Dephosphorylation of skim milk, ultra-filtered milk or micellar casein isolate
US-2026053157-A1 · Feb 26, 2026 · US
US11517023B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-11517023-B2 |
| Application number | US-201916564644-A |
| Country | US |
| Kind code | B2 |
| Filing date | Sep 9, 2019 |
| Priority date | Sep 9, 2019 |
| Publication date | Dec 6, 2022 |
| Grant date | Dec 6, 2022 |
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A method of removing one or more antibiotics from a dairy product, the method involve passing the dairy product comprising an antibiotic in a first amount through a bulk comprising, relative to a total bulk weight, at least 75 wt. % of titanium oxide nanostructures, to provide the dairy product comprising the antibiotic in a second, lesser amount, wherein the nanostructures have lengths at least two-fold in excess of their width and height. Bulk materials useful in this or related methods or applications may have loosely tangled, noodle-like morphologies on sub-100 nm scale, and need not employ graphene and/or polymeric support networks in columns, generally having only titanium oxides without silicon or iron oxides.
Opening claim text (preview).
The invention claimed is: 1. A method of removing one or more antibiotics from a first dairy product, the method comprising: passing the first dairy product comprising an antibiotic in a first amount through a bulk comprising, relative to a total bulk weight, at least 75 wt. % of titanium oxide nanostructures, to provide a treated dairy product comprising the antibiotic in a second amount, wherein the first amount is greater than the second amount, and wherein the titanium oxide nanostructures have lengths at least two-fold in excess of their width and height. 2. The method of claim 1 , wherein the titanium oxide nanostructures are nanotubes having an average diameter in a range of from 5 to 200 nm. 3. The method of claim 1 , wherein the titanium oxide nanostructures have a formula H x Na 2-x Ti 2 O 5 ·(H 2 O), wherein x≤2. 4. The method of claim 1 , wherein the first dairy product is milk. 5. The method of claim 1 , wherein the first dairy product is eluted in a carrier having a pH in a range of from 5.0 to 8.0. 6. The method of claim 1 , wherein the bulk is present in the form of a stationary phase within a column packed with the bulk. 7. The method of claim 1 , wherein the bulk comprises no more than 5 wt. % of materials aside from titanium oxide, relative to the total bulk weight. 8. The method of claim 1 , wherein the passing occurs at a pressure in a range of from 2 to 20 bar. 9. The method of claim 1 , wherein the first amount of the antibiotic is in a range of from 10 to 1200 ppm. 10. The method of claim 1 , wherein the second amount of the antibiotic, reached immediately after the passing, is no more than 15% of the first amount. 11. The method of claim 1 , wherein the passing comprises removing no more than 5 wt. % of an original amount of non-antibiotic components of the first dairy product.
Oxides or hydroxides · CPC title
using chemicals in liquid or solid state, e.g. flocculating, adsorbing or extracting agents (A23C9/146 and A23C9/148 take precedence) · CPC title
being in the range 2-50 nm, i.e. mesopores · CPC title
with size in the range 1-100 nanometers, e.g. nanosized particles, nanofibers, nanotubes, nanowires or the like (carbon nanostructures B01J20/205) · CPC title
comprising oxides or hydroxides of metals not provided for in group B01J20/04 · CPC title
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