Method and device for extracting pepper seed oil from pepper seeds
A technology of prickly ash seed oil and prickly ash seed is applied in the directions of fat oil/fat production, fat oil/fat refining, fat production, etc., and can solve the problems of low oil yield, influence, high manufacturing cost and operating cost
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Embodiment 1
[0026] Embodiment 1. Dry the pepper seeds to a water content of ≤13%, and analyze and detect that the oil content is 27.5%; weigh 10 kg of pre-dried pepper seeds, crush them to 40-80 mesh through a pulverizer, put them into the extraction kettle 7, and close Feed valve, use vacuum pump 3 to evacuate down to 1×10 4 below pa, discharge the air in the extraction kettle; then pass the R134A gas in the gas tank 1 into the liquefaction storage tank 2, and condense it into a liquid solvent through the condensation jacket 4; the R134A solution stored in the storage tank 2 is pumped into In the extraction kettle, observe the liquid level through the sight glass until the raw material of prickly ash is submerged; it is heated by the heater 6, and the heating jacket 8 is kept warm to form R134A subcritical fluid, which is stirred at 1.0-1.2Mpa and 40-45°C for extraction and co-extraction 3 times, 45min for the first time, 30min for the 2nd and 3rd times; after the extraction is completed...
Embodiment 2
[0027] Embodiment 2. What is different from Example 1 is that the pepper seeds are dried at a temperature of 50-60 degrees; each extraction time is 35-40min, and the separation time is 20-25min; the remaining steps are the same as in Example 1.
Embodiment 3
[0028] Embodiment 3. A device for extracting pepper seed oil from Zanthoxylum bungeanum, the output end of the tetrafluoroethane gas tank 1 is connected with the input end of the tetrafluoroethane liquefaction storage tank 2 through a pipeline; the tetrafluoroethane liquefaction storage tank The output end of 2 is connected with extraction kettle 7 through plunger pump 5, heater 6, and the output end of extraction kettle 7 is connected with the input end of separation kettle 9 by pipeline; Separator 9 is connected compressor 11, condenser 12 sequentially through pipeline , and connected between the tetrafluoroethane gas tank 1 and the tetrafluoroethane liquefaction storage tank 2; a vacuum pump 3 is provided on the extraction kettle 7; a condensation jacket 4 is provided on the tetrafluoroethane liquefaction storage tank 2; A heating insulation jacket 8 is arranged on the extraction kettle 7; a heating jacket 10 is arranged on the separation kettle 9.
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