Method of preparing cation fatty acid softening agent
A fatty acid, cationic technology, applied in textiles, papermaking, fiber processing, etc., can solve problems such as unusability, yellowing, and reducing hand feel, and achieve the effects of wide application, improved whiteness, and reduced yellowing
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Embodiment 1
[0023] After stearic acid is heated to 70-120°C to melt, 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 the epichlorohydrin was weighed, wherein the molar ratio of epichlorohydrin to diethylenetriamine was 0.5:1, and the dropwise reaction was carried out with a constant pre...
Embodiment 2
[0025] After stearic acid is heated to 70-120°C to melt, 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 105-10°C, and dimethyl sulfate was weighed, wherein the molar ratio of dimethyl sulfate to diethylenetriamine was 0.5:1, and the constant pressure funnel was used for dropwise reaction ...
Embodiment 3
[0027] After stearic acid is heated to 70-120°C to melt, 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 cool down the amide condensation reaction product to 105-110°C, weigh dimethyl sulfate, wherein the molar ratio of dimethyl sulfate to diethylenetriamine is 0.5:1, and use a constant pressure funnel to carry out dropwise reaction at a temp...
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