Method for chemically extracting purified water-soluble natural organic substances by solid film
A technology of organic substances and solid membranes, applied in the direction of solvent extraction of liquid solutions, etc., can solve the problems of reducing transmembrane pressure difference, extremely high pressure stability control requirements, and polluting industrial wastewater from extracts, so as to achieve separation efficiency and effect The effect of improving and reducing industrial wastewater discharge and solving potential safety hazards
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[0044] Example 1
[0045] Take 50kg of Pueraria lobata root, add 12 times the amount of water to reflux, extract 1.5 hours each time, extract 2 times, and combine to obtain 1100kg of extract; the extract is ultrafiltered with a ceramic membrane with a pore size of 10nm, and the ultrafiltration permeate is collected about 1000kg; % Trialkyl phosphine oxide-sulfonated kerosene is the extractant, 0.05% NaOH solution is the stripping reagent, the ultrafiltration permeate is extracted and stripped according to the specific implementation steps of the present invention, the membrane extraction temperature is 20℃, and the stripping temperature is 35 ℃; the flow velocity of ultrafiltration permeate, extractant, and stripping liquid are 1.0m / min, 0.25m / min, 0.65m / min, and the membrane extraction time is 12 hours; collect the stripping liquid about 1000kg; Adjust the pH value of the solution to 4 with HCl, pass it through a polyamide resin column, eluting with 70% ethanol, collect the elua...
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[0046] Example 2
[0047] Take 50kg of rhubarb, add 20 times the amount of water to reflux, extract 30min each time, extract 2 times, and combine to obtain 900kg of the extract; the water extract is ultrafiltered with a ceramic composite membrane with a pore size of 20nm to obtain the ultrafiltrate; Adjust the pH to 3.0 with 20% hydrochloric acid solution for the permeate, use 5% trialkylphosphine oxide-sulfonated kerosene as the extractant, 0.5% ammonia as the stripping agent, and extract the ultrafiltration permeate according to the specific implementation steps of the present invention Stripping, membrane extraction temperature is 25℃, stripping temperature is 30℃; the flow speeds of ultrafiltrate, extractant and stripping liquid are 2.0m / min, 0.3m / min, 1.0m / min, and membrane extraction time is 8 hours Collect the back extract about 800kg; concentrate the back extract to 50kg under reduced pressure, adjust the pH to 2 with hydrochloric acid, precipitate, wash the precipitate w...
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[0048] Example 3
[0049] Take 50kg of licorice, add 0.75% ammonia water for 24 times reflux extraction, extract 1 hour each time, extract 3 times, and combine to obtain 1100kg of extract; the extract is ultrafiltered with a ceramic membrane with a pore size of 10nm, and the ultrafiltration permeate is collected about 1050kg , Adjust the pH to 6 with hydrochloric acid, use 20% trialkylphosphine oxide-sulfonated kerosene as the extractant, 0.07% NaOH solution as the stripper, and extract the ultrafiltration permeate according to the specific implementation steps of the present invention. , The membrane extraction temperature is 25°C, the stripping temperature is 40°C, the flow speeds of the ultrafiltrate, extractant, and stripping liquid are 1.0m / min, 0.3m / min, 0.65m / min, respectively. The total amount of membrane extraction and stripping liquid After 12 hours, the stripping solution is about 1000kg; the stripping solution is adjusted to pH 4 with hydrochloric acid, passed through...
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