Method for extracting useful components from high-water-content plant raw materials
A water plant and extraction technology, which is applied in the direction of solid solvent extraction, etc., can solve problems such as labor-consuming, time-consuming, loss, and raw material loss
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Embodiment 1
[0016] Example 1: Extraction of fresh capsicum pigment: After removing seeds and grinding fresh capsicum, take 3000 kg and send it into an extractor with a pressure vessel structure. After closing the feeding channel, the pressure in the device is reduced to - 0.08Mpa, into the liquefied methyl ether extraction solvent for 8 countercurrent extractions, the extraction time is 150-200 minutes, the extraction temperature is 20°C-35°C, the extraction pressure is 0.6Mpa-0.9Mpa; during the extraction process, mechanical stirring is carried out continuously to ensure Improve extraction efficiency. The extract obtained from the extraction enters the evaporation system to vaporize the solvent and separate the extract, and then obtain the crude plant extract product with more water and capsanthin and capsaicin as useful components. After the extraction is completed, the extract in the extractor is pumped out, and the outlet valve of the extractor is opened to vaporize the solvent adsorb...
Embodiment 2
[0017] Example 2: Extraction of marigold lutein: the marigold flower treated by breaking the wall is drained and pulverized after surface moisture, and 3000 kg is taken, and sent to an extractor with a pressure vessel structure. After closing the feed channel, the air is extracted. Make the internal pressure drop to -0.08Mpa. Put in the liquefied methyl ether extraction solvent and carry out 6 countercurrent extractions, the extraction time is 120-160 minutes, the extraction temperature is 20°C-35°C, and the extraction pressure is 0.6Mpa-0.9Mpa. The extracted extract enters the evaporation system to vaporize the solvent and separate the extract to obtain a multi-water plant extract product with marigold lutein as the useful ingredient. After the extraction was completed, the solvent in the material was removed according to the conditions in Example 1, the marigold residue was discharged from the extractor, and the solvent was recovered for recycling.
Embodiment 3
[0018] Example 3: Extraction of plant alkaloids: 3000 kg of freshly picked tobacco leaves are crushed and sent to an extractor with a pressure vessel structure. After closing the feeding channel, the air is drawn out to reduce the pressure inside the device to -0.08 MPa. Pour in the liquefied methyl ether extraction solvent for 4 countercurrent extractions, the extraction time is 100-150 minutes, the extraction temperature is 20°C-35°C, and the extraction pressure is 0.6Mpa-0.9Mpa. The extract obtained by extraction enters the evaporation system to vaporize the solvent and separate the extract, so as to obtain the crude product of polyhydric plant alkaloid with nicotine as the main component. After the extraction is completed, the solvent in the material is removed according to the conditions in Example 1, the tobacco leaves are taken out from the extractor, and the solvent is recovered for recycling.
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