Method for producing pentaerythrite oleate by utilizing swill-cooked dirty oil
A technology of pentaerythritol oleate and gutter oil, which is applied in the field of oleochemical industry, can solve the problems of increasing the production cost of pentaerythritol oleate, lack of pretreatment and fine separation process steps, and can not meet the requirements of pentaerythritol oleate, so as to save imported raw materials Effects of foreign exchange, solving social pollution problems, and reducing raw material costs
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Embodiment 1
[0025] 1. Early preprocessing:
[0026] A. Freezing: freeze the waste oil raw material in a freezing container at a freezing temperature of -5°C for 3 hours;
[0027] B. Filtration: filter the frozen waste oil raw material to obtain crystalline A and non-crystalline B products;
[0028] 2. Hydrolysis:
[0029] The A and B products obtained in step 1 are hydrolyzed by physical hydrolysis respectively, the hydrolysis pressure is 2.0Mpa, and the hydrolysis temperature is 220°C; the time is 10 hours; after hydrolysis, the A and B products become crude acids C and D accordingly;
[0030] 3. Distillation:
[0031] Put the crude acids C and D obtained in step 2 into negative pressure distillation in the distillation pot respectively, at a temperature of 220°C and a pressure of -0.098MPa, and then condense and collect them in a temporary storage tank for later use;
[0032] 4. Rough points:
[0033] The product of step 3 is roughly divided in a fractionation tower at a temperature...
Embodiment 2
[0041] 1. Early preprocessing:
[0042] A. Freezing: freeze the waste oil raw material in a freezing container at a freezing temperature of -15°C for 2 hours;
[0043] B. Filtration: filter the frozen waste oil raw material to obtain crystalline A and non-crystalline B products;
[0044] 2. Hydrolysis:
[0045] The A and B products obtained in step 1 are hydrolyzed by physical hydrolysis respectively, the hydrolysis pressure is 2.5MPa, and the hydrolysis temperature is 250°C; the time is 8 hours; after hydrolysis, the A and B products become crude acids C and D accordingly;
[0046] 3. Distillation:
[0047] Put the crude acids C and D obtained in step 2 into negative pressure distillation in the distillation pot respectively, at a temperature of 240°C and a pressure of -0.096MPa, and then condense and collect them in a temporary storage tank for later use;
[0048] 4. Rough points:
[0049] The product of step 3 is roughly divided in a fractionation tower at a temperature...
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