Method for preparing fertilizer by extracting triacontanol from vegetable pitch
A technology of plant asphalt and triacontanol, applied in organic fertilizers, liquid fertilizers, fertilizer mixtures, etc., can solve the problems of restricting the large-scale production and use of triacontanol, high production costs, etc., and achieve abundant reserves and low equipment requirements , cheap effect
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Embodiment 1
[0027] 1) Mix 500L of plant asphalt, 50L of sodium alkoxide solution, and 50L of methanol evenly, maintain the reaction temperature at 45-50°C, and stir for 3 hours;
[0028] 2) Step 1) The temperature of the reaction liquid is rapidly cooled to below 5°C, and the cooling time is no more than 2 hours, and the filter cake is obtained by filtering with a diaphragm filter press. The weight loss of the filter cake on drying does not exceed 6%, and the weight of the filter cake is about 158kg;
[0029] 3) The filter cake is dissolved by adding 8 times the volume of n-hexane, and about 1100 L of supernatant liquid is separated in the extraction tank;
[0030] 4) Step 3) add 366L of acetone to the clear liquid, cool down to 5°C gradually, the cooling rate is 10°C / h, stop stirring and maintain the temperature for 10h, and filter to obtain 31kg of crude product crystals;
[0031] 5) Step 4) Dissolve the crystals in hot ethanol, add 62kg of urea and stir until dissolved, gradually cool ...
Embodiment 2
[0035] 1) Mix 2000L of plant asphalt, 200L of sodium alkoxide solution, and 200L of methanol evenly, maintain the reaction temperature at 45-50°C, and stir for 3 hours;
[0036] 2) Step 1) The temperature of the reaction liquid is cooled to below 5°C extremely quickly, and the cooling time is no more than 2 hours, and the filter cake is obtained by filtering with a diaphragm filter press. The weight loss of the filter cake on drying does not exceed 6%, and the weight of the filter cake is about 705kg;
[0037] 3) The filter cake is dissolved by adding 8 times the volume of n-hexane, and about 5600L of the supernatant is separated in the extraction tank;
[0038] 4) In step 3), add 1800L acetone to the clear liquid, cool down to 5°C gradually, and the cooling rate is 10°C / h, stop stirring and maintain the temperature for 10h, and filter to obtain 140kg of crude crystals;
[0039] 5) Step 4) Dissolve the crystals in hot ethanol, add 280kg of urea and stir until dissolved, gradua...
Embodiment 3
[0043] 1) Mix 1000L of plant asphalt, 100L of sodium alkoxide solution, and 100L of methanol evenly, maintain the reaction temperature at 45-50°C, and stir for 3 hours;
[0044] 2) Step 1) The temperature of the reaction liquid is rapidly cooled to below 5°C, and the cooling time is no more than 2 hours, and the filter cake is obtained by filtering with a diaphragm filter press. The weight loss of the filter cake on drying does not exceed 6%, and the weight of the filter cake is about 350kg;
[0045] 3) Add 8 times the volume of n-hexane to the filter cake to dissolve, and separate the supernatant liquid in the extraction tank to about 2800L;
[0046] 4) Step 3) add 930L acetone to the supernatant liquid, cool down to 5°C gradually, the cooling rate is 10°C / h, stop stirring and maintain the temperature for 10h, and filter to obtain 70kg of crude product crystals;
[0047] 5) Step 4) Dissolve the crystals in hot ethanol, add 140kg of urea and stir until dissolved, gradually coo...
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