US20130008852A1 - Urea sorbent - Google Patents

Urea sorbent Download PDF

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US20130008852A1
US20130008852A1 US13/541,107 US201213541107A US2013008852A1 US 20130008852 A1 US20130008852 A1 US 20130008852A1 US 201213541107 A US201213541107 A US 201213541107A US 2013008852 A1 US2013008852 A1 US 2013008852A1
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urea
polymer
dialysate
water
functional groups
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US13/541,107
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Moris S. Eisen
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Technion Research and Development Foundation Ltd
Fresenius Medical Care Holdings Inc
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Technion Research and Development Foundation Ltd
Fresenius Medical Care Holdings Inc
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Assigned to NATIONAL QUALITY CARE, INC., THE TECHNION RESEARCH AND DEVELOPMENT FOUNDATION, LTD. reassignment NATIONAL QUALITY CARE, INC. ASSIGNMENT OF ASSIGNORS INTEREST (SEE DOCUMENT FOR DETAILS). Assignors: EISEN, MORIS S.
Assigned to FRESENIUS MEDICAL CARE HOLDINGS, INC. reassignment FRESENIUS MEDICAL CARE HOLDINGS, INC. ASSIGNMENT OF ASSIGNORS INTEREST (SEE DOCUMENT FOR DETAILS). Assignors: FRESENIUS USA, INC.
Publication of US20130008852A1 publication Critical patent/US20130008852A1/en
Priority to US13/953,565 priority patent/US8672145B2/en
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    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08FMACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
    • C08F8/00Chemical modification by after-treatment
    • C08F8/14Esterification
    • AHUMAN NECESSITIES
    • A61MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61MDEVICES FOR INTRODUCING MEDIA INTO, OR ONTO, THE BODY; DEVICES FOR TRANSDUCING BODY MEDIA OR FOR TAKING MEDIA FROM THE BODY; DEVICES FOR PRODUCING OR ENDING SLEEP OR STUPOR
    • A61M1/00Suction or pumping devices for medical purposes; Devices for carrying-off, for treatment of, or for carrying-over, body-liquids; Drainage systems
    • A61M1/36Other treatment of blood in a by-pass of the natural circulatory system, e.g. temperature adaptation, irradiation ; Extra-corporeal blood circuits
    • A61M1/3679Other treatment of blood in a by-pass of the natural circulatory system, e.g. temperature adaptation, irradiation ; Extra-corporeal blood circuits by absorption
    • AHUMAN NECESSITIES
    • A61MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61MDEVICES FOR INTRODUCING MEDIA INTO, OR ONTO, THE BODY; DEVICES FOR TRANSDUCING BODY MEDIA OR FOR TAKING MEDIA FROM THE BODY; DEVICES FOR PRODUCING OR ENDING SLEEP OR STUPOR
    • A61M1/00Suction or pumping devices for medical purposes; Devices for carrying-off, for treatment of, or for carrying-over, body-liquids; Drainage systems
    • A61M1/14Dialysis systems; Artificial kidneys; Blood oxygenators ; Reciprocating systems for treatment of body fluids, e.g. single needle systems for hemofiltration or pheresis
    • A61M1/16Dialysis systems; Artificial kidneys; Blood oxygenators ; Reciprocating systems for treatment of body fluids, e.g. single needle systems for hemofiltration or pheresis with membranes
    • A61M1/1694Dialysis systems; Artificial kidneys; Blood oxygenators ; Reciprocating systems for treatment of body fluids, e.g. single needle systems for hemofiltration or pheresis with membranes with recirculating dialysing liquid
    • A61M1/1696Dialysis systems; Artificial kidneys; Blood oxygenators ; Reciprocating systems for treatment of body fluids, e.g. single needle systems for hemofiltration or pheresis with membranes with recirculating dialysing liquid with dialysate regeneration
    • AHUMAN NECESSITIES
    • A61MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61PSPECIFIC THERAPEUTIC ACTIVITY OF CHEMICAL COMPOUNDS OR MEDICINAL PREPARATIONS
    • A61P7/00Drugs for disorders of the blood or the extracellular fluid
    • A61P7/08Plasma substitutes; Perfusion solutions; Dialytics or haemodialytics; Drugs for electrolytic or acid-base disorders, e.g. hypovolemic shock
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J20/00Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
    • B01J20/02Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material
    • B01J20/20Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material comprising free carbon; comprising carbon obtained by carbonising processes
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J20/00Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
    • B01J20/22Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising organic material
    • B01J20/26Synthetic macromolecular compounds
    • B01J20/261Synthetic macromolecular compounds obtained by reactions only involving carbon to carbon unsaturated bonds
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J20/00Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
    • B01J20/22Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising organic material
    • B01J20/26Synthetic macromolecular compounds
    • B01J20/264Synthetic macromolecular compounds derived from different types of monomers, e.g. linear or branched copolymers, block copolymers, graft copolymers
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J20/00Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
    • B01J20/22Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising organic material
    • B01J20/26Synthetic macromolecular compounds
    • B01J20/265Synthetic macromolecular compounds modified or post-treated polymers
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J20/00Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
    • B01J20/28Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof characterised by their form or physical properties
    • B01J20/28014Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof characterised by their form or physical properties characterised by their form
    • B01J20/28052Several layers of identical or different sorbents stacked in a housing, e.g. in a column
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J41/00Anion exchange; Use of material as anion exchangers; Treatment of material for improving the anion exchange properties
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    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08FMACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
    • C08F216/00Copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by an alcohol, ether, aldehydo, ketonic, acetal or ketal radical
    • C08F216/02Copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by an alcohol, ether, aldehydo, ketonic, acetal or ketal radical by an alcohol radical
    • C08F216/04Acyclic compounds
    • C08F216/06Polyvinyl alcohol ; Vinyl alcohol
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08FMACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
    • C08F218/00Copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by an acyloxy radical of a saturated carboxylic acid, of carbonic acid or of a haloformic acid
    • C08F218/02Esters of monocarboxylic acids
    • C08F218/04Vinyl esters
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08FMACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
    • C08F218/00Copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by an acyloxy radical of a saturated carboxylic acid, of carbonic acid or of a haloformic acid
    • C08F218/02Esters of monocarboxylic acids
    • C08F218/04Vinyl esters
    • C08F218/10Vinyl esters of monocarboxylic acids containing three or more carbon atoms
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08FMACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
    • C08F8/00Chemical modification by after-treatment
    • C08F8/30Introducing nitrogen atoms or nitrogen-containing groups
    • C08F8/32Introducing nitrogen atoms or nitrogen-containing groups by reaction with amines
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D15/00Separating processes involving the treatment of liquids with solid sorbents; Apparatus therefor
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08FMACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
    • C08F220/00Copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and only one being terminated by only one carboxyl radical or a salt, anhydride ester, amide, imide or nitrile thereof
    • C08F220/02Monocarboxylic acids having less than ten carbon atoms; Derivatives thereof
    • C08F220/04Acids; Metal salts or ammonium salts thereof
    • C08F220/06Acrylic acid; Methacrylic acid; Metal salts or ammonium salts thereof
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    • C08FMACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
    • C08F2800/00Copolymer characterised by the proportions of the comonomers expressed
    • C08F2800/10Copolymer characterised by the proportions of the comonomers expressed as molar percentages
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08FMACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
    • C08F2810/00Chemical modification of a polymer
    • C08F2810/20Chemical modification of a polymer leading to a crosslinking, either explicitly or inherently

Definitions

  • the following disclosure relates to sorbent materials for separating and/or removing urea from dialysate solutions in sorbent-based dialysis treatment or for separating and/or removing urea from aqueous solutions or liquids in medical related processes or circumstances.
