A kind of production method of low-soluble residual capsanthin
A technology of capsanthin and its production method, which is applied in the field of extraction using antioxidants, can solve the problems of high color value loss of capsanthin, unfavorable industrial continuous production, and low removal efficiency, so as to avoid pigment loss and reduce color value Loss, the effect of short processing time
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Embodiment 1
[0029] 1) Using capsanthin crude product with 5% solvent content after removing capsaicin as raw material, add 0.3% tocopherol (directly added, no need to dissolve in solvent).
[0030] 2) The crude product of capsanthin containing antioxidant is subjected to secondary series series removal, and the removal equipment is a short-range evaporator. The first-level and second-level removal equipment are all heated by hot water. The temperature of the hot water is 65°C and 68°C. The pressures of the first-level and second-level removal equipment are -0.090MPa and -0.0999Mpa respectively. Nitrogen gas with a purity of 99.99% (volume fraction) is introduced, and the nitrogen flow rate is 10m 3 / h.
[0031] The deresidue time of capsanthin in this process is 30 minutes (the time of passing through the two-stage series short-range evaporator).
[0032] 3) Enter the condenser after the second stage of residue removal, and the temperature of the finished capsanthin pigment drops to 20°...
Embodiment 2
[0034] 1) Using capsanthin crude product with capsaicinoid removed and solvent content of 1% as raw material, add 0.8% mixture of tocopherol and tea polyphenol antioxidant (mass ratio 1:1). Add directly, no need to dissolve in solvent.
[0035] 2) The crude product of capsanthin containing antioxidant is subjected to secondary series series removal, and the removal equipment is a short-range evaporator. The primary and secondary removal equipment are all heated by hot water, the temperature of hot water is 62°C and 70°C in turn, the pressure of the primary and secondary removal equipment is -0.100MPa, -0.100Mpa respectively, and the secondary short-path evaporator Introduce carbon dioxide gas with a purity of 99.95%, and the gas flow rate is 1m 3 / h.
[0036] 3) Enter the condenser after the second stage of residue removal, and the temperature of the finished capsanthin pigment drops to 23°C. The color value yield of capsanthin is 99.9%, and the total organic solvent residu...
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