Liquid column packing materials and method for making the same

• US 5,545,317 A
• Filed: 04/17/1995
• Issued: 08/13/1996
• Est. Priority Date: 12/30/1992
• Status: Expired due to Term

• Current Assignee: Dow, Inc.
• Original Assignee: Dow, Inc.
• Inventors: Williams, Dwight E.
• Primary Examiner(s): KIM, SUN U
• Application Number:
  US08/422,803
• Time in Patent Office: 484 Days
• Field of Search: 210/198.2, 210/656, 210/502.1, 502/401, 502/403, 502/405, 530/413, 530/811, 530/812, 530/816, 435/176, 435/177, 435/181, 436/518, 436/524, 436/527, 436/528, 436/532, 427/487, 427/532
• US Class Current: 210/198.2
• CPC Class Codes: B01J 20/28078 Pore diameter
• CPC Class Codes: B01J 20/287 Non-polar phases; Reversed phases
• CPC Class Codes: B01J 20/289 bonded via a spacer
• CPC Class Codes: B01J 20/3204 Inorganic carriers, supports or substrates
• CPC Class Codes: B01J 20/3219 involving a particular spacer or linking group, e.g. for attaching an active group
• CPC Class Codes: B01J 20/3274 Proteins, nucleic acids, polysaccharides, antibodies or antigens
• CPC Class Codes: B01J 20/3282 Crosslinked polymers
• CPC Class Codes: B01J 2220/54 Sorbents specially adapted for analytical or investigative chromatography
• CPC Class Codes: B01J 2220/58 Use in a single column
• CPC Class Codes: B01J 31/0254 on mineral substrates
• CPC Class Codes: B01J 31/08 Ion-exchange resins
• CPC Class Codes: Y10S 530/811 Peptides or proteins is immobilized on, or in, an inorganic carrier
• CPC Class Codes: Y10S 530/812 Peptides or proteins is immobilized on, or in, an organic carrier

Abstract

Packing materials for liquid chromatographic or catalytic columns are prepared by contacting a porous protein-adsorptive particulate or membranous support, such as a porous silica particulate support, with an aqueous solution into which a protein has been dissolved to form a saturated coating of protein on the external surfaces of the porous protein-adsorptive support, removing excess protein that remains in solution by washing, and, then crosslinking the protein in the coating. The result is a packing material which resists further adsorption by many different proteins but which continues to provide the adsorptive or catalytic properties of the groups on the internal surfaces of the porous protein-adsorptive support for separations, analysis, or alteration of small molecules. The packing material of the present invention is particularly useful in HPLC or solid phase extraction columns for direct injection drug analysis in plasma, serum, and urine.

Claims

1. A method for making a packing material for liquid chromatographic or catalytic columns which comprises:

a) providing a porous protein-adsorptive support,

b) providing an aqueous solution into which a protein has been dissolved,

c) contacting said porous protein-adsorptive support with said aqueous solution into which a protein has been dissolved for a sufficient period of time to form, and under conditions which form, a saturated coating of protein on the external surfaces of said porous protein-adsorptive support,

d) removing excess protein that remains in solution, and,

e) crosslinking said saturated coating of protein in situ to form a relatively thin but saturated coating of crosslinked protein on the external surfaces of said porous protein-adsorptive support wherein said relatively thin but saturated coating of crosslinked protein gives a signal obtained by at least one surface selective analytical method for nitrogen which does not exceed 67 percent of that for a bulk amount of the crosslinked protein.

2. The method of claim 1 wherein said porous protein-adsorptive support is a porous silica support.

3. The method of claim 2 wherein the said support is confined in a tube by porous frits at both ends and a sequence of wetting liquids, protein solution, washing liquid, and crosslinking solution is passed through or separately recycled through the tube.

4. The method of claim 2 wherein the said support is suspended in a slurry and exposed to a sequence of:

wetting liquids, excess protein in solution, washing liquid, and crosslinking solution by resuspension of support following solids recovery from each preceding slurry.

5. The method of claim 4 wherein said support, prior to exposure to excess protein in solution, is first dispersed in aqueous-organic cosolvent mixture into which protein is then dissolved, stirred, support recovered and washed free of organic cosolvent.

6. The method of claim 5 wherein the aqueous solvent component of said aqueous-organic cosolvent mixture is at least 1 pH unit from the isoelectric point of the protein initially, the amount of added protein is less than that in a saturated coating, and the pH of the mixture is then adjusted to that which would occur if the pH of the initial aqueous portion was within 1/2 unit of the isoelectric point.

7. The method of claim 2 wherein said protein is of a sufficient molecular size as to be size-excluded from the internal surfaces of said porous silica support prior to crosslinking.

8. The method of claim 1 wherein the said support is a membranous one which is immersed and exposed to a sequence of stirred wetting liquids, excess protein solution, washing liquid, and crosslinking solution by displacing each liquid by the next.

9. The method of claim 1 wherein before said protein has been coated, it has been slightly crosslinked in solution to raise its molecular size while remaining water soluble.

10. The method of claim 1 wherein said protein is selected from the group consisting of serum albumin, bovine serum albumin, egg conalbumin, ovalbumin, and serum α

-glycoprotein, and wherein said protein is crosslinked with a cross-linking agent selected from the group consisting of glutaraldehyde, N, N'"'"' dimethylaminopropyl ethyl-carbodiimide, formaldehyde, and bis (sulfosuccinimidyl) suberate.

11. The method of claim 10 wherein said protein is serum albumin and wherein said crosslinking agent is glutaraldehyde.

12. The method of claim 11 wherein the crosslinked protein is further reacted with sodium cyanoborohydride and tris (hydroxymethyl) aminomethane.

13. The method of claim 12 wherein said porous support is particulate and has a pore size of 30 to 1200 angstroms and said protein in said aqueous solution into which a protein has been dissolved is supplied to the support in an amount greater than 10/D weight percent of the support, where D is the support particle diameter in micrometers, and wherein said aqueous solution into which a protein has been dissolved is supplied to the support in an amount between 100 percent and 10,000 percent of the support, the pH of the said aqueous solution is 4.3 to 5.3, the contact time is 5 minutes to 24 hours at 4°

C. to 70°

C., and the crosslinking step takes place for 15 minutes to 24 hours at a temperature of 4°

C. to 40°

C.