  • Hemodialysis is a process by which toxins and other molecules, such as urea, are removed from the blood using a semi-permeable filtering membrane.
  • a semi-permeable filtering membrane typically, the patient's blood and an aqueous solution (i.e., dialysate) are pumped in counter-direction flows in and about hollow, semi-permeable fibers.
  • FIG. 1 a known configuration of a dialyzer is shown.
  • blood flows in one end of the dialyzer and through hollow semi-porous or semipermeable fibers toward the blood output side of the dialyzer.
  • dialysate flows in an opposite direction, with respect to the blood flow, by entering a dialysate inlet and flowing around or about the semi-porous hollow fibers in which the blood is flowing.
  • the dialysate then exits the dialysate outlet.
  • the toxins within the blood are removed from the blood via a combination of diffusion, convection, and osmosis processes while the blood is flowing within the fibers and the dialysate is flowing outside the fibers.
  • the dialyzer is comprised of a large number of semi-permeable hollow fibers bundled together and placed in a cylindrical jacket as shown. Present day dialysis processes may be classified as: 1) single pass; and 2) sorbent-based.
  • Single pass processes require a continuous supply of gallons of fresh and treated water.
  • the treated water may be purified by for example, reverse osmosis or distillation.
  • the gallons of fresh and treated water are used to create the dialysis fluid, which is discarded after flowing through the dialyzer and collecting the toxins in a single pass through of the dialyzer.
  • FIG. 2 shows a schematic/diagram of a cross section of a single semi-permeable fiber that may be used in a dialyzer.
  • the blood flows through the hollow lumen within the semi-permeable walls of the fiber.
  • the membrane walls have a thickness, which is the difference of the radius R 2 minus the radius R 1 .
  • the membrane is semi-permeable and the dialysate, as shown, flows in the opposite direction outside of the semi-permeable fiber.
  • Sorbent dialysis differs from single pass dialysis in that the dialysate is regenerated using a series of chemical powders to remove toxins from the dialysate solution.
  • spent dialysate from the dialyzer is pumped through the first chemical layer of an enzyme called “urease”.
  • the urease catalyzes the breakdown of urea into ammonia and carbon dioxide.
  • the dialysate will then pass through a second chemical layer, a cation exchange layer (zirconium phosphate) which absorbs ammonia and other positively charged ions and then through a third, chemical layer, an anion exchange layer (hydrous zirconium oxide) where anions such as phosphate and fluoride are absorbed.
  • dialysate is pumped through a fourth layer of activated carbon where organic metabolites such as creatinine are absorbed.
  • the filtered dialysate may be passed through a degasser to remove air, carbon dioxide and other gas bubbles that may form or be found in the dialysate.
  • the capacity of the zirconium phosphate cation exchange layer to absorb ammonia is limited by the number of sites available to bind ammonia. If the zirconium phosphate layer is depleted, ammonia will remain in the dialysate as it is recycled to the dialyzer. In this case the patient may be at risk of ammonia toxicity. Consequently, the filtered dialysate must be periodically tested or monitored for ammonia concentration.
  • a typical dialysis patient generates an excess of about 24 to about 60 grams of urea per day that must be removed from the blood to avoid uremia. Therefore, what is needed is a sorbent for use in dialysis that has the capacity to remove this quantity of urea in a reasonable time frame. Thus, suitable sorbents should have the capacity to remove approximately 2.5 grams per deciliter of dialysate per hour (gm/dl/hr) from the dialysate.
  • a urea sorbent is provided that is suitable for use in a sorbent-based dialysis process.
  • the sorbent absorbs urea from the dialysate without generating ammonia or carbon dioxide, thereby eliminating the need for monitoring the concentration of ammonia in the dialysate as well as reducing or eliminating the need for de-gassing the dialysate.
  • the sorbent is insoluble or substantially insoluble in water and effective to remove urea from dialysate in a pH range of between 4 and 12 and more particularly in a pH range of between about 6 and 8.
  • the sorbent is soluble or substantially soluble and effective to bond with urea to remove, or bind urea from a dialysate solution or other aqueous solution.
  • a filter for regenerating dialysate includes a sorbent layer comprising a polymer having specific functional groups bonded thereto that interact or react with urea at a pH of between 4 and 12, and more particularly at a pH of between 6 and 8, to remove urea from an aqueous solution.
  • the exemplary polymer may be any one of soluble, substantially soluble, insoluble and substantially insoluble in water.
  • the exemplary polymer further reacts or interacts with urea while near room temperature or while in a defined temperature range between about 50° F. and 110° F. without releasing ammonia or generating carbon dioxide.
  • the reaction product of the polymer and urea may also be any one of soluble, substantially soluble, insoluble and substantially insoluble in water.
  • a second filter layer may be used with the exemplary polymer sorbent.
  • the second filter layer comprises activated carbon for absorbing organic metabolites from the dialysate or other aqueous solution.
  • the filter further includes an anion exchange layer for removing anions from the dialysate.
  • a filter for removing urea from an aqueous solution or liquid comprises a sorbent layer or coating.
  • the sorbent layer or coating comprises a polymer having specific functional groups bonded thereto.
  • the exemplary polymer having specific functional groups bonded thereto interacts or reacts with urea at a pH of between 4 and 12 or a predetermined bounded pH range therebetween (i.e., 3 to 7, 5-9, 6-8, etc.)
  • urea is bonded to the exemplary sorbent polymer and removed from an aqueous solution.
  • An exemplary polymer may be soluble, substantially soluble, insoluble, or substantially insoluble in water.
  • an exemplary polymer reacts with urea at near room temperature or other predetermined temperature range without releasing ammonia or generating carbon dioxide.
  • an exemplary polymer reacts or interacts with urea to produce a single reaction product.
