Method for preparing zinc fatty acid rubber plastifier by using illegal cooking oil
A technology of rubber plasticizer and fatty acid zinc, which is applied in the field of oleochemical industry, can solve the problems of increasing the production cost of fatty acid zinc rubber plasticizer, lack of pre-treatment and post-granulation process steps, and high price of fatty acid, so as to solve social pollution problems , raw material cost reduction, and the effect of broad market prospects
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Embodiment 1
[0022] 1. Early oil treatment:
[0023] A. Freezing: freeze the waste oil raw material in a freezing container at a freezing temperature of -5°C for 3 hours;
[0024] B. Filtration: Filtrate the frozen waste oil raw material to obtain crystallized product A and non-crystallized product B;
[0025] 2. Hydrolysis:
[0026] The A and B products obtained in step 1 are hydrolyzed by physical hydrolysis, the hydrolysis pressure is 2.0Mpa, the hydrolysis temperature is 250°C, and the time is 10 hours; after hydrolysis, the A and B products are correspondingly converted into corresponding crude acids C and D.
[0027] 3. Distillation:
[0028] The crude acid C or D obtained in step 2 is placed in a distillation pot for negative pressure distillation at a temperature of 220 to 240° C., and the negative pressure and vacuum degree are negatively correlated with the temperature.
[0029] 4. Rough points:
[0030] The product of step 3 is roughly divided in a fractionation tower at a t...
Embodiment 2
[0036] 1. Early oil treatment:
[0037] A. Freezing: freeze the waste oil raw material in a freezing container at a freezing temperature of -15°C for 2 hours;
[0038] B. Filtration: Filtrate the frozen waste oil raw material to obtain crystallized product A and non-crystallized product B;
[0039] 2. Hydrolysis:
[0040] The A and B products obtained in step 1 are hydrolyzed by physical hydrolysis, the hydrolysis pressure is 2.5Mpa, the hydrolysis temperature is 220°C, and the time is 8 hours; after hydrolysis, the A and B products are correspondingly converted into corresponding crude acids C and D.
[0041] 3. Distillation:
[0042] The crude acid C or D obtained in step 2 is placed in a distillation pot for negative pressure distillation at a temperature of 220 to 240° C., and the negative pressure and vacuum degree are negatively correlated with the temperature.
[0043] 4. Rough points:
[0044] The product of step 3 is roughly divided in a fractionation tower at a t...
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