Apparatus and method for preparation of a hemodialysis solution optionally containing bicarbonate

• US 4,202,760 A
• Filed: 07/24/1978
• Issued: 05/13/1980
• Est. Priority Date: 07/24/1978
• Status: Expired due to Term

• Current Assignee: Cordis Dow Corp.
• Original Assignee: Cordis Dow Corp.
• Inventors: Hall, Robert C., Storey, L. Robert
• Primary Examiner(s): Hart, Charles N.
• Assistant Examiner(s): Sadowski, David R.
• Application Number:
  US05/927,322
• Time in Patent Office: 659 Days
• Field of Search: 210/321 B, 210/321 A, 210/22, 210/101, 210/188, 210/194, 210/96 M, 137/101.11, 137/90, 137/93, 128/DIG. 3, 222/193, 222/63, 222/61, 222/129.2
• US Class Current: 252/364
• CPC Class Codes: A61M 1/1656 Apparatus for preparing dialysates
• CPC Class Codes: A61M 1/1658 Degasification
• CPC Class Codes: A61M 1/1664 with temperature control
• CPC Class Codes: B01F 25/51 in which the mixture is circulated through a set of tubes, e.g. with gradual introduction of a component into the circulating flow
• CPC Class Codes: Y10T 137/2526 Main line flow displaces or entrains material from reservoir

Abstract

Apparatus and method for make up of a hemodialysis solution and supply of same to an artificial kidney; the solution optionally contains bicarbonate in any desired amount. The apparatus comprises a recirculation loop which mixes a hemodialysis dialysate concentrate with deaerated water and may include another interconnected recirculation loop adopted to form an aqueous bicarbonate solution. Both recirculation loops mix the concentrates in the recirculation fluid in venturi means operated by continuously controlling the velocity of fluid flowing therethrough to create suction to inject the requisite quantity of concentrate to form the final desired composition in the product hemodialysis solution.

Claims

1. Apparatus for preparing dialysate for use in hemodialysis which comprises a main line connected at its inlet end to a water source and at its exit end to an artificial kidney, a dialysate recirculation line connected into said main line at an upstream end and at a spaced downstream end, and including dialysate venturi means connected at its ends into said recirculation line and at its throat portion with a line to a dialysate concentrate tank, conductivity measuring means in said recirculation line adjacent to and downstream of said venturi means, and pump means in said recirculation line downstream of said conductivity measuring means.

2. Apparatus in accordance with claim 1 wherein the speed of said pump means varies in response to variations in the conductivity of said dialysate from a preselected conductivity value.

3. Apparatus in accordance with claim 1 wherein said conductivity means includes temperature compensating means.

4. Apparatus in accordance with claim 1 wherein a bicarbonate recirculation line is interposed between said water source and the upstream end of said dialysate recirculation line, said bicarbonate line comprising bicarbonate venturi means connected at its ends into said bicarbonate line and at its throat portion to a bicarbonate-saline concentrate tank, pump means in said bicarbonate line downstream of said bicarbonate venturi means, and conductivity measuring means in said bicarbonate line downstream of said pump means.

5. Apparatus in accordance with claim 1 wherein a bicarbonate recirculation line is interposed between said water source and the upstream end of said dialysate recirculation line, said bicarbonate line comprising bicarbonate venturi means connected at its ends into said bicarbonate line and at its throat portion to a bicarbonate-saline concentrate tank, a variable flow restriction downstream of and adjacent to the exit side of said bicarbonate venturi, pump means downstream of and adjacent to said variable flow restriction, conductivity measuring means downstream of and adjacent to said pump means, and bubble removal means downstream of and adjacent to said conductivity measuring means.

6. Apparatus for preparing dialysate for use in hemodialysis which comprises a main line connected at its inlet end to a water source and at its exit end to an artificial kidney, a dialysate recirculation line connected into said main line at an upstream end and at a spaced downstream end, and including dialysate venturi means connected at its ends into said recirculation line and at its throat portion with a line to a dialysate concentrate tank, conductivity measuring means in said recirculation line adjacent to and downstream of said venturi means, pump means in said recirculation line downstream of said conductivity measuring means, and a bicarbonate recirculation line interposed between said water source and the upstream end of said dialysate recirculation line, said bicarbonate line comprising bicarbonate venturi means connected at its ends into said bicarbonate line and at its throat portion to a bicarbonate-saline concentrate tank, pump means in said bicarbonate line downstream of said bicarbonate venturi means, and conductivity measuring means in said bicarbonate line downstream of said pump means.

