Porous membranes for high pressure filtration
US-12064731-B2 · Aug 20, 2024 · US
US2024344006A1 · US · A1
| Field | Value |
|---|---|
| Publication number | US-2024344006-A1 |
| Application number | US-202218291524-A |
| Country | US |
| Kind code | A1 |
| Filing date | Aug 19, 2022 |
| Priority date | Aug 19, 2021 |
| Publication date | Oct 17, 2024 |
| Grant date | — |
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A method of manufacture of crosslinked, edible, porous hollow fibers and sheet membranes suitable for the manufacture of clean meat products, the hollow fibers and sheet membranes made therefrom and methods of use thereof.
Opening claim text (preview).
1 . A method for manufacturing cross-linked, edible, porous hollow fibers or sheet membranes, comprising: a) providing: i) one or more edible proteins, ii) one or more solvents iii) a formation bath; wherein the one or more solvents or the formation bath also comprise one or more multivalent cations or anions or a buffer solution; b) co-mixing the one or more edible proteins in the one or more solvents to form a mixture; c) extruding the mixture into the formation bath to form an extruded hollow fiber or casting the mixture into the formation bath to form a sheet membrane; and d) exposing the extruded hollow fiber or sheet membrane to an energy source selected from one or more of heat and irradiation sufficient to at least partially crosslink the one or more proteins to form cross-linked, edible, porous hollow fibers or sheet membrane. 2 . The method of claim 1 , further providing one or more edible polysaccharides and, in step b), co-mixing the one or more polysaccharides with the one or more edible proteins in the one or more solvents. 3 . The method of claim 1 , further providing a plasticizer and, in step b) co-mixing the plasticizer with the one or more edible proteins in the one or more solvents. 4 . The method of claim 1 , wherein the one or more proteins are selected from a group consisting of pea, soy, wheat, pumpkin, rice, brown rice, sunflower, canola, chickpea, lentil, mung bean, navy bean, corn, oat, potato, quinoa, sorghum and peanut. 5 . The method of claim 2 , wherein said one or more polysaccharides are selected from a group consisting of agar, chitosan, chitin, alginate, sodium alginate, cellulose, hydroxypropyl cellulose, Methyl cellulose, hydroxypropyl methylcellulose, gellan gum, xanthan gum, pectin, tapioca, guar gum and bean gum. 6 . The method of claim 1 , wherein said one or more solvents are selected from a group consisting of water, acetic acid, citric acid, lactic acid, phosphoric acid, malic acid, tartaric acid, sodium hydroxide, ethanol, glycerin and propylene glycol. 7 . The method of claim 1 , wherein said formation bath comprises one or more of calcium, zinc, magnesium, iron and potassium, in combination with one or more of 1) water, acetic acid, citric acid, lactic acid, phosphoric acid, malic acid, tartaric acid, or one or more of 2) sodium hydroxide and potassium hydroxide. 8 . The method of claim 1 , wherein said ion is selected from the group consisting of Ca2+, Mg2+, Fe3+, Zn2+, tripolyphosphate and trisodium citrate and wherein said selected ion is capable of at least enabling partial crosslinking of the one or more polysaccharides. 9 . The method of claim 1 , wherein said heat in step d) is from about 70° C. to about 140° C., applied under a pressure of from about 0 PSI to about 20 PSI gauge, at a relative humidity of from about 50% to about 100%, for about 2 to about 60 minutes or the hollow fiber or sheet membrane is dipped in a water bath that is from about 60° C. to about 100° C. at atmospheric conditions. 10 . The method of claim 1 , wherein the mixture of step b) is heated. 11 . The method of claim 1 , wherein the co-mixing of step b) is performed at about 0° C. to about 90° C. 12 . The method of claim 1 , wherein said mixture is at a pH of about 10 to about 13 and said formulation bath is at a pH of about 3 to about 5. 13 . The method of claim 12 , wherein after formation said membrane is neutralized to a pH of about 6.8 to about 7.8. 