater is mainly coagulation sedimentation-chemical oxidation-activated adsorption method, but this method can only treat wastewater with low COD content (≤10000mg / L) and has no relevant treatment for methanol waste liquid Research

Method used

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  • Treatment method of triglycidyl isocyanurate production waste liquid
  • Treatment method of triglycidyl isocyanurate production waste liquid

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0070] like figure 1 As shown, under stirring conditions, in 1LTGIC production wastewater (COD value of 1.85 × 10 5 mg / L, inorganic salt content of 3.7 wt%) was added dropwise with a sulfuric acid solution with a mass concentration of 65% to pH 2, stirred for 2 h in a water bath at 50 °C for acid hydrolysis, followed by intermittent vacuum distillation (so The intermittent vacuum distillation is one-stage vacuum distillation, and the conditions are 43kPa, 75°C, 7h) to obtain 0.6L of condensed water (COD value is 5230mg / L) and 0.375L of light yellow oil containing industrial salt;

[0071] After heating the 0.6L condensed water to 40°C, slowly add 50mL of chlorine dioxide solution with a mass concentration of 1.0% dropwise, continue to keep stirring for 2h, and obtain water with a COD value of 790mg / L (the water can be recycled and reused). or direct discharge);

[0072] The light yellow oil containing the industrial salt was mixed with 1 L of methanol for crystallization, fi...

Embodiment 2

[0076] like figure 1 As shown, under stirring conditions, in 10LTGIC production wastewater (COD value of 1.85 × 10 5 mg / L, the inorganic salt content is 3.7 wt%), add dropwise a sulfuric acid solution with a mass concentration of 65% to pH 2, stir for 1 h in a water bath at 70 °C for acidolysis, and conduct intermittent vacuum distillation (so The intermittent vacuum distillation was one-stage vacuum distillation, and the conditions were 45kPa, 85°C, 7h) to obtain 6.4L of condensed water (COD value was 7861mg / L) and 3.35L of light yellow oil containing industrial salt;

[0077] After heating the 6.4L of condensed water to 40°C, slowly add 0.8L of chlorine dioxide solution with a mass concentration of 1.0% dropwise, and continue to keep stirring for 2.5h to obtain water with a COD value of 920mg / L (the water can be recycled. reuse or direct discharge);

[0078] The light yellow oily substance containing industrial salt was mixed with 10L of methanol for crystallization, filte...

Embodiment 3

[0082] like figure 2 As shown, under stirring conditions, in 1L methanol waste liquid (the content of epichlorohydrin is 4.58wt%), add hydrochloric acid with a mass concentration of 32% dropwise to pH 3, then add 0.05g of tetraethyl chloride ammonium chloride, stirred for 2 hours in a water bath at 40 °C for acid hydrolysis, and distilled at 65 °C for 3 hours to obtain anhydrous methanol (0.87 L, the content of epichlorohydrin was 20 ppm, the mass content of methanol was 99.6%) and an oily high Boiler solution in methanol (0.11 L);

[0083] The methanol solution of the oily high boiler is subjected to atmospheric distillation (the condition of the atmospheric distillation is 90° C., 2 h) to obtain 0.065L of anhydrous methanol and 0.04L of the oily high boiler;

[0084] The oily high waste was mixed with 0.55 L of sodium hydroxide solution with a mass concentration of 40%, and a cyclization reaction was carried out (the temperature was 75° C. and the time was 1.5 min) to obtain...

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Abstract

The invention relates to the technical field of waste liquid treatment, in particular to a treatment method of triglycidyl isocyanurate production waste liquid. The treatment method provided by the invention comprises the following steps: sequentially carrying out first acidolysis and intermittent reduced pressure distillation on the TGIC production wastewater, mixing the obtained faint yellow oily substance containing industrial salt with absolute methanol, and crystallizing to obtain a methanol solution of inorganic salt and a first oily high-boiling residue; sequentially carrying out second acidolysis and first distillation on the methanol waste liquid to obtain absolute methanol and a methanol solution of a second oily high-boiling residue; performing second distillation on the methanol solution of the first oily high-boiling-point substance and / or the methanol solution of the second oily high-boiling-point substance to obtain absolute methanol and oily high-boiling-point substances; and mixing the oily high-boiling residue with alkali liquor to carry out cyclization reaction to obtain the epoxy chloropropane. The treatment method is suitable for treating high-COD (Chemical Oxygen Demand) and high-salinity wastewater, and can also be used for treating methanol wastewater.

Description

technical field [0001] The invention relates to the technical field of waste liquid treatment, in particular to a treatment method for waste liquid in the production of triglycidyl isocyanurate. Background technique [0002] Triglycidyl isocyanurate (TGIC), white crystal, mainly used as curing agent for carboxyl polyester and carboxyl acrylic resin powder coatings, also used in the manufacture of electrical insulating material laminates, printed circuits, various tools, adhesives agents and plastic stabilizers. Has excellent heat resistance, weather resistance, light resistance, corrosion resistance and mechanical properties. [0003] The solvent in the traditional TGIC production process is water, and the TGIC production wastewater with high content of COD and industrial waste salt is also obtained when the crude TGIC product is prepared; and the crude TGIC product needs to be further recrystallized with hot methanol solution to obtain TGIC quality products, a large amoun...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C02F9/10C07D405/14C07C29/80C07C31/04C07D303/08C07D301/32C07D301/26C02F1/04C02F1/66C02F1/52C02F103/36C02F101/34C02F101/38
CPCC02F9/00C07D405/14C07C29/80C07D303/08C07D301/32C07D301/26C02F1/04C02F1/66C02F1/52C02F2001/5218C02F2209/08C02F2103/36C02F2101/34C02F2101/38C07C31/04
Inventor 亓蒙周新民江雨柔张千峰
Owner ANHUI UNIVERSITY OF TECHNOLOGY