Sodium hyaluronate with full molecular weight distribution (mwd), and preparation method and use thereof
US-2024002551-A1 · Jan 4, 2024 · US
US10376840B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-10376840-B2 |
| Application number | US-201515517439-A |
| Country | US |
| Kind code | B2 |
| Filing date | Oct 7, 2015 |
| Priority date | Oct 7, 2014 |
| Publication date | Aug 13, 2019 |
| Grant date | Aug 13, 2019 |
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The present invention relates to a process for separation of oxyresveratrol molecule from the extracted solution of Artocarpus lakoocha Roxb. through membrane application. The product can be obtained in excellent yield upto 81% in case of extraction using water as solvent and can be separated from the extracted mixture upto 98% using indigenously developed nanofiltration membrane. Only the desired Trans isomer is obtained and no cis isomerization takes place during the extraction process.
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We claim: 1. A process for extraction and separation of oxyresveratrol from heartwood of Artocarpus lakoocha Roxb., said process comprising the steps of: (i) mixing Artocarpus lakoocha Roxb. Powder obtained from the heartwood with water at a temperature in the range of 30° C.-70° C. for 1 to 10 hours to extract a solution and filtering the solution to obtain a solution enriched in oxyresveratrol; (ii) subjecting the solution enriched in oxyresveratrol obtained in step (i) to a membrane treatment in a two compartment membrane cell containing a nanofiltration membrane selected from an Alpha cyclodextrin-polysulfone composite nanofiltration membrane, a Beta cyclodextrin-polysulfone composite nanofiltration membrane or a Gamma cyclodextrin-polysulfone composite nanofiltration membrane by circulating through the nanofiltration membrane with a peristaltic pump at a flow rate in the range of 42.50 ml/min to 107.14 ml/min to obtain oxyresveratrol; and (iii) collecting the oxyresveratrol obtained in step (ii) from feed side of the membrane; wherein the trans membrane pressure across the membrane in step (ii) is maintained within the range of 7.2 psi to 21.75 psi. 2. The process as claimed in claim 1 , wherein the mixing of Artocarpus lakoocha Roxb. powder with water is done at 50° C. 3. The process as claimed in claim 1 , wherein the mixing of Artocarpus lakoocha Roxb. powder with water is done for 4 hours. 4. The process as claimed in claim 1 , wherein the nanofiltration membrane is a beta cyclodextrin-polysulfone composite nanofiltration membrane. 5. The process as claimed in claim 1 , wherein the two compartment membrane cell has a feed side and a permeate side with volumes of 150 ml and 120 ml respectively. 6. The process as claimed in claim 1 , wherein the trans membrane pressure across the membrane is maintained at 14.50 psi. 7. The process as claimed in claim 1 , wherein the membrane is cyclically backwashed with ethanol. 8. The process as claimed in claim 1 , wherein the oxyresveratrol obtained is a trans isomer of oxyresveratrol.
Backflushing · CPC title
Organic material · CPC title
Use of other chemical agents · CPC title
Nanofiltration · CPC title
Polysulfones; Polyethersulfones · CPC title
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