7. Apparatus in accordance with claim 6 wherein the speed of said pump means in said bicarbonate line varies in response to variations in conductivity of said bicarbonate solution from a preselected conductivity value.

8. Apparatus in accordance with claim 6 wherein said conductivity measuring means includes temperature compensating means.

9. A method for continuously formulating dialysate and supplying same to an artificial kidney which comprises the steps of:

(1) establishing a main line between a water supply and an artificial kidney having a recirculation loop therein provided with dialysate venturi means, recirculation pump means and conductivity measuring means,

(2) establishing a water flow in said main line toward said kidney and removing dissolved air and bubbles to form a deaerated stream,

(3) establishing sufficient suction in the throat of said venturi means by recirculation of fluid therethrough to inject dialysate concentrate into said deaerated stream at said throat,

(4) mixing said concentrate with said recirculating fluid in said venturi means and in said recirculation loop, and

(5) said recirculating fluid consisting of a mixture of water and a portion of said dialysate in an amount exceeding the quantity of fresh water fed into said main line by an amount in the range of about 25% to about 300%.

10. A method in accordance with claim 9 wherein said dialysate has the composition of normal dialysate for use in hemodialysis.

11. A method in accordance with claim 9 wherein said dialysate contains sodium acetate in an amount in the range of about 75% to 0% of the sodium acetate concentration in normal dialysate.

12. A method in accordance with claim 9 wherein the suction in said venturi means in step (3) varies responsive to conductivity variations from a preset conductivity range for the desired composition of said dialysate.

13. A method in accordance with claim 9 wherein the quantity of said recirculating fluid is an amount exceeding the quantity of fresh water fed into said main line in the range of about 50% to about 150%.

14. A method for continuously formulating a bicarbonate-containing hemodialysis solution and supplying same to an artificial kidney which comprises the steps of:

(1) establishing a main line between a water supply and an artificial kidney having a dialysate recirculation loop therein provided with dialysate venturi means, recirculation pump means and conductivity measuring means,

(2) establishing a bicarbonate solution recirculation loop in said main line interposed between said dialysate recirculation loop and said water supply, said bicarbonate solution recirculation loop being provided with bicarbonate venturi means, recirculation pump means, conductivity measuring means and air removal means,

(3) establishing a water flow in said main line toward said kidney and into said bicarbonate recirculation loop,

(4) establishing sufficient suction in the throat of said bicarbonate venturi means by recirculation of fluid therethrough to inject bicarbonate concentrate into said fluid at said throat and mixing same therewith to thereby form a deaerated dilute bicarbonate solution,

(5) forwarding said bicarbonate solution to the said dialysate recirculation loop and recirculating a stream of a mixture of said bicarbonate solution and an aqueous solution of other dialysate components through said dialysate venturi means at a velocity to create sufficient suction to inject dialysate concentrate into said stream at the throat of said dialysate venturi means and mixing same therewith in said means and in said dialysate recirculation loop to thereby form bicarbonate-containing hemodialysis solution having the preselected composition,

(6) the portion of said bicarbonate solution recirculating in said bicarbonate recirculation loop exceeding the quantity of fresh water fed into said main line by an amount in the range of about 25% to about 300%, and

(7) the portion of said stream of a mixture of said bicarbonate solution and said bicarbonate-containing hemodialysis solution recirculating in said dialysate recirculation loop exceeding the quantity of bicarbonate solution fed to the upstream end of said dialysate recirculation loop by an amount in the range of about 25% to about 300%.

15. A method in accordance with claim 14 wherein said dialysate contains sodium acetate in an amount in the range of about 75% to 0% of the sodium acetate concentration in normal dialysate.

16. A method in accordance with claim 14 wherein the suction in said venturi means in step (4) varies responsive to conductivity variations from a preset conductivity range for the desired composition of said bicarbonate solution.

17. A method in accordance with claim 14 wherein the suction in the venturi means in step (5) varies responsive to conductivity variations from a preset conductivity range for the desired composition of said hemodialysis solution.

18. A method in accordance with claim 14 wherein the quantity of said recirculating fluids in each of said recirculating loops is an amount in the range of abut 50% to about 150% of the fresh water fed to said main line.