Method for production of cellulose nano crystals from cellulose-containing waste material
US-9464142-B2 · Oct 11, 2016 · US
US11780936B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-11780936-B2 |
| Application number | US-202017010808-A |
| Country | US |
| Kind code | B2 |
| Filing date | Sep 2, 2020 |
| Priority date | Apr 25, 2020 |
| Publication date | Oct 10, 2023 |
| Grant date | Oct 10, 2023 |
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A method for extracting and purifying Dendrobium officinale polysaccharides comprises following steps: (1) fully disperse Dendrobium officinale powder in pure water to obtain crude liquid; (2) removing insoluble impurities from the crude liquid through a microfiltration membrane to obtain permeate 1 and retentate 1; (3) performing macroporous ultrafiltration treatment of the permeate 1 and collect permeate 2 and retentate 2; (4) adding an aqueous solution of edible alkali metal inorganic salt to the retentate 2, fully stirring and dissolving to obtain polysaccharide crude liquid, performing macroporous ultrafiltration treatment and collecting permeate 3 and retentate 3; (5) combining the permeate 2 and permeate 3, adding the combined permeate into an electrodialysis device for desalination, and collecting dilute solution and concentrated solution; (6) performing microporous ultrafiltration treatment of the dilute solution and collect retentate 4 and permeate 4; (7) carrying out freeze-drying of the retentate 4 to obtain Dendrobium officinale polysaccharides.
Opening claim text (preview).
The invention claimed is: 1. A method for extracting and purifying Dendrobium officinale polysaccharides, comprising following steps: (1) taking Dendrobium officinale powder and fully dispersing it in pure water to obtain crude liquid; (2) removing insoluble impurities from the crude liquid obtained in the step (1) through a microfiltration membrane to obtain permeate 1 and retentate 1; (3) performing ultrafiltration treatment of the permeate 1 collected in the step (2) through a macroporous ultrafiltration membrane with a molecular weight cut-off of 100-800 kDa, and collecting permeate 2 and retentate 2; (4) adding 0.5-1.5 mol/L of aqueous solution of edible alkali metal inorganic salt to the retentate 2 collected in the step (3), stirring and fully dissolving to obtain polysaccharide crude liquid, performing ultrafiltration treatment through a macroporous ultrafiltration membrane with a molecular weight cut-off of 100-800 kDa, and collecting permeate 3 and retentate 3; (5) combining the permeate 2 and permeate 3 obtained in the step (3) and step (4), adding the combined permeate into an electrodialysis device for desalination, and collecting dilute solution and concentrated solution; (6) performing ultrafiltration treatment of the dilute solution obtained in the step (5) through an ultrafiltration membrane with a molecular weight cut-off of 3 kDa-8 kDa and collecting retentate 4 and permeate 4; (7) carrying out freeze-drying of the retentate 4 obtained in the step (6) to obtain Dendrobium officinale polysaccharides. 2. The method for extracting and purifying Dendrobium officinale polysaccharides according to claim 1 , wherein the concentration of Dendrobium officinale in the crude liquid is 10-30 wt %. 3. The method for extracting and purifying Dendrobium officinale polysaccharides according to claim 1 , wherein conditions of the microfiltration membrane treatment are as follows: operating temperature is 25-50° C., transmembrane pressure is 0.3-0.6 MPa, flow rate of feed liquid is 0.2-0.5 L/min. 4. The method for extracting and purifying Dendrobium officinale polysaccharides according to claim 1 , wherein in the steps (3) and (4), the molecular weight cut-off of the macroporous ultrafiltration membrane is 300-800 kDa. 5. The method for extracting and purifying Dendrobium officinale polysaccharides according to claim 4 , wherein in the steps (3) and (4), the molecular weight cut-off of the macroporous ultrafiltration membrane is 500 kDa. 6. The method for extracting and purifying Dendrobium officinale polysaccharides according to claim 1 , wherein conditions of the ultrafiltration treatment are as follows: operating temperature is 25-50° C., transmembrane pressure is 0.3-0.6 MPa, flow rate of feed liquid is 0.2-0.5 L/min. 7. The method for extracting and purifying Dendrobium officinale polysaccharides according to claim 1 , wherein in the step (4), the edible alkali metal inorganic salt is one of NaCl, Na 2 SO 4 , KCl, K 2 SO 4 or a mixture thereof. 8. The method for extracting and purifying Dendrobium officinale polysaccharides according to claim 1 , wherein the aqueous solution of the edible alkali metal inorganic salt is 0.5-1.5 M NaCl aqueous solution or 0.5-1M Na 2 SO 4 aqueous solution. 9. The method for extracting and purifying Dendrobium officinale polysaccharides according to claim 8 , wherein the aqueous solution of the edible alkali metal inorganic salt is 0.5M NaCl aqueous solution or 0.5M Na 2 SO 4 aqueous solution. 10. The method for extracting and purifying Dendrobium officinale polysaccharides according to claim 1 , wherein conditions of the ultrafiltration treatment are as follows: pH of feed liquid is 4-10, operating temperature is 25-50° C., transmembrane pressure is 0.3-0.6 MPa, and flow rate of feed liquid is 0.2-0.5 L/min. 11. The method for extracting and purifying Dendrobium officinale polysaccharides according to claim 10 , wherein in the step (4), the conditions of the ultrafiltration treatment are as follows: pH of the feed liquid is 6-7, operating temperature is 30-35° C., and flow rate of feed liquid is 0.2-0.5 L/min. 12. The method for extracting and purifying Dendrobium officinale polysaccharides according to claim 1 , wherein in the step (6), the molecular weight cut-off of the ultrafiltration membrane is 3-5 kDa. 13. The method for extracting and purifying Dendrobium officinale polysaccharides according to claim 1 , wherein in the step (6), the molecular weight cut-off of the ultrafiltration membrane is 5 kDa.
comprising multiple electrodialysis steps · CPC title
Multistep processes comprising different kinds of membrane processes selected from ultrafiltration or microfiltration · CPC title
General processes for their isolation or fractionation, e.g. purification or extraction from biomass · CPC title
Ultrafiltration · CPC title
comprising multiple ultrafiltration steps · CPC title
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