Method for enriching active ingredient of seal oil
An active ingredient, the technology of seal oil, applied in the direction of oil/fat refining, fat production, etc., can solve the problems of many steps, complicated process, limited application of seal oil, etc., and achieve the effect of short residence time and simple process
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Embodiment 1
[0014] In the feeder of self-made molecular distillation device (feeder volume 300ml, evaporation area 1.2 square meters, wiper rotating speed 100~1000rpm), add 1L seal oil crude product, containing 3-PUFA 17.4%. Turn on the raw material preheating device and raise the temperature to 100°C. Turn on the cooling device and keep the cooling temperature at 40°C (the condensation temperature should not be too low to cause the viscosity of the distillate to be too high and affect the flow), add liquid nitrogen to the cold trap, turn on the rotary vane vacuum pump, and make the operating pressure of the system reach 1.5 Pa, turn on the oil diffusion pump after 20 minutes, and the system pressure reaches 0.6Pa. Turn on the precision constant temperature tank for evaporating materials to heat the heat transfer oil, make the temperature stable to 180°C first, then set the temperature to 290°C, and start feeding after reaching the target temperature, the feeding rate is 20mL / min, the wip...
Embodiment 2
[0016] In the feeder of self-made molecular distillation device (same as above), add 1L seal oil crude product, contain 3-PUFA 18.8%. Turn on the raw material preheating device and raise the temperature to 100°C. Turn on the cooling device, keep the cooling temperature at 50°C, add liquid nitrogen to the cold trap, turn on the rotary vane vacuum pump, and make the operating pressure of the system reach 1.5Pa, turn on the oil diffusion pump after 20 minutes, and the system pressure reaches 0.8Pa. Turn on the precision constant temperature tank for evaporating materials to heat the heat transfer oil, make the temperature stable to 180°C first, then set the temperature to 310°C, and start feeding after reaching the target temperature, the feeding rate is 60mL / min, the wiper The rotating speed is 300rpm. After the distillation process, 486mL of distillate and 505mL of heavy fraction are obtained; the content of 3-PUFA in the final product reaches 28.3%.
Embodiment 3
[0018] Add 1L crude seal oil, containing 3-PUFA15.3%, into the feeder of the self-made molecular distillation device (same as above). Turn on the raw material preheating device and raise the temperature to 100°C. Turn on the cooling device, keep the cooling temperature at 60°C, add liquid nitrogen to the cold trap, turn on the rotary vane vacuum pump, so that the operating pressure of the system reaches 1.5Pa, and turn on the oil diffusion pump after 20 minutes, and the system pressure reaches 0.1Pa. Turn on the precision constant temperature tank for evaporating materials to heat the heat transfer oil, make the temperature stable to 180°C first, then set the temperature to 330°C, and start feeding after reaching the target temperature. The feed rate is 80mL / min, and the wiper The rotating speed is 350rpm. After the distillation process, 484mL of distillate and 504mL of heavy fraction are obtained; the content of 3-PUFA in the final product reaches 27.6%.
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