Preparation method of pulping waste liquid adhesive
A technology for pulping waste liquid and adhesive, which is applied in the direction of adhesive, adhesive type, aldehyde/ketone condensation polymer adhesive, etc., can solve the problems of waste liquid pollution, etc. Effects of low levels of phenols and free aldehydes
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Embodiment 1
[0027] 1) Phenolic modification of pulping waste liquor
[0028] Under the action of alkaline catalyst and phenol, phenolization modification is carried out at 90°C on the kraft pulping waste liquid; the pulping waste liquid is physically filtered and concentrated, and its solid content is 25.0-45.0%. The mass ratio of pulping waste liquid to phenol is 1.0:0.1, the amount of alkaline catalyst sodium hydroxide is 2.0% of the total mass of pulping waste liquid and phenol, and the phenolization modification time is 4.0h;
[0029] 2) Synthesis of pulping waste liquid adhesive
[0030] Add aldehyde and basic catalyst to the pulping waste liquid after phenolization modification, under stirring, react at 55°C for 3 hours, then add urea, raise the temperature to 95°C and continue the reaction for 0.5h, stop heating when the viscosity is 500-900mPa·s, Cool to room temperature, discharge and serve;
[0031] Wherein the mol ratio of phenol and formaldehyde solution is 1.0: 1.5, the con...
Embodiment 2
[0033] 1) Phenolic modification of pulping waste liquor
[0034] Under the action of alkaline catalyst and phenol, the caustic soda pulping waste liquid is phenolized and modified at 120°C; the pulping waste liquid is physically filtered and concentrated, and its solid content is 25.0-45.0%. The mass ratio of waste liquid to cresol is 1.0:0.5, the amount of alkaline catalyst potassium hydroxide is 3.5% of the total mass of pulping waste liquid and phenol, and the phenolization modification time is 0.5h;
[0035] 2) Synthesis of pulping waste liquid adhesive
[0036] Add aldehyde and basic catalyst to the pulping waste liquid after phenolization modification, under stirring, react at 70°C for 1 hour, then add urea, raise the temperature to 85°C and continue the reaction for 1 hour, stop heating when the viscosity is 500-900mPa·s, cool to room temperature, put the ingredients and serve;
[0037] Wherein the mol ratio of phenol and solid formaldehyde is 1.0: 1.8, the consumptio...
Embodiment 3
[0039] 1) Phenolic modification of pulping waste liquor
[0040] Under the action of alkaline catalyst and phenol, the chemical mechanical pulping waste liquid is phenolized and modified at 100 °C; the pulping waste liquid is physically filtered and concentrated, and its solid content is 25.0-45.0%. The mass ratio of pulping waste liquid to xylenol is 1.0:0.8, the amount of alkaline catalyst sodium hydroxide and sodium carbonate is 4.2% of the total mass of pulping waste liquid and phenol, and the phenolization modification time is 1h;
[0041] 2) Synthesis of pulping waste liquid adhesive
[0042] Add aldehyde and basic catalyst to the pulping waste liquid after phenolization modification, under stirring, react at 65°C for 1.5h, then add urea, raise the temperature to 90°C and continue the reaction for 2h, stop heating when the viscosity is 500-900mPa·s, Cool to room temperature, discharge and serve;
[0043] Wherein the mol ratio of phenol and furfural is 1.0: 1.6, and the...
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