Method for producing lycopene oleoresin
A technology of lycopene oil and resin, applied in chemical instruments and methods, azo dyes, organic dyes, etc., can solve the problems of high cost, non-flammability, low corrosiveness, etc., and achieves low investment, high production efficiency, and no irritation. sexual effect
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Embodiment 1
[0020] 750kg of dehydrated tomato block raw materials, wherein the content of lycopene is 0.58‰, put into the extraction kettle of subcritical extraction after crushing, use 1,1,1,2-tetrafluoroethane as the extraction agent, and the extraction temperature is controlled at 30°C. The pressure is 0.8Ma, the extraction time is 2h, the extractant is separated, and the extractant is reinjected into the extraction kettle to repeat the extraction 3 times, the extraction and separation time is 8h in total, and 12kg of lycopene oleoresin crude extract is obtained in the separation kettle; lycopene oil The content of lycopene in the crude extract of resin is 0.96%, and the content of lycopene in the raffinate of tomato powder is 0.37‰.
Embodiment 2
[0022] 1150 kg of dehydrated tomato block raw materials, wherein the content of lycopene is 0.58‰, is put into the extraction kettle of subcritical extraction, with 1,1,1,2-tetrafluoroethane as the extraction agent, the extraction temperature is controlled at 36 ° C, and the pressure is 0.8MPa, the extraction time is 2h, the extractant is separated, and the extractant is reinjected into the extraction kettle to repeat the extraction 3 times, the extraction and separation time is 8h in total, and 21kg of lycopene oleoresin crude extract is obtained in the separation kettle; The content of lycopene in the crude extract is 0.96%, and the content of lycopene in the raffinate of tomato powder is 0.37‰.
Embodiment 3
[0024] 1000kg of dehydrated tomato block raw materials, in which the content of lycopene is 0.76‰, is put into the extraction kettle of subcritical extraction, with 1,1,1,2-tetrafluoroethane as the extraction agent, the extraction temperature is controlled at 35°C, and the pressure is 0.8Ma, the extraction time is 2h, the extraction agent is separated, and the extraction agent is reinjected into the extraction kettle to repeat the extraction 3 times, the extraction and separation time is 8h in total, and 20kg of lycopene oleoresin crude extract is obtained in the separation kettle; The content of lycopene in the crude extract is 0.97%, and the content of lycopene in the extract of tomato powder is 0.21‰.
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