Process for separating high purity stevioside STV
A stevioside and high-purity technology, which is applied in the process field of separating high-purity stevioside STV, can solve the problems of increasing the application limitation of stevioside and the difference in taste of stevioside, and achieves considerable economic benefits and stable product quality. , the effect of short production cycle
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Embodiment 1
[0012] A process for separating high-purity stevioside STV, the implementation steps are as follows:
[0013] Steviosides containing 50-60% of STV in 80-90% of total glycosides (mass percentage, the same below) are used as raw materials to produce products with STV content of 90% and above:
[0014] Add the mixture of absolute methanol and absolute ethanol in material crystallization tank, methanol: ethanol is 2: 8, the add-on of mixed alcohol is 1500 liters, then drops into 300 kilograms containing STV50-60%, total glucoside 80-90 % steviol glycoside spray-dried products, turn on the agitator: raise the temperature to a slight boil at a rate of 1°C per minute, then keep it warm for 1 hour, start to cool down after the end of the heat preservation, and cool down to 20°C at a rate of 1°C every 4-6 minutes ℃, and then keep warm for 1.5 hours. After the heat preservation is completed, the crystals are separated from the mother liquor as usual, and the solvent in the mother liquor...
Embodiment 2
[0016] A process for separating high-purity stevioside STV, the implementation steps are as follows:
[0017] Use steviol glycosides with 80-90% of total glycosides and 50-60% of STV as raw materials to produce products with STV content of 90% and above:
[0018] Add the mixture of methyl alcohol and ethanol in material crystallization tank, (all adopt absolute methanol and absolute ethanol), methyl alcohol: ethanol is 4: 6, the add-on of mixed alcohol is 1800 liters, then drops into 300 kilograms containing STV 50- For stevioside spray-dried products with 60% and 80-90% total glycosides, turn on the agitator: raise the temperature to a slight boil at a rate of 1°C per minute, then keep it warm for 1 hour, and start to cool down after the heat preservation is over, every 4-6 Reduce the temperature by 1°C per minute to 20°C, and then keep it warm for 1-1.5 hours. After the heat preservation is completed, separate the crystal from the mother liquor as usual, recover the solvent ...
Embodiment 3
[0020] A process for separating high-purity stevioside STV, the implementation steps are as follows:
[0021] Use steviol glycosides with 80-90% of total glycosides and 50-60% of STV as raw materials to produce products with STV content of 90% and above:
[0022] Add the mixture of methyl alcohol and ethanol in material crystallization tank, (all adopt absolute methanol and absolute ethanol), methyl alcohol: ethanol is 1: 9, and the add-on of mixed alcohol is 1200 liters, then drops into 300 kilograms containing STV 50- For stevioside spray-dried products with 60% and 80-90% total glycosides, turn on the agitator: raise the temperature to a slight boil at a rate of 1°C per minute, then keep it warm for 1 hour, and start to cool down after the heat preservation is over, every 4-6 Reduce the temperature by 1°C per minute to 20°C, and then keep it warm for 1.5 hours. After the heat preservation is completed, separate the crystals from the mother liquor as usual, recover the solve...
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