Permanently polarized hydroxyapatite, a process for its manufacture and uses thereof
US-2020180960-A1 · Jun 11, 2020 · US
US9815695B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-9815695-B2 |
| Application number | US-201313891502-A |
| Country | US |
| Kind code | B2 |
| Filing date | May 10, 2013 |
| Priority date | May 30, 2012 |
| Publication date | Nov 14, 2017 |
| Grant date | Nov 14, 2017 |
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Methods and compositions are provided for treatment of an apatite-based resin from which retained solutes have been eluted by an elution buffer that contains an alkali metal salt with solutions of calcium ion, phosphate ion, and hydroxide separately from any sample loading and elution buffers. The treatment solutions restore the resin, reversing the deterioration that is caused by the alkali metal salt in the elution buffer.
Opening claim text (preview).
What is claimed is: 1. A method for increasing the resin mass and particle strength of an apatite-based chromatography resin after purification of a target molecule with said apatite-based chromatography resin, wherein said apatite-based chromatography resin is ceramic hydroxyapatite (CHT), said method comprising: (a) equilibrating said apatite-based chromatography resin; (b) after equilibrating said apatite-based chromatography resin, loading a sample containing a target analyte onto said apatite-based chromatography resin; (c) after loading said sample, eluting said target analyte from said apatite-based chromatography resin by passing a solution of elution buffer through said apatite-based chromatography resin; and (d) after eluting said target molecule, and before subsequent loading of additional target molecule: (i) passing a solution of calcium ion through said apatite-based chromatography resin; (ii) after (i), passing a solution of phosphate ion having a pH of at least about 6.5 through said apatite-based chromatography resin; and (iii) after (ii), passing a solution of hydroxide ion through said apatite- based chromatography resin; wherein (i), (ii), and (iii) are performed at concentrations of said calcium ions, phosphate ions, and hydroxide ions and at volumes of said solution of calcium ion, solution of phosphate ion, and solution of hydroxide ion that are effective to increase the resin mass and particle strength of said apatite-based chromatography resin. 2. The method of claim 1 , further comprising passing an aqueous wash solution through said apatite-based chromatography resin after each of steps (i) and (ii). 3. The method of claim 1 , wherein said solution of calcium ion has a calcium ion concentration of about 10 ppm to about 2000 ppm and is passed through said resin in an amount of about 1.0 resin volume to about 10.0 resin volumes. 4. The method of claim 1 , wherein said solution of calcium ion has a calcium ion concentration of about 30 ppm to about 1000 ppm and is passed through said resin in an amount of about 1.5 resin volumes to about 6.0 resin volumes. 5. The method of claim 1 , wherein said solution of phosphate ion has a pH of about 6.5 to about 9.0, has a phosphate ion concentration of about 50 mM to about 1 M, and is passed through said resin in an amount of about 1.0 resin volume to about 20.0 resin volumes. 6. The method of claim 1 , wherein said solution of phosphate ion has a pH of about 6.5 to about 7.5, has a phosphate ion concentration of about 200 mM to about 750 mM, and is passed through said resin in an amount of about 1.5 resin volumes to about 10.0 resin volumes. 7. The method of claim 1 , wherein said solution of hydroxide ion has a hydroxide ion concentration of about 0.1 M to about 5.0 M and is passed through said resin in an amount of about 1.0 resin volume to about 20.0 resin volumes. 8. The method of claim 1 , wherein said solution of hydroxide ion has a hydroxide ion concentration of about 0.3 M to about 3.0 M and is passed through said resin in an amount of about 1.5 resin volume to about 10.0 resin volumes. 9. The method of claim 1 , wherein said apatite-based chromatography resin is one that has been exposed to said elution buffer at a pH of about 8.0 or below. 10. The method of claim 1 , wherein said apatite-based chromatography resin is one that has been exposed to said elution buffer at a pH of about 6.0 to about 8.0. 11. The method of claim 1 , wherein said apatite-based chromatography resin is one that has been exposed to said elution buffer containing an alkali metal halide at a concentration of at least about 30 mM. 12. The method of claim 1 , wherein said apatite-based chromatography resin is one that has been exposed to said elution buffer containing an alkali metal halide at a concentration of about 30 mM to about 3000 mM. 13. The method of claim 1 , wherein said target molecule is a polypeptide. 14. In a method for purifying target molecules from a plurality of samples on an apatite-based chromatography resin by loading said samples in succession onto said resin and eluting said target molecules from said resin after each such loading with an elution buffer comprising an alkali metal salt, wherein said apatite-based chromatography resin is ceramic hydroxyapatite (CHT), the improvement comprising treating said resin after each target molecule elution and before subsequent sample loading by: (i) passing a solution of calcium ion through said resin; (ii) after (i), passing a solution of phosphate ion having a pH of at least about 6.5 through said resin; and (iii) after (ii), passing a solution of hydroxide ion through said resin; wherein steps (i), (ii), and (iii) are performed at concentrations of said ions and at volumes of said solution of calcium ion, solution of phosphate ion, and solution of hydroxide ion that are effective to increase resin mass and particle strength of said apatite-based chromatography resin. 15. The method of claim 14 , wherein said plurality of samples consists of at least twenty samples. 16. The method of claim 14 , wherein said plurality of samples consists of at least fifty samples. 17. The method of claim 14 , further comprising passing an aqueous wash solution through said resin after each of steps (i), (ii), and (iii). 18. The method of claim 14 , wherein said solution of calcium ion has a calcium ion concentration of about 10 ppm to about 2000 ppm and is passed through said resin in an amount of about 1.0 resin volume to about 10.0 resin volumes. 19. The method of claim 14 , wherein said solution of calcium ion has a calcium ion concentration of about 30 ppm to about 1000 ppm and is passed through said resin in an amount of about 1.5 resin volumes to about 6.0 resin volumes. 20. The method of claim 14 , wherein said solution of phosphate ion has a pH of about 6.5 to about 9.0, has a phosphate ion concentration of about 50 mM to about 1 M, and is passed through said resin in an amount of about 1.0 resin volume to about 20.0 resin volumes. 21. The method of claim 14 , wherein said solution of phosphate ion has a pH of about 6.5 to about 7.5, has a phosphate ion concentration of about 200 mM to about 750 mM, and is passed through said resin in an amount of about 1.5 resin volumes to about 10.0 resin volumes. 22. The method of claim 14 , wherein said solution of hydroxide ion has a hydroxide ion concentration of about 0.1 M to about 5.0 M and is passed through said resin in an amount of about 1.0 resin volume to about 20.0 resin volumes. 23. The method of claim 14 , wherein said solution of hydroxide ion has a hydroxide ion concentration of about 0.3 M to about 3.0 M and is passed through said resin in an amount of about 1.5 resin volume to about 10.0 resin volumes. 24. The method of claim 14 , wherein said elution buffer has a pH of about 8.0 or below. 25. The method of claim 14 , wherein said elution buffer has a pH of about 6.0 to about 8.0.
Affinity chromatography or related techniques based upon selective absorption processes · CPC title
in the liquid phase · CPC title
After-treatment · CPC title
Partition-, reverse-phase or hydrophobic interaction chromatography · CPC title
Equilibration or regeneration · CPC title
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