  • the filter may also include activated carbon for adsorbing and removing other molecules from the aqueous solution.
  • the reaction product produced by the reaction or interaction of an exemplary polymer and urea may be soluble, substantially soluble, insoluble, or substantially insoluble in water.
  • FIG. 1 illustrates a diagram of a dialyzer
  • FIG. 2 illustrates a cross-sectional diagram of a fiber lumen in a dialyzer.
  • Glyoxylic acid monohydrate was dissolved in thionyl chloride and the mixture was refluxed for 48 h. Removal of excess thionyl chloride under vacuum gave a gum (glyoxaloyl chloride).
  • Polyvinyl alcohol co-ethylene was dissolved in dry DMF (by warming up to 100° C.) and this solution was added (after cooling to about 40° C.) to the previously obtained gum. The mixture was stirred for about 30 min in ice bath and NaH was added. Stirring continued for overnight after removal of the ice bath to obtain a sticky solid which was used for the urea trapping experiments from the dialysis solutions.
  • Polyvinyl alcohol co-ethylene was dissolved in DMF (15 ml) by heating the mixture to 100° C. This solution (after cooling to 40° C.) was added to a mixture of pyruvic acid, dicyclohexyl carbodiimide (DCC) and 4-dimethylaminopyridine (DMAP) in dry DMF (15 ml) and the reaction mixture was stirred at room temperature for overnight. The solid obtained was filtered off, washed with water, methanol, dichloromethane (DCM), acetone and ether respectively, dried and used for the urea trapping experiments from the dialysis solutions.
  • DCC dicyclohexyl carbodiimide
  • DMAP 4-dimethylaminopyridine
  • Polyvinyl alcohol co-ethylene was dissolved in DMF (15 ml) by heating the mixture to 100° C. This solution (after cooling to 40° C.) was added to a mixture of glyoxylic acid monohydrate, dicyclohexyl carbodiimide (DCC) and 4-dimethylaminopyridine (DMAP) in dry DMF (15 ml) and the reaction mixture was stirred at room temperature for overnight. The solid obtained was filtered off, washed with water, methanol, dichloromethane (DCM), acetone and ether respectively, dried and used for the urea trapping experiments from the dialysis solutions.
  • DCC dicyclohexyl carbodiimide
  • DMAP 4-dimethylaminopyridine
  • Poly(acrylic acid) was added to a stirred solution of EDC.HCl in distilled water. To this stirred suspension, iso-propylamine was added and the solution was stirred for overnight. The gel obtained was filtered under suction (vacuum pump), washed with water, methanol, dichloromethane (DCM), acetone and ether respectively and dried for one week at room temperature to obtain a thick gel (like a glassy solid), which was used for urea trapping experiments from the dialysis solutions.
  • DCM dichloromethane
  • Dialysate solutions were analyzed for nitrogen content and the amount of urea in the dialysate was calculated. In some cases, additional urea was added to the solution as indicated in column 2 of each Table (1-5). The polymer reagent was added to the solution in the amount indicated in column 3. The mixture was stirred at room temperature for one hour and filtered. The filtrate was analyzed and the amount of urea removed from the dialysate solution was determined. A minus sign ( ⁇ ) indicates that the results were inconclusive.
  • the title identifies the particular polymer reagent tested.
  • the first column of each table represents the experiment or run number.
  • the second column identifies the particular dialysate solution used for the experiment and whether additional urea was added to the solution.
  • the third column indicates the amount of polymer reagent used in the experiment.
  • the fifth column identifies the analyzed portion of the reaction mixture (e.g. filtrate). In some cases, a neutralizing agent was added to the filtrate.
  • the sixth column (BUN or Blood Urea Nitrogen) provides the concentration of nitrogen in the particular dialysate solution used for the experiment.
  • the seventh column gives the amount of urea in the solution.
  • the eighth column contains the maximum amount of urea in the solution. In the cases where additional urea was added as indicated in column 2, this number will be higher than the corresponding entry in the sixth column.
  • the ninth column is the amount of urea removed from the dialysate solution.
  • the first row of each table provides the nitrogen, urea and maximum or total amount of urea present in the dialysate solution used in the experiments.
  • vinyl polymers having specific functional groups selected from carboxylic acids, esters and salts, amides, dicarboxylic acids, and esters and salts may be formulated to provide sorbents suitable for use in removing urea from an aqueous solution having a pH from about 6 to 8.
  • Other sorbents suitable for removing urea from an aqueous solution having a pH range from 4 to 12 are realizable with various ones of the aforementioned specific functional groups by one of ordinary skill in the art having the information contained herein.
  • Such exemplary polymers are substantially insoluble in water and can remove urea from dialysate at a rate of at least 2.5 mg/di/hr. Additionally, such polymers may be soluble, substantially soluble or insoluble in water depending on variations in their manufacture.
  • vinyl polymers such as polyvinyl alcohol, polyvinyl alcohol-ethylene co-polymers and polyacrylic acid are reacted with specific functional groups selected from carboxylic acids, carboxylic acid esters, carboxylates, amides, dicarboxylic acids, dicarboxylic acid esters, and dicarboxylates to produce the desired exemplary sorbents.
  • Exemplary polymers may be applied to various substrates for use as dialysis sorbents. Such substrates may be organic or inorganic and may include filter paper, plastic or glass beads and other particulate materials that are insoluble in water. The polymers may also be applied to various screens and mesh-type filter materials formed from wire or plastic strands or cloth.
  • an exemplary urea sorbent is the use of selective functional groups that can be utilized to make a variety of resultant exemplary sorbents ranging from being soluble, insoluble, a liquid, a gum, an adhesive, a flexible material, a coating as well as a solid or powder.

Abstract

A sorbent polymer is provided that interacts or reacts with aqueous urea to aid the regeneration of a dialysate liquid. The sorbent polymer may include one or more specific functional groups bonded thereto. Such specific functional groups are selected from carboxylic acids, carboxylic acid esters, carboxylates, amides, dicarboxylic acids, dicarboxylic acid esters, and dicer boxylates to produce the desired urea sorbent.

Description

    CROSS-REFERENCE TO RELATED APPLICATIONS
  • This application is a divisional of U.S. application Ser. No. 12/479,513, filed Jun. 5, 2009, which claims priority from U.S. Provisional Patent Application No. 61/059,610, filed Jun. 6, 2008 and entitled UREA SORBENT. The entire teachings of the above applications are incorporated herein by reference.
  • TECHNICAL FIELD
  • The following disclosure relates to sorbent materials for separating and/or removing urea from dialysate solutions in sorbent-based dialysis treatment or for separating and/or removing urea from aqueous solutions or liquids in medical related processes or circumstances.
