Vitamin D3 production process
A production process, vitamin technology, applied in the direction of sustainable manufacturing/processing, chemical industry, climate sustainability, etc., can solve the problems of low product purity, serious environmental pollution, inability to react, etc., to improve process conditions and simplify processes Steps, the effect of reducing occupational health hazards
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Embodiment 1
[0027] 10 kg of 7-dehydrocholesterol and 300 L of methanol were added to the batching tank, the temperature was raised to 32° C. with stirring, and a photoreaction solution with a concentration of 3wt% was prepared. The photochemical reaction is carried out by an ultraviolet irradiator with a light source power of 20kw, the temperature of the photoreaction solution is controlled to be 65°C, and the flow rate of the photoreaction solution is controlled at 120L / h, and then the irradiated reaction solution is concentrated under reduced pressure in a concentration pot, and the concentrated The filtrate was transferred to a refrigerated stirring tank at -16°C for freezing and crystallization for 10h, and the unreacted raw materials were recovered by filtration. The filtrate was reacted at 60°C and -0.08Mpa for 2 hours to obtain 1.5 kg of converted oil. The converted oil was detected by liquid phase. of which vitamin D 3 The content is 80wt%; 1.5 kilograms of transformed oil and 3 t...
Embodiment 2
[0029] 15 kg of 7-dehydrocholesterol, 350 L of methanol and 280 L of cyclohexane were added to the batching tank, the stirring was turned on and the temperature was raised to 30° C. to prepare a light reaction solution with a concentration of 2 wt %, and the light reaction solution was incubated for 2 hours. The photochemical reaction is carried out by an ultraviolet irradiator with a light source power of 30kw that is passing through nitrogen, the temperature of the photoreaction solution is controlled to 60°C, and the flow rate of the photoreaction solution is controlled to 110L / h, and then the irradiated reaction solution is reduced in the concentration pot. Pressure and concentration, transfer the concentrate into a refrigerated stirring tank and freeze and crystallize at -15°C for 8h, filter and recover unreacted raw materials, and react the filtrate at 65°C and -0.09Mpa for 1.5 hours to obtain 1.8 kg of transformed oil. Oil tested by liquid phase for vitamin D 3 The cont...
Embodiment 3
[0031] 12 kg of 7-dehydrocholesterol and 260 L of ethanol were added to the batching tank, the temperature was raised to 35° C. with stirring, and a photoreaction solution with a concentration of 4wt% was prepared. The photochemical reaction is carried out by an ultraviolet irradiator with a light source power of 25kw, the temperature of the photoreaction solution is controlled to be 70°C, and the flow rate of the photoreaction solution is controlled at 130L / h, and then the irradiated reaction solution is concentrated under reduced pressure in a concentration pot, and the concentrated The filtrate was transferred to a refrigerated stirring tank at -20°C for freezing and crystallization for 5h, the unreacted raw materials were recovered by filtration, and the filtrate was reacted at 70°C and -0.095Mpa for 1 hour to obtain 1.68 kg of transformed oil, which was detected by liquid phase. of which vitamin D 3 The content of ethyl acetate is 83wt%; the conversion oil and 2 times the...
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