Method and device for extracting tomato seed oil from tomato seeds
A tomato seed oil and tomato seed technology, applied in the direction of fat oil/fat production, fat oil/fat refining, fat production, etc., can solve the problem of low oil yield, unsuitable processing of bulk raw materials for tomato seed production, flammable and explosive solvents, etc. question
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Embodiment 1
[0026] Example 1. Dry the tomato seeds to a moisture content≤13%, and analyze and detect that the oil content is 22%; take 10kg of pre-dried tomato seeds, pulverize them to 40-80 mesh through a pulverizer, put 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 system; 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 by the plunger pump 5 into the extraction kettle, observe the liquid level through the sight glass until the tomato seed raw material is submerged; it is heated by the heater 6, and the heating jacket 8 is kept warm to form an R134A subcritical fluid, which is stirred at 1.0-1.2Mpa and 40-45°C for extraction. Extract 2 times, 45 minutes each time; after the extraction is completed, the extract enters the sepa...
Embodiment 2
[0027] Embodiment 2. What is different from Example 1 is that the tomato seeds are dried at 80-90 degrees through the drying temperature; each extraction time is 45-50min, and the separation time is 20-25min; the remaining steps are the same as in Example 1.
Embodiment 3
[0028] Embodiment 3. A kind of device that extracts tomato seed oil from tomato seed, the output end of tetrafluoroethane gas tank 1 is connected with the input end of tetrafluoroethane liquefaction storage tank 2 by pipeline; 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; Separation kettle 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 system 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 provided on the extraction kettle 7 ; and a heating jacket 10 is provided on the separation kettle 9 .
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