  • BACKGROUND
  • Hemodialysis is a process by which toxins and other molecules, such as urea, are removed from the blood using a semi-permeable filtering membrane. Typically, the patient's blood and an aqueous solution (i.e., dialysate) are pumped in counter-direction flows in and about hollow, semi-permeable fibers. In FIG. 1 a known configuration of a dialyzer is shown. Generally, blood flows in one end of the dialyzer and through hollow semi-porous or semipermeable fibers toward the blood output side of the dialyzer. Meanwhile, dialysate flows in an opposite direction, with respect to the blood flow, by entering a dialysate inlet and flowing around or about the semi-porous hollow fibers in which the blood is flowing. The dialysate then exits the dialysate outlet. The toxins within the blood are removed from the blood via a combination of diffusion, convection, and osmosis processes while the blood is flowing within the fibers and the dialysate is flowing outside the fibers. Generally, the dialyzer is comprised of a large number of semi-permeable hollow fibers bundled together and placed in a cylindrical jacket as shown. Present day dialysis processes may be classified as: 1) single pass; and 2) sorbent-based. Single pass processes require a continuous supply of gallons of fresh and treated water. The treated water may be purified by for example, reverse osmosis or distillation. The gallons of fresh and treated water are used to create the dialysis fluid, which is discarded after flowing through the dialyzer and collecting the toxins in a single pass through of the dialyzer.
  • FIG. 2 shows a schematic/diagram of a cross section of a single semi-permeable fiber that may be used in a dialyzer. The blood flows through the hollow lumen within the semi-permeable walls of the fiber. The membrane walls have a thickness, which is the difference of the radius R2 minus the radius R1. The membrane is semi-permeable and the dialysate, as shown, flows in the opposite direction outside of the semi-permeable fiber.
  • Sorbent dialysis differs from single pass dialysis in that the dialysate is regenerated using a series of chemical powders to remove toxins from the dialysate solution. Typically, spent dialysate from the dialyzer is pumped through the first chemical layer of an enzyme called “urease”. The urease catalyzes the breakdown of urea into ammonia and carbon dioxide. The dialysate will then pass through a second chemical layer, a cation exchange layer (zirconium phosphate) which absorbs ammonia and other positively charged ions and then through a third, chemical layer, an anion exchange layer (hydrous zirconium oxide) where anions such as phosphate and fluoride are absorbed. Finally, the dialysate is pumped through a fourth layer of activated carbon where organic metabolites such as creatinine are absorbed. At some point, the filtered dialysate may be passed through a degasser to remove air, carbon dioxide and other gas bubbles that may form or be found in the dialysate.
  • The capacity of the zirconium phosphate cation exchange layer to absorb ammonia is limited by the number of sites available to bind ammonia. If the zirconium phosphate layer is depleted, ammonia will remain in the dialysate as it is recycled to the dialyzer. In this case the patient may be at risk of ammonia toxicity. Consequently, the filtered dialysate must be periodically tested or monitored for ammonia concentration.
  • A typical dialysis patient generates an excess of about 24 to about 60 grams of urea per day that must be removed from the blood to avoid uremia. Therefore, what is needed is a sorbent for use in dialysis that has the capacity to remove this quantity of urea in a reasonable time frame. Thus, suitable sorbents should have the capacity to remove approximately 2.5 grams per deciliter of dialysate per hour (gm/dl/hr) from the dialysate.
  • SUMMARY
  • In one embodiment, a urea sorbent is provided that is suitable for use in a sorbent-based dialysis process. The sorbent absorbs urea from the dialysate without generating ammonia or carbon dioxide, thereby eliminating the need for monitoring the concentration of ammonia in the dialysate as well as reducing or eliminating the need for de-gassing the dialysate. In one variation, the sorbent is insoluble or substantially insoluble in water and effective to remove urea from dialysate in a pH range of between 4 and 12 and more particularly in a pH range of between about 6 and 8. In another embodiment the sorbent is soluble or substantially soluble and effective to bond with urea to remove, or bind urea from a dialysate solution or other aqueous solution.
  • In another aspect, a filter for regenerating dialysate includes a sorbent layer comprising a polymer having specific functional groups bonded thereto that interact or react with urea at a pH of between 4 and 12, and more particularly at a pH of between 6 and 8, to remove urea from an aqueous solution. The exemplary polymer may be any one of soluble, substantially soluble, insoluble and substantially insoluble in water. The exemplary polymer further reacts or interacts with urea while near room temperature or while in a defined temperature range between about 50° F. and 110° F. without releasing ammonia or generating carbon dioxide. The reaction product of the polymer and urea may also be any one of soluble, substantially soluble, insoluble and substantially insoluble in water. A second filter layer may be used with the exemplary polymer sorbent. The second filter layer comprises activated carbon for absorbing organic metabolites from the dialysate or other aqueous solution. In one variation, the filter further includes an anion exchange layer for removing anions from the dialysate.
  • In another aspect, a filter for removing urea from an aqueous solution or liquid is provided. The filter comprises a sorbent layer or coating. The sorbent layer or coating comprises a polymer having specific functional groups bonded thereto. The exemplary polymer having specific functional groups bonded thereto interacts or reacts with urea at a pH of between 4 and 12 or a predetermined bounded pH range therebetween (i.e., 3 to 7, 5-9, 6-8, etc.) Upon interaction or perhaps a reaction with urea, urea is bonded to the exemplary sorbent polymer and removed from an aqueous solution. An exemplary polymer may be soluble, substantially soluble, insoluble, or substantially insoluble in water. Furthermore, an exemplary polymer reacts with urea at near room temperature or other predetermined temperature range without releasing ammonia or generating carbon dioxide. In various aspects, an exemplary polymer reacts or interacts with urea to produce a single reaction product. The filter may also include activated carbon for adsorbing and removing other molecules from the aqueous solution. The reaction product produced by the reaction or interaction of an exemplary polymer and urea may be soluble, substantially soluble, insoluble, or substantially insoluble in water.
  • BRIEF DESCRIPTION OF THE DRAWINGS
  • For a more complete understanding, reference is now made to the following description taken in conjunction with the accompanying Drawings in which:
  • FIG. 1 illustrates a diagram of a dialyzer; and
  • FIG. 2 illustrates a cross-sectional diagram of a fiber lumen in a dialyzer.
  • DETAILED DESCRIPTION
  • Referring now to the drawings, the various views and embodiments of exemplary urea sorbents are illustrated and described, and other possible embodiments are described. The figures are not necessarily drawn to scale, and in some instances the drawings have been exaggerated and/or simplified in places for illustrative purposes only. One of ordinary skill in the art will appreciate the many possible applications and variations based on the following examples of possible embodiments.
