Acid Zirconium Phosphate and Alkaline Hydrous Zirconium Oxide Materials For Sorbent Dialysis

• US 20130180905A1
• Filed: 03/01/2013
• Published: 07/18/2013
• Est. Priority Date: 09/30/2008
• Status: Active Grant

• Current Assignee: Fresenius Medical Care Holdings Incorporated (Fresenius Medical Care AG)
• Original Assignee: Fresenius Medical Care Holdings Incorporated (Fresenius Medical Care AG)
• Inventors: Wong, Raymond June-Hin
• Granted Patent: US 8,647,506 B2
• Time in Patent Office: Days
• US Class Current: 210/195.2
• CPC Class Codes: A61M 1/1696 with dialysate regeneration
• CPC Class Codes: B01J 39/12 Compounds containing phosphorus
• CPC Class Codes: B01J 41/10 Inorganic material
• CPC Class Codes: B01J 47/04 Mixed-bed processes

Abstract

A combination of acid zirconium phosphate and alkaline hydrous zirconium oxide are utilized as ion-exchange materials, for example, in sorbent dialysis. The combination provides for dialysate regeneration while maintaining constant and controlled levels of Na⁺, HCO₃⁻, and pH.

Claims

1-30. -30. (canceled)

31. An apparatus for conducting dialysis comprising a sorbent cartridge, and a dialyzer in fluid communication with the sorbent cartridge, wherein spent dialysate passes from the dialyzer to and through the sorbent cartridge, and wherein said sorbent cartridge comprising a layer of a mixture of acid zirconium phosphate (AZP) and alkaline hydrous zirconium oxide (NaHZO) in the sorbent cartridge, and wherein said acid zirconium phosphate is the only form of zirconium phosphate present in said layer.

32. The apparatus of claim 31, wherein the spent dialysate is spent hemodialysate, spent peritoneal dialysate, or combinations thereof.

33. The apparatus of claim 31, wherein the dialyzer is in fluid communication with the blood of a patient.

41. The apparatus of claim 31, wherein the cartridge comprises at least two layers, wherein at least one of the layers comprises the combination of AZP and NaHZO.

42. The apparatus of claim 31, wherein the AZP and the NaHZO comprise particles having an average grain size of from about 25 microns to about 60 microns.

43. The apparatus of claim 31, wherein the combination has a pH of from about 3 to about 7.

44. The apparatus of claim 31, wherein the combination has a pH of from about 3.5 to about 4.

45. The apparatus of claim 31, wherein the combination has a pH of from about 5.5 to about 6.

46. The apparatus of claim 31, wherein the AZP and NaHZO are each present in the combination in an amount to produce an NaHZO:

AZP weight ratio of from about 0.2;

0.8 to about 0.8;

0.2.

47. The apparatus of claim 46, wherein the NaHZO:

AZP weight ratio is from about 0.5;

0.5 to about 0.6;

0.4.

48. The apparatus of claim 46, wherein the NaHZO:

AZP weight ratio is from about 0.22;

0.78 to about 0.33;

0.67.

49. The apparatus of claim 31, further comprising zirconium phosphate (ZrP) as an additional layer in the sorbent cartridge.

50. The apparatus of claim 31, further comprising activated carbon, immobilized urease, or combinations thereof.

34. A dialysis system comprising a sorbent cartridge and a source of spent dialysate, wherein the source of the spent dialysate is in fluid communication with the sorbent cartridge and the spent dialysate passes to and through the sorbent cartridge, and wherein said sorbent cartridge comprising a layer of a mixture of acid zirconium phosphate (AZP) and alkaline hydrous zirconium oxide (NaHZO) in the sorbent cartridge, and wherein said acid zirconium phosphate is the only form of zirconium phosphate present in said layer.

35. The dialysis system of claim 34, wherein the spent dialysate passes through the sorbent cartridge at a rate of about 100 ml/min to about 550 ml/min.

36. The dialysis system of claim 34, wherein the spent dialysate is regenerated.

37. The dialysis system of claim 36, wherein the spent dialysate is regenerated to a pH level about equal to that of fresh dialysate.

38. The dialysis system of claim 36, wherein the spent dialysate is regenerated to a Na⁺ level and HCO₃⁻

level about equal to that of fresh dialysate.

39. The dialysis system of claim 36, wherein the spent dialysate is regenerated without formation of CO₂ bubbles.

40. The dialysis system of claim 36, wherein a uniform level of Na⁺ is maintained in the spent dialysate while being regenerated.