A treatment process for peony flower residue after supercritical CO2 extraction
A treatment process, peony flower technology, which is applied in the field of peony flower residue reuse, can solve the problems of low utilization value of cosmetic raw materials, waste of functional ingredients in flower water, and reduced antioxidant capacity, so as to improve resource utilization and anti-oxidation. Ability to improve, avoid the effects of property changes
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Embodiment 1
[0026] Embodiment 1 A kind of supercritical CO 2 Processing technology of peony flower residue after extraction
[0027] (1) Subcritical low temperature extraction
[0028] for supercritical CO 2 The extracted peony flower residue is subjected to subcritical low temperature extraction, the extraction agent is dimethyl ether, the weight ratio of the peony flower residue and the extraction agent is 1:2, the extraction temperature is 25 ° C, the pressure is 0.65MPa, the extraction time is 40min, and the extraction The number of times is 6 times, and the evaporation temperature of the recovered solvent is 30 ° C, and dark peony flower water and solid impurities are obtained after extraction;
[0029] (2) Decolorization
[0030] Activated carbon is added to the dark peony flower water obtained in step (1), and the mass ratio of the activated carbon to the dark peony flower water is 3:100, and the decolorization is performed twice for 30min each time;
[0031] (3) Filtration
...
Embodiment 2
[0041] Embodiment 2 A kind of supercritical CO 2 Processing technology of peony flower residue after extraction
[0042] (1) Subcritical low temperature extraction
[0043] for supercritical CO 2 The extracted peony flower residue is subjected to subcritical low temperature extraction, the extraction agent is dimethyl ether, the weight ratio of the peony flower residue to the extraction agent is 1:1.5, the extraction temperature is 40 ° C, the pressure is 0.75MPa, the extraction time is 40min, and the extraction The number of times is 5 times, and the evaporation temperature of the recovered solvent is 40 ° C, and dark peony flower water and solid impurities are obtained after extraction;
[0044] (2) Decolorization
[0045] Activated carbon is added to the dark peony flower water obtained in step (1), and the mass ratio of the activated carbon to the dark peony flower water is 2:100, and decolorization is performed twice for 30min each time;
[0046] (3) Filtration
[00...
Embodiment 3
[0056] Embodiment 3 A kind of supercritical CO 2 Processing technology of peony flower residue after extraction
[0057] (1) Subcritical low temperature extraction
[0058] for supercritical CO 2 The extracted peony flower residue is subjected to subcritical low temperature extraction, the extraction agent is dimethyl ether, the weight ratio of the peony flower residue to the extraction agent is 1:3, the extraction temperature is 22° C., the pressure is 0.45MPa, and the extraction time is 50min. The number of times is 7 times, and the evaporation temperature of the recovered solvent is 25 ° C, and the dark peony flower water and solid impurities are obtained after extraction;
[0059] (2) Decolorization
[0060] Activated carbon is added to the dark peony flower water obtained in step (1), and the mass ratio of the activated carbon to the dark peony flower water is 4:100, and decolorization is performed twice for 30min each time;
[0061] (3) Filtration
[0062] The peony...
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