  • Sorbent Preparation:
  • 1. Preparation of MPS-IV-048 (Polyvinylglyoxalate)
  • Figure US20130008852A1-20130110-C00001
  • 1.1 Reagents
  • Entry Reagent/solvent Amount mmol Equivalent
    1 Polyvinyl alcohol 1.000 g 5.0 × 10−3 1
    (M. wt. = 205000) (23.3 mmol of
    alcohol units)
    2 Glyoxylic acid 2.144 g 23.30 1
    monohydrate
    (M. wt. = 92)
    3 EDC.HC1 (M. wt. = 3.973 g 20.72 0.88
    191.71)
    4 Distilled water 15 ml
  • 1.2 Procedure.
  • To a stirred solution of glyoxylic acid monohydrate and EDC.HCl in distilled water, polyvinyl alcohol was added stirred the solution for 24 h. Water was evaporated under reduced pressure to obtain a gum, which was used for urea trapping experiments from the dialysis solutions.
  • 2. Preparation of MPS-IV-054 (Polyvinylglyoxalate)
  • Figure US20130008852A1-20130110-C00002
  • 2.1 Reagents
  • Entry Reagent/solvent Amount mmol Equivalent
    1 Polyvinyl alcohol 1.000 g 5.0 × 10−3 1
    (M. wt. = 205000) (23.3 mmol of
    alcohol units)
    2 Glyoxylic acid 2.144 g 23.30 1
    monohydrate
    (M. wt. = 92)
    3 NaH (M. wt. = 1.538 g 0.846 1.51
    24 55-60%
    in suspension)
    4 Dry- N,N- 10 ml
    Dimethylformamide
    (DMF)
  • 2.2 Procedure
  • Sodium hydride was added to a cooled (0° C., ice bath) stirred suspension of polyvinyl alcohol in dry DMF and stirring continued for 2-3 min. Glyoxylic acid monohydrate was added to this mixture and the mixture was brought to room temperature after 2 h stirring at 0° C. Stirring continued for overnight. The solid obtained was washed with DCM and used for urea trapping experiments from the dialysis solutions.
  • 2.3 Properties
  • Weight of MPS-IV-054=3.691 g
  • Melting Point of MPS-IV-054=doesn't melt up to 290 0° C.
    Mn=75540; Mw=79736; ρ=1.055 g/cm3
  • 3. Preparation of MPS-V-003 (Bis(Polyvinyloxalate))
  • Figure US20130008852A1-20130110-C00003
  • 3.1 Reagents
  • Entry Reagent/solvent Amount mmol Equivalent
    1 Polyvinyl alcohol 1.000 g 5.0 × 10−3 1
    (M. wt. = 205000) (23.3 mmol of
    alcohol units)
    2 Oxalic acid (M. wt. =78) 2.000 g 25.64 1.1
    3 EDC.HC1 (M. wt. = 3.973 g 20.72 0.88
    191.71)
    4 Distilled water 20 ml
  • 3.2 Procedure
  • To a stirred solution of oxalic acid and EDC.HCl in distilled water, polyvinyl alcohol was added stirred the solution for 24 h. Water was evaporated under reduced pressure to obtain a gum, which was used for urea trapping experiments from the dialysis solutions.
  • 3.3 Properties
  • Weight of MPS-V-003=6.20 g
  • 4. Preparation of MPS-V-004 (Polyvinylpyruvate)
  • Figure US20130008852A1-20130110-C00004
  • 4.1 Reagents
  • Reagent/
    Entry solvent Amount mmol Equivalent
    1 Polyvinyl 1.000 g 5.0 × 10−3 1
    alcohol (M. (23.3 mmol of
    wt. = 205000) alcohol units)
    2 Pyruvic acid 2.10 ml(≡2.226 g) 25.28 1.1
    (M. wt. =
    88.06; d =
    1.06)
    3 EDC.HC1 (M. 3.92 g 20.44 0.88
    wt. = 191.71)
    4 Distilled water 15 ml
  • 4.2 Procedure
  • To a stirred solution of pyruvic acid and EDC.HCl in distilled water, polyvinyl alcohol was added stirred the solution for 24 h. Water was evaporated under reduced pressure to obtain a gum, which was used for urea trapping experiments from the dialysis solutions.
  • 4.3 Properties
  • Weight of MPS-V-004=6.42 g
  • 5. Preparation of MPS-V-005 (Polyvinylbezoate 0.33 Polyvinylalcohol 0.66)
  • Figure US20130008852A1-20130110-C00005
  • 5.1 Reagents
  • Entry Reagent/solvent Amount mmol Equivalent
    1 2.000 g 1.0 × 10−2 (46.6 1 × 10−2 (46.6 1
    Polyvinyl mmol of alcohol mmole of alcohol
    alcohol (M. wt. = units) units)
    205000)
    2 Benzoyl chloride 2.00 ml(≡2.422 g) 17.23 0.37
    (M. wt. = 130.57;
    d = 1.211)
    3 Dry pyridine 25 ml
  • 5.2 Procedure
  • To a stirred, cooled (0° C., ice bath) solution of polyvinyl alcohol in dry pyridine (17 ml), a solution of benzoyl chloride in dry pyridine (8 ml) was added dropwise over a period of 10 min and stirring continued for 24 h with gradual increase in reaction temperature to rt. After 24 h, the pyridine was removed under reduced pressure and by co-evaporation with toluene to obtain a gum which was used for next step. The gum (MPS-V-005) swelled when brought in contact with solvents like ethyl acetate, dichloromethane (DCM), chloroform and methanol.
  • 6. Preparation of MPS-Iv-009 (Polyvinylbezoate 0.33 Polyvinylglyoxalate 0.66)
  • Figure US20130008852A1-20130110-C00006
  • 6.1 Reagents
  • Entry Reagent/solvent Amount mmol Equivalent
    1 MPS-V-005 2.000 g (29.3 mmol of 1
    alcohol units)
    2 Glyoxylic acid 0.920 g 10.00 0.34
    monohydrate (M.
    wt. = 92)
    3 EDC.HC1 (M. wt. = 1.55 g 10.00 0.34
    191.71)
    4 Distilled water 20 ml
  • 6.2 Procedure
  • A solution of glyoxylic acid monohydrate and EDC.HCl in distilled water was added to MPS-V-005 and the suspension was stirred at room temperature for 48 h. The white ppt obtained was filtered off, dried and used for urea trapping experiments from the dialysis solutions.
