Degassing membrane for dialysis

Patent metadata

Field	Value
Publication number	US-2016166752-A1
Application number	US-201414566692-A
Country	US
Kind code	A1
Filing date	Dec 10, 2014
Priority date	Dec 10, 2014
Publication date	Jun 16, 2016
Grant date	—

Abstract

The degasser can have a degassing membrane that can be constructed from non-porous silica. The degassing membrane can be highly permeable to carbon dioxide but less permeable oxygen or nitrogen gases. Pressure in the dialysate and the degasser can be controlled in order to control the amount of carbon dioxide and other gases in dialysate leaving the degasser. The degassing membrane may be placed in a degassing module in a dialysate flow path to remove dissolved carbon dioxide from the dialysate.

First claim

We claim:

1 . A degassing system, comprising:
a degassing vessel having a dialysate passage exposed to a first side of a degassing membrane having a permeability coefficient of carbon dioxide greater than the permeability coefficient of oxygen and/or nitrogen; the membrane positioned in the degassing vessel to contact a dialysate containing dissolved carbon dioxide; a shell side of the degassing vessel exposed to a second side of the degassing membrane for removing gas; and a vacuum pump connected to the shell side of the degassing vessel to create a low pressure vacuum on the second side of the degassing membrane.

2 . The degassing system of claim 1 , wherein the membrane has a permeability coefficient of carbon dioxide that is any one of about 2.0, 2.5, 3.0, 3.5, 4.0, 4.5 or 5.0 times greater than the permeability coefficient of oxygen and/or the permeability coefficient of carbon dioxide is any one of about 2.0, 2.5, 3.0, 3.5, 4.0, 4.5, 5.0, 5.5, 6.0, 6.5, 7.0, 7.5, 8.0, 8.5, 9.0, 9.5, 10.0, 10.5, or 11.0 times greater than the permeability coefficient of nitrogen.

3 . The degassing system of claim 1 , wherein the membrane is constructed from non-porous silicone or poly(dimethylsiloxane).

4 . The degassing system of claim 1 , wherein the membrane has a surface area of between any of 1.0-3.5 m 2 , 1.5-2.0 m 2 , 2.0-2.5 m 2 , or 2.5-3.0 m 2 .

5 . The degassing system of claim 1 wherein the membrane is compatible with temperatures of at least 80° C.

6 . The degassing system of claim 1 wherein the membrane is compatible with a 2% citric acid solution and/or the membrane is compatible with bleach.

7 . The degassing system of claim 1 wherein the vacuum pump is any of a gear pump, peristaltic pump, diaphragm pump or impeller pump.

8 . The degassing system of claim 1 , wherein the degassing vessel further comprises a fluid inlet and a fluid outlet; wherein dialysate flows into the degassing vessel through the fluid inlet and exits the degassing vessel through the fluid outlet.

9 . The degassing system of claim 8 , wherein the fluid inlet is at a lower elevation than the fluid outlet, such that dialysate travels vertically upward through the degassing vessel.

10 . The degassing system of claim 8 , wherein the fluid inlet is at a higher elevation than the fluid outlet, such that dialysate travels vertically downward through the degassing vessel.

11 . A method, comprising the steps of:
contacting a solution containing dissolved carbon dioxide with a first side of a degassing membrane in a degasser, wherein the concentration of a gas on the first side of the degassing membrane is higher than the partial pressure of the gas on a second side of the degassing membrane opposite to the first side, and wherein the degassing membrane has a permeability coefficient for carbon dioxide that is greater than the permeability coefficient for nitrogen and/or oxygen; and controlling the gas pressure on the second side of the degassing membrane to control the concentration of carbon dioxide at an outlet of the degasser.

12 . The method of claim 11 , wherein the degassing membrane has a permeability coefficient of carbon dioxide that is any one of about 2.0, 2.5, 3.0, 3.5, 4.0, 4.5 or 5.0 times greater than the permeability coefficient of oxygen and/or the permeability coefficient of carbon dioxide is any one of about 2.0, 2.5, 3.0, 3.5, 4.0, 4.5, 5.0, 5.5, 6.0, 6.5, 7.0, 7.5, 8.0, 8.5, 9.0, 9.5, 10.0, 10.5, or 11.0 times greater than the permeability coefficient of nitrogen.

13 . The method of claim 11 wherein the pressure on the second side of the degassing membrane is controlled between a predetermined limits.

14 . The method of claim 11 wherein the rate of flow of the dialysate contacting the degassing membrane is between any of 50 and 800 mL/min, 150 and 750 mL/min, 250 and 375 mL/min, 75 and 200 mL/min, 150 and 300 mL/min, 250 and 500 mL/min, or 400 and 800 mL/min.

15 . The method of claim 11 used for degassing a dialysis fluid.

16 . The method of claim 15 wherein the dialysis fluid is an ultrafiltrate.

17 . The method of claim 15 wherein the dialysis fluid is a dialysate.

18 . The method of claim 11 , wherein the method is used for degassing blood to be returned to a patient.

19 . The method of claim 11 wherein the degasser is located in a flow path that is parallel to a dialysate flow path.

20 . The method of claim 11 wherein the degasser is located in a dialysate flow path.

Assignees

• Medtronic Inc

Inventors

• Meyer Thomas E

Classifications

• B01D19/0073

  by a method not covered by groups B01D19/0005 - B01D19/0042 · CPC title

• A61M1/1658 Primary

  Degasification · CPC title

• B01D19/0063

  Regulation, control including valves and floats (for construction and details of valves F16K) · CPC title

• B01D71/701

  Polydimethylsiloxane · CPC title

• B01D19/0031

  by filtration · CPC title