Method of preparing cation fatty acid softening agent
A fatty acid and cationic technology, applied in textiles, papermaking, fiber treatment, etc., can solve the problems of large yellowing, inability to use, and reduce hand feeling, and achieve the effects of improving whiteness, wide application, and reducing yellowing
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Embodiment 1
[0022] After stearic acid is heated to 70-120°C and melted, diethylenetriamine is added to the molten stearic acid and mixed, wherein the molar ratio of stearic acid to diethylenetriamine is 2:1, and then added to account for the total amount of materials 0.01% KOH aqueous solution with a concentration of 30% is used as a catalyst, and under the protection of nitrogen with a flow rate of 1-5 L / min, the temperature is raised and reacted at a rate of 0.5-3° C. / min. Dehydration begins when the temperature rises to 120-130°C, and the reaction temperature is controlled at 125-130°C. After the anhydrous is distilled out, the water output is counted, and the acid value is less than or equal to 1.5, and the amide condensation reaction is completed. Then the amide condensation reaction product is cooled to 105-110°C, and the epichlorohydrin is weighed, wherein the molar ratio of epichlorohydrin to diethylenetriamine is 0.5:1, and the dropwise reaction is carried out with a constant pres...
Embodiment 2
[0024] After stearic acid is heated to 70-120°C and melted, diethylenetriamine is added to the molten stearic acid and mixed, wherein the molar ratio of stearic acid to diethylenetriamine is 2:1, and then added to account for the total amount of materials 0.01% KOH aqueous solution with a concentration of 30% is used as a catalyst, and under the protection of nitrogen with a flow rate of 1-5 L / min, the temperature is raised and reacted at a rate of 0.5-3° C. / min. Dehydration begins when the temperature rises to 120-130°C, and the reaction temperature is controlled at 125-130°C. After the anhydrous is distilled out, the water output is counted, and the acid value is less than or equal to 1.5, and the amide condensation reaction is completed. Then the amide condensation reaction product was cooled to 105-110°C, and dimethyl sulfate was weighed, wherein the molar ratio of dimethyl sulfate to diethylenetriamine was 0.5:1. 130°C, the dropwise addition is completed, and the temperat...
Embodiment 3
[0026] After stearic acid is heated to 70-120°C and melted, diethylenetriamine is added to the molten stearic acid and mixed, wherein the molar ratio of stearic acid to diethylenetriamine is 2:1, and then added to account for the total amount of materials 0.01% KOH aqueous solution with a concentration of 30% is used as a catalyst, and under the protection of nitrogen with a flow rate of 1-5 L / min, the temperature is raised and reacted at a rate of 0.5-3° C. / min. Dehydration begins when the temperature rises to 120-130°C, and the reaction temperature is controlled at 125-130°C. After the anhydrous is distilled out, the water output is counted, and the acid value is less than or equal to 1.5, and the amide condensation reaction is completed. Then the amide condensation reaction product was cooled to 105-110°C, and dimethyl sulfate was weighed, wherein the molar ratio of dimethyl sulfate to diethylenetriamine was 0.5:1. 130°C, the dropwise addition is completed, and the temperat...
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