  • 6.3 Properties
  • Weight of MPS-V-009=1.543 g
  • 7. Preparation of MPS-V-027 (Polyvinylglyoxalate-Ethylene Copolymer)
  • Figure US20130008852A1-20130110-C00007
  • 7.1 Reagents
  • Entry Reagent/solvent Amount mmol Equivalent
    1 Polyvinyl alcohol- 2.28 g (≡1.838 g of 41.67 1
    coethylene (27% polyvinyl alcohol) mmol of
    ethylene) OH group
    2 Glyoxalic acid 4.00 g 43.48 1.04
    monohydrate
    (M. wt. = 92)
    3 NaH (M. wt. = 1.200 g 50.00 1.2
    24 55-60%
    in suspension)
    4 Thionyl chloride 12 (≡19.572 g) 164.51 3.78
    (M. wt. = 118.97,
    d = 1.613)
    5 Dry- N,N - 30 ml
    Dimethylformamide
    (DMF)
  • 7.2 Procedure
  • Glyoxylic acid monohydrate was dissolved in thionyl chloride and the mixture was refluxed for 48 h. Removal of excess thionyl chloride under vacuum gave a gum (glyoxaloyl chloride). Polyvinyl alcohol co-ethylene was dissolved in dry DMF (by warming up to 100° C.) and this solution was added (after cooling to about 40° C.) to the previously obtained gum. The mixture was stirred for about 30 min in ice bath and NaH was added. Stirring continued for overnight after removal of the ice bath to obtain a sticky solid which was used for the urea trapping experiments from the dialysis solutions.
  • 7.3 Properties
  • Weight of MPS-V-027=4.763 g
  • 8. Preparation of MPS-V-036 (Polyacrylicacid0.9Polyvinylpolyacrylicacid0.1)
  • Figure US20130008852A1-20130110-C00008
  • 8.1 Reagents
  • Entry Reagent/solvent Amount mmol Equivalent
    1 Poly(acrylic acid) 1.500 g 3.75 × 10−4 1
    (M. wt. = 4000000) (20.83 mmol of
    —COOH units)
    2 Polyvinyl alcohol 1.000 g 4.88 × 10−4 0.1
    (M. wt. = 205000) (2.27 mmol of
    —OH units)
    3 EDC.HC1 0.479 g 2.49 1.1 eq of —OH
    (M. wt. = 191.71) groups
    4 Distilled water 50 ml
  • 8.2 Procedure
  • Poly (acrylic acid) was added to a stirred solution of EDC.HCl in distilled water. To this stirred suspension, polyvinyl alcohol was added and the solution was stirred for overnight. The gel obtained was filtered under suction (vacuum pump), washed with water, methanol, dichloromethane (DCM), acetone and ether respectively and dried for one week at room temperature to obtain a glassy solid, which was used for urea trapping experiments from the dialysis solutions.
  • 8.3 Properties
  • Weight of MPS-V-036=3.361 g
  • 9. Preparation of MPS-V-037 (Polyvinylpyrurate-Ethylene Copolymer)
  • Figure US20130008852A1-20130110-C00009
  • 9.1 Reagents
  • Entry Reagent/solvent Amount mmol Equivalent
    1 Polyvinyl alcohol - 1.14 g (≡0.909 g of 20.84 1
    coethylene (27% polyvinyl alcohol) mmol of
    ethylene) OH group
    2 Pyruvic acid (M. 1.90 ml (≡2.394 g) 27.19 1.3
    wt. = 88.06,
    d = 1.26)
    3 DCC (M. wt. 6.450 g 31.26 1.5
    206.33)
    4 DMAP (M. wt. = 0.382 g 3.13 0.15
    122.17)
    5 Dry- N,N - 30 ml
    Dimethylformamide
    (DMF)
  • 9.2 Procedure
  • Polyvinyl alcohol co-ethylene was dissolved in DMF (15 ml) by heating the mixture to 100° C. This solution (after cooling to 40° C.) was added to a mixture of pyruvic acid, dicyclohexyl carbodiimide (DCC) and 4-dimethylaminopyridine (DMAP) in dry DMF (15 ml) and the reaction mixture was stirred at room temperature for overnight. The solid obtained was filtered off, washed with water, methanol, dichloromethane (DCM), acetone and ether respectively, dried and used for the urea trapping experiments from the dialysis solutions.
  • 9.3 Properties
  • Weight of MPS-V-037=6.305 g
  • 10. Preparation of MPS-V-038 (Polyvinylglyoxalate-Ethylene Copolymer)
  • Figure US20130008852A1-20130110-C00010
  • 10.1 Reagents
  • Entry Reagent/solvent Amount mmol Equivalent
    1 Polyvinyl alcohol- 1.14 g (≡0.909 g of 20.84 1
    coethylene (27% polyvinyl alcohol) mmol of
    ethylene) OH group
    2 Glyoxylic acid 2.400 g 26.09 1.25
    monohydrate (M.
    wt. = 92)
    3 DCC (M. wt. = 6.450 g 31.26 1.5
    206.33)
    4 DMAP (M. wt. = 0.382 g 3.13 0.15
    122.17)
    5 Dry- N,N - 30 ml
    Dimethylformamide
    (DMF)
  • 10.2 Procedure
  • Polyvinyl alcohol co-ethylene was dissolved in DMF (15 ml) by heating the mixture to 100° C. This solution (after cooling to 40° C.) was added to a mixture of glyoxylic acid monohydrate, dicyclohexyl carbodiimide (DCC) and 4-dimethylaminopyridine (DMAP) in dry DMF (15 ml) and the reaction mixture was stirred at room temperature for overnight. The solid obtained was filtered off, washed with water, methanol, dichloromethane (DCM), acetone and ether respectively, dried and used for the urea trapping experiments from the dialysis solutions.
  • 10.3 Properties
  • Weight of MPS-V-038=6.025 g
  • 11. Preparation of MPS-V-047 (Isopropylaminepolyacrylicamide)
  • Figure US20130008852A1-20130110-C00011
  • 11.1 Reagents
  • Entry Reagent/solvent Amount mmol Equivalent
    1 Poly(acrylic acid) 1.500 g 3.75 × 10−4 1
    (M. wt. = (20.83 mmol of
    4000000) —COOH units)
    2 iso-Propylamine 0.20 ml 2.33 0.11
    (M. wt. = 59.11, (≡0.138 g)
    d = 0.688)
    3 EDC.HC1 (M. 0.479 g 2.49 1.1 eq of
    wt. = 191.71) —OH
    groups
    4 Distilled water 50 ml
  • 11.2 Procedure
  • Poly(acrylic acid) was added to a stirred solution of EDC.HCl in distilled water. To this stirred suspension, iso-propylamine was added and the solution was stirred for overnight. The gel obtained was filtered under suction (vacuum pump), washed with water, methanol, dichloromethane (DCM), acetone and ether respectively and dried for one week at room temperature to obtain a thick gel (like a glassy solid), which was used for urea trapping experiments from the dialysis solutions.
