The patent badge is an abbreviated version of the USPTO patent document. The patent badge does contain a link to the full patent document.

The patent badge is an abbreviated version of the USPTO patent document. The patent badge covers the following: Patent number, Date patent was issued, Date patent was filed, Title of the patent, Applicant, Inventor, Assignee, Attorney firm, Primary examiner, Assistant examiner, CPCs, and Abstract. The patent badge does contain a link to the full patent document (in Adobe Acrobat format, aka pdf). To download or print any patent click here.

Date of Patent:
May. 06, 2025

Filed:

Apr. 25, 2024
Applicant:

Fresenius Medical Care Deutschland Gmbh, Bad Homburg, DE;

Inventors:

Thierry Eyrard, Lyons, FR;

Philippe Laffay, Sainte-Foy-les-Lyon, FR;

Benoit Luaire, Sourcieux-les-Mines, FR;

Assignee:
Attorney:
Primary Examiner:
Int. Cl.
CPC ...
A61M 1/16 (2005.12); A61K 9/08 (2005.12); A61K 33/14 (2005.12); B01F 21/00 (2021.12); B01F 21/10 (2021.12); B01F 23/53 (2021.12); B01F 25/50 (2021.12); B01F 25/52 (2021.12); B01F 35/21 (2021.12); A61K 9/00 (2005.12); B01F 23/50 (2021.12);
U.S. Cl.
CPC ...
A61M 1/1656 (2012.12); A61K 9/08 (2012.12); A61K 33/14 (2012.12); B01F 21/02 (2021.12); B01F 21/10 (2021.12); B01F 23/53 (2021.12); B01F 25/50 (2021.12); B01F 25/52 (2021.12); B01F 35/2117 (2021.12); B01F 35/2133 (2021.12); B01F 35/2134 (2021.12); A61K 9/0019 (2012.12); A61M 2205/3393 (2012.12); B01F 21/30 (2021.12); B01F 23/511 (2021.12); B01F 23/56 (2021.12);
Abstract

The invention relates to a method for manufacturing a liquid acid concentrate for hemodialysis machines, with the following steps. In a preliminary step a water source (), an acid source (), an electrolyte tank () containing a mixture of electrolytes in exactly the quantity needed for the manufacture of the liquid acid concentrate, and a sodium chloride source () are connected to a mixing tank (). During Step a), the quantity of water needed for the manufacture of the batch of liquid acid concentrate is introduced into the mixing tank (). At Step b), the quantity of acid needed for manufacture the liquid acid concentrate is introduced into the mixing tank (), the solution is stirred until a homogeneous solution is obtained. Step c) is to repeat Sub-steps c1) and c2) until the electrolyte mixture contained in the electrolyte tank is completely dissolved. At Sub-step c1) part of the solution contained in the mixing tank () is transferred into the electrolyte tank () containing the electrolyte mixture, then at Sub-step c2) the solution contained in the electrolyte tank () is transferred into the mixing tank, leaving the still solid constituents in the electrolyte tank. At Step d) the quantity of sodium chloride needed to manufacture the liquid acid concentrate is introduced into the mixing tank (). Finally, at Step e), the solution is stirred and recirculated by taking it from the bottom the mixing tank () and reintroducing it at the top of the mixing tank until a homogeneous liquid acid concentrate is obtained. Steps a) to d) can be performed in any order, Step a) preceding always Step c).


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