14 . The method of claim 12 , wherein after formation said membrane is neutralized to a pH of about 7.3 to about 7.5. 15 . The method of claim 1 , wherein said irradiation is selected from the group consisting of electron beam, UV light and gamma irradiation. 16 . The method of claim 15 , wherein said irradiation is applied in process or post process. 17 . The method of claim 15 , wherein said irradiation is from about 1 to about 100 kGy or from about 10 to about 50 kGy. 18 . The method of claim 1 , wherein said porosity is from about 1% to about 90%. 19 . The method of claim 1 , wherein said porosity is from about 50% to about 80%. 20 . The method of claim 1 , the method further comprising coating the cross-linked, edible, porous hollow fiber or sheet membrane with a coating to enhance cell adhesion. 21 . The method of claim 20 , wherein said coating is selected from one or more of fibronectin, fibrinogen, laminin, collagen, gelatin or short peptide sequences isolated from those proteins. 22 . The method of claim 21 wherein said short peptide sequences are selected from one of more of the group consisting of RGD, YIGSR, IKVAV, DGEA, PHRSN and PRARI. 23 . The method of claim 1 , the method further comprising modifying the outer surface of the cross-linked, edible, porous hollow fiber to enhance cell adhesion. 24 . The method of claim 1 , the method further comprising coating the cross-linked, edible, porous hollow fiber or sheet membrane with a plasticizer. 25 . The method of claim 23 , wherein said surface modification is selected from one or more of plasma, corona, abrasion, etching, ablation, or sputter coating. 26 . The method of claim 1 , wherein said proteins are powdered or finely milled prior to their dissolution in the solvent. 27 . The method of claim 1 , wherein said proteins are at least 70%, 80%, 90%, 95%, 98%, 99%, 99.9% pure. 28 . The method of claim 1 , wherein said polysaccharides are at least 70%, 80%, 90%, 95%, 98%, 99%, 99.9% pure. 29 . The method of claim 1 , wherein the ratio of protein to polysaccharide in said mixture is from approximately 10:1 to approximately 1:10 or approximately 1:99 to approximately 99:1. 30 . The method of claim 1 , wherein the ratio of protein to polysaccharide in said mixture is approximately 4:1 to approximately 1:4. 31 . The method of claim 1 , wherein the ratio of protein to polysaccharide in said mixture is approximately 1:1 or approximately 7:1. 32 . The method of claim 1 , wherein the formation bath comprises one or more of calcium, zinc, magnesium, iron and potassium, in combination with one or more of i) water, acetic acid, citric acid, lactic acid, phosphoric acid, malic acid, tartaric acid, or one or more of ii) sodium hydroxide and potassium hydroxide. 33 . A hollow fiber or sheet membrane made by the method of claim 1 . 34 . A method for manufacturing cross-linked, edible, porous hollow fibers or sheet membranes, comprising: a) providing: i) one or more edible proteins, ii) one or more edible polysaccharides, iii) one or more solvents and iv) a formation bath, wherein the formation bath comprises one or more of calcium, zinc, magnesium, iron and potassium, in combination with one or more of 1) water, acetic acid, citric acid, lactic acid, phosphoric acid, malic acid, tartaric acid, or one or more of 2) sodium hydroxide and potassium hydroxide; b) co-mixing the one or more edible proteins and one or more edible polysaccharides in the one or more solvents to form a mixture; c) extruding the mixture into the formation bath to form an extruded hollow fibers or casting the mixture to form a sheet membrane; and d) exposing the extruded hollow fiber or sheet membrane to an energy source selected from one or more of heat and irradiation sufficient to at least
Hollow fibers or tubes (hollow fiber modules in general B01D63/02) · CPC title
Use of radiation · CPC title
Cross-linking · CPC title
Plasticizers · CPC title
Specific ratios of components used · CPC title
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