  • 11.3 Properties
  • Weight of MPS-V-047=2.46 g
  • Dialysate solutions were analyzed for nitrogen content and the amount of urea in the dialysate was calculated. In some cases, additional urea was added to the solution as indicated in column 2 of each Table (1-5). The polymer reagent was added to the solution in the amount indicated in column 3. The mixture was stirred at room temperature for one hour and filtered. The filtrate was analyzed and the amount of urea removed from the dialysate solution was determined. A minus sign (−) indicates that the results were inconclusive.
  • In the following tables, the title identifies the particular polymer reagent tested. The first column of each table represents the experiment or run number. The second column identifies the particular dialysate solution used for the experiment and whether additional urea was added to the solution. The third column indicates the amount of polymer reagent used in the experiment. The fourth column gives the reaction conditions e.g. time and temperature. (Note: rt=room temperature). It is further understood that room temperature is between about 60 and 78° F. (about 15.56° C. to about 25.56° C.) and that reactions will also occur in a temperature range of between about 50° F. to about 110° F. (about 10° C. to about 43.3° C.). It is believed that reactions will also occur at colder or warmer temperatures, but such reactions have not been specifically tested. The fifth column identifies the analyzed portion of the reaction mixture (e.g. filtrate). In some cases, a neutralizing agent was added to the filtrate. The sixth column (BUN or Blood Urea Nitrogen) provides the concentration of nitrogen in the particular dialysate solution used for the experiment. The seventh column gives the amount of urea in the solution. The eighth column contains the maximum amount of urea in the solution. In the cases where additional urea was added as indicated in column 2, this number will be higher than the corresponding entry in the sixth column. The ninth column is the amount of urea removed from the dialysate solution. The first row of each table provides the nitrogen, urea and maximum or total amount of urea present in the dialysate solution used in the experiments.
  • TABLE 1
    MPS-IV-048
    Results (in mg/dL)
    Analyzed Blood Blood Maximum Amount
    Amount of portion of Urea Urea amount of of urea
    Soln Reagent Reaction reaction Nitrogen (BUN × urea taken out
    Entry compn Used (g) condn. mixture (BUN) 2.14) present (mg/dL/h)
    1 Soln-3 7.8 16.692 16.692
    Blank
    (10 ml)
    2 Soln-3 2 rt, 1 h Filtrate 14.6 31.244 16.692 (−) 14.552
    (10 ml) (8 mL)
    3 Soln-3 13 (0.50 g) rt, 1 h Filtrate 797.2 1706.0 2516.7 810.7
    (20 ml) + (10 mL)
    Urea
    (0.50 g)
  • TABLE 2
    MPS-IV-OS4 and MPS-V-009
    Results (in mg/dL)
    Analyzed Blood Blood Maximum Amount
    Amount of portion of Urea Urea amount of of urea
    Soln Reagent Reaction reaction Nitrogen (BUN × urea taken out
    Entry compn Used (g) condn. mixture (BUN) 2.14) present (mg/dL/h)
    1 Soln-3 4 8.56 8.56
    Blank
    (10 ml)
    MPS-IV-054
    2 Soln-3 2.5 rt, 1 h Filtrate 2227 4765.78 5008.56 242.78
    (20 ml) + (5 ml;
    Urea pH = 10)
    (0.50 g)
    3 Soln-3 2.50 rt, 1 h Filtrate 2523 5399.22 5008.56 (−) 390.66 
    (10 ml) + (3 ml;
    Urea pH = 10) +
    (1.00 g) 2% HCI—
    (0.4 ml)
    to
    neutralize
    to pH = 7
    MPS-V-009
    4 Soln-3 1.26 rt, 1 h Filtrate 2563 5484.82 2508.56 (−) 2976.26
    (10 ml) + (3 ml;
    Urea pH = 7)
    (0.50 g)
  • TABLE 3
    MPS-V-003
    Results (in mg/dL)
    Analyzed Blood Blood Maximum Amount
    Amount of portion of Urea Urea amount of of urea
    Soln Reagent Reaction reaction Nitrogen (BUN × urea taken out
    Entry compn Used (g) condn. mixture (BUN) 2.14) present (mg/dL/h)
    1 Soln-3 4 8.56 8.56
    (10 ml)
    Blank
    2 Soln-3 rt, 1 h Filtrate 2257 4740 5008 268.3
    (20 ml) + (5 mL;
    Urea pH = 1)
    (1.00 g)
    3 Soln-3 rt, 1 h Filtrate 1527 3267.78 5008 1740.22
    (20 ml) + (3 m;
    Urea pH = 1) +
    (1.00 g) saturated
    HCO3
    (1 ml) to
    neutralize
    to pH = 7
  • TABLE 4
    MPS-V-027 and MPS-V-036
    Results (in mg/dL)
    Analyzed Blood Blood Maximum Amount
    Amount of portion of Urea Urea amount of of urea
    Soln Reagent Reaction reaction Nitrogen (BUN × urea taken out
    Entry compn Used (g) condn. mixture (BUN) 2.14) present (mg/dL/h)
    1 Soln-4 88 188.32 188.32
    Blank
    (9 ml)
    2 Soln-4 MPS-V rt, 1 h Filtrate 0 0 2688.32 2688.32
    (10 ml) + 036 (2 ml)
    Urea (residue (pH = 6~7)
    (0.50 g) after
    filtration)
    (2.28 g)
    3 Soln-4 MPS-V rt, 1 h Filtrate 1114 2339.4 2688.32 349.3
    (10 ml) + 027 (4 ml)
    Urea (residue (pH = 7~8)
    (0.50 g) after
    filtration
    and
    washing
    with
    MeOH)
    (4.40 g)
  • TABLE 5
    MPS-V-037, MPS-V-038 and MPS-V-047
    Data for Solution -4
    Results (in mg/dL)
    Analyzed Blood Blood Maximum Amount
    Amount portion of Urea Urea amount of of urea
    Soln of Reagent Reaction reaction Nitrogen (BUN × urea taken out
    Entry compn Used (g) condn. mixture (BUN) 2.14) present (mg/dL/h)
    1 Soln-4 25 53..5 53..5
    Blank
    (9 ml)
    2 Soln-4 2 rt, 1 h Filtrate 0 0 5053.5 5053.5
    (20 ml) + (10 ml)
    Urea (pH-7)
    (1.00 g)
    3 Soln-4 13 (0.50 g) rt, 1 h Filtrate 0 0 2553.5 2553.5
    (10 ml) + (10 ml)
    Urea (pH-7)
    (0.50 g)
    4 Soln-4 MPS-V047 rt, 1 h Filtrate 479 1025.06 2553.5 1528.44
    (10 ml) + (2.46 g) (5 ml)
    Urea (pH = 5)
    (0.50 g)
  • As will be appreciated from the foregoing, vinyl polymers having specific functional groups selected from carboxylic acids, esters and salts, amides, dicarboxylic acids, and esters and salts may be formulated to provide sorbents suitable for use in removing urea from an aqueous solution having a pH from about 6 to 8. Other sorbents suitable for removing urea from an aqueous solution having a pH range from 4 to 12 are realizable with various ones of the aforementioned specific functional groups by one of ordinary skill in the art having the information contained herein. Such exemplary polymers are substantially insoluble in water and can remove urea from dialysate at a rate of at least 2.5 mg/di/hr. Additionally, such polymers may be soluble, substantially soluble or insoluble in water depending on variations in their manufacture.
