Systems and Methods of Urea Processing to Reduce Sorbent Load

• US 20100184198A1
• Filed: 01/16/2009
• Published: 07/22/2010
• Est. Priority Date: 01/16/2009
• Status: Abandoned Application

• Current Assignee: Fresenius Medical Care Holdings Incorporated (Fresenius SE & Co. KGaA)
• Original Assignee: Fresenius Medical Care Holdings Incorporated (Fresenius SE & Co. KGaA)
• Inventors: Gabrielaityte, Lina, Joseph, Russell T., Mishelevich, David J.
• Application Number:
  US12/355,102
• Publication Number:
  US 20100184198A1
• Time in Patent Office: Days
• US Class Current: 435/266
• CPC Class Codes: A61M 1/1696 with dialysate regeneration
• CPC Class Codes: H01M 8/0656 by electrochemical means H01M8/065 takes precedence
• CPC Class Codes: Y02E 60/50 Fuel cells

Abstract

The present invention provides novel methods for removal and disposal of ammonia from spent dialysate in a dialysis system. Ammonium ions present in spent dialysate are converted into gaseous ammonia by raising the pH of the spent dialysate solution in a first reactor. Gaseous ammonia diffuses through a semi-permeable hydrophobic membrane at the outlet of the first reactor and into a second reactor via a gas channel. The second reactor converts gaseous ammonia into an ammonium compound for easy disposal.

Claims

1. A method of removing ammonia from a stream of used dialysate solution in a dialysis system, the method comprising:

passing the stream of used dialysate solution having a pH through a first reactor;

raising the pH of the stream of used dialysate solution in said first reactor to a level sufficient to substantially convert ammonium ions in said stream to gaseous ammonia;

releasing the gaseous ammonia from said stream by allowing it to diffuse through a semi-permeable hydrophobic membrane at the outlet of said first reactor;

receiving the gaseous ammonia through a gas channel into a second reactor; and

capturing and removing the gaseous ammonia in said second reactor.

2. The method of claim 1, wherein the step of capturing and removing the gaseous ammonia in said second reactor further comprises converting the ammonia gas into nitrogen and hydrogen by electrolysis in the presence of H₂O and KOH.

3. The method of claim 2, wherein the hydrogen released in ammonia electrolysis is channeled to a hydrogen fuel cell.

4. The method of claim 1, wherein the step of capturing and removing the gaseous ammonia in said second reactor further comprises the steps of converting gaseous ammonia into an ammonium compound by mixing it with an acidic stream and exposing it to industrial zeolite.

5. The method of claim 1, wherein the step of capturing and removing the gaseous ammonia in said second reactor further comprises the steps of converting gaseous ammonia into an ammonium compound by mixing with an acidic stream and converting said ammonium compound into struvite by reacting it with magnesium salts and phosphorous.

6. The method of claim 1, wherein said second reactor is a bio-reactor and the step of capturing and removing the gaseous ammonia comprises using a microorganism for oxidizing ammonia to nitrite.

7. The method of claim 6, wherein said microorganism is nitrosomonas europea.

8. The method of claim 1, wherein said second reactor comprises a three-sided horseshoe housing and the step of capturing and removing the gaseous ammonia further comprises the steps of converting gaseous ammonia into an ammonium compound by mixing it with an acidic stream, filling said horseshoe housing with an aqueous fluid devoid of ammonium ions, and extracting ammonium into said aqueous fluid by diffusion.

9. The method of claim 1, wherein the release of gaseous ammonia from the dialysate stream is assisted by a vacuum or suction device in the gas channel.

10. The method of claim 1, wherein said first reactor and said second reactor are disposable.

11. A system for removing ammonia from a stream of used dialysate solution during dialysis, the system comprising:

a first reactor through which the stream of used dialysate solution is passed and its pH raised such that ammonium ions in said stream are substantially converted to gaseous ammonia, wherein said gaseous ammonia is released from said stream by diffusion through a semi-permeable hydrophobic membrane at the outlet of said first reactor; and

a second reactor for receiving the gaseous ammonia from the first reactor via a gas channel, wherein said second reactor captures and removes the gaseous ammonia.

12. The system of claim 11, wherein capturing and removing the gaseous ammonia in said second reactor comprises converting the ammonia gas into nitrogen and hydrogen by electrolysis in the presence of H₂O and KOH.

13. The system of claim 12, wherein the hydrogen released in ammonia electrolysis is channeled to a hydrogen fuel cell.

14. The system of claim 11, wherein capturing and removing the gaseous ammonia in said second reactor further comprises converting gaseous ammonia into an ammonium compound by mixing it with an acidic stream and using industrial zeolite to capture the ammonium.

15. The system of claim 11, wherein capturing and removing the gaseous ammonia in said second reactor further comprises converting gaseous ammonia into an ammonium compound by mixing with an acidic stream and converting said ammonium compound into struvite by reacting with magnesium salts and phosphorous.

16. The system of claim 11, wherein said second reactor is a bio-reactor and capturing and removing the gaseous ammonia comprises using a microorganism for oxidizing ammonia to nitrite.

17. The system of claim 16, wherein said microorganism is nitrosomonas europea.

18. The system of claim 11, wherein said second reactor comprises a three-sided horseshoe housing and capturing and removing the gaseous ammonia further comprises converting gaseous ammonia into an ammonium compound by mixing it with an acidic stream, filling said horseshoe housing with an aqueous fluid devoid of ammonium ions, and extracting ammonium into said aqueous fluid by diffusion.

19. The system of claim 11 further comprising a vacuum or suction device in the gas channel for assisting the release of gaseous ammonia from the dialysate stream.

20. The system of claim 11, wherein said first reactor and said second reactor are disposable.