  • In some variations of the invention, vinyl polymers such as polyvinyl alcohol, polyvinyl alcohol-ethylene co-polymers and polyacrylic acid are reacted with specific functional groups selected from carboxylic acids, carboxylic acid esters, carboxylates, amides, dicarboxylic acids, dicarboxylic acid esters, and dicarboxylates to produce the desired exemplary sorbents. Exemplary polymers may be applied to various substrates for use as dialysis sorbents. Such substrates may be organic or inorganic and may include filter paper, plastic or glass beads and other particulate materials that are insoluble in water. The polymers may also be applied to various screens and mesh-type filter materials formed from wire or plastic strands or cloth.
  • Another advantage of an exemplary urea sorbent is the use of selective functional groups that can be utilized to make a variety of resultant exemplary sorbents ranging from being soluble, insoluble, a liquid, a gum, an adhesive, a flexible material, a coating as well as a solid or powder.
  • It will be appreciated by those skilled in the art having the benefit of this disclosure that this urea sorbent provides a viable replacement for prior known dialysis sorbent materials. It should be understood that the drawings and detailed description herein are to be regarded in an illustrative rather than a restrictive manner, and are not intended to be limiting to the particular forms and examples disclosed. On the contrary, included are any further modifications, changes, rearrangements, substitutions, alternatives, design choices, and embodiments apparent to those of ordinary skill in the art, without departing from the spirit and scope hereof, as defined by the following claims. Thus, it is intended that the following claims be interpreted to embrace all such further modifications, changes, rearrangements, substitutions, alternatives, design choices, and embodiments.

Claims (17)

1. A polymer suitable for use as a sorbent for regenerating dialysate, the polymer including specific functional groups bonded thereto that interact with urea in a liquid at a pH of between 6 and 8 to remove urea from an aqueous solution, wherein the polymer is substantially insoluble in water and reacts with urea without releasing ammonia, wherein the reaction product of the polymer and urea is substantially insoluble in water, and wherein the polymer is selected from the group consisting of polymers having repeating units having the formula
Figure US20130008852A1-20130110-C00012
2. The polymer of claim 1, wherein the functional group includes at least two adjacent carbonyl groups.
3. The polymer of claim 1, wherein the functional group comprises one of a dicarboxlic acid, a dicarboxlic acid ester, or a dicarboxalate.
4. The polymer of claim 1, wherein the functional group comprises one of an oxalate, a pyruvate, a benzoate or an acrylic acid.
5. A filter for regenerating dialysate comprising:
a sorbent layer comprising a polymer having specific functional groups bonded thereto that interact with urea at a pH of between 5 and 10 to remove urea from an aqueous solution, wherein the polymer is substantially insoluble in water and interacts with urea in a predetermined temperature range and without releasing ammonia and wherein the reaction product of the polymer and urea is substantially insoluble in water; and
activated carbon for absorbing organic metabolites from the dialysate.
6. The filter of claim 5, further comprising an anion exchange layer for removing anions from the dialysate.
7. A polymer suitable for use as a sorbent for regenerating dialysate, the polymer including specific functional groups bonded thereto that react with urea at a pH of between 4 to 12 to remove urea from an aqueous solution, wherein the polymer is either soluble or substantially insoluble in water and interacts or reacts with urea in a temperature range of about 50° F. to 110° F. without releasing ammonia, wherein the reaction product of the polymer and urea is soluble or substantially insoluble in water, and wherein the polymer is selected from the group consisting of polymers having repeating units having the formula
Figure US20130008852A1-20130110-C00013
8. The polymer of claim 7, wherein the functional group includes at least one carbonyl group (C═O) either as a ketone, anhydride, ester, amido, or a combination of functional groups from two to 10 either adjacent or apart.
9. The polymer of claim 7, wherein the functional group comprises one of a dicarboxylic acid, a dicarboxylic acid ester, a general dicarboxylate moiety or a combination of said functional groups.
10. The polymer of claim 7, wherein the functional group comprises one of an oxalate, a pyruvate, a benzoate or an acrylic acid.
11. The polymer of claim 7, wherein the functional groups react with urea at a pH of between 6 and 9.
12. The polymer of claim 7, wherein the reaction product of the polymer and urea is insoluble in water.
13. A dialysate regenerating filter for removing solids or liquids from dialysate comprising:
a sorbent layer comprising a polymer having functional groups bonded thereto that interact or react with urea at a pH of between 4 to 12 and bind urea from an aqueous solution, wherein the polymer is either soluble or substantially insoluble in water and interacts or reacts with urea without releasing ammonia and wherein the interaction or reaction product of the polymer and urea is either soluble or substantially insoluble in water; and
activated carbon for absorbing organic metabolites from the dialysate.
14. The filter of claim 13, further comprising an anion exchange layer for removing anions from the dialysate.
15. The filter of claim 13, wherein the functional groups interact or react with urea at a pH of between 6 and 9.
16. The filter of claim 13, wherein the polymer is insoluble in water.
17. The filter of claim 13, wherein the interaction or reaction product of the polymer and urea is insoluble in water.
US13/541,107 2008-06-06 2012-07-03 Urea sorbent Abandoned US20130008852A1 (en)

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Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2014151322A1 (en) 2013-03-14 2014-09-25 Fresenius Medical Care Holdings, Inc. Universal portable machine for online hemodiafiltration using regenerated dialysate
US9433720B2 (en) 2013-03-14 2016-09-06 Fresenius Medical Care Holdings, Inc. Universal portable artificial kidney for hemodialysis and peritoneal dialysis

Families Citing this family (59)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20060217771A1 (en) 2005-02-07 2006-09-28 Medtronic, Inc. Potassium monitoring
US8220643B2 (en) 2008-06-06 2012-07-17 Fresenius Medical Care Holdings, Inc. Urea sorbent
US9399091B2 (en) 2009-09-30 2016-07-26 Medtronic, Inc. System and method to regulate ultrafiltration
US9750862B2 (en) 2011-04-29 2017-09-05 Medtronic, Inc. Adaptive system for blood fluid removal
US9456755B2 (en) 2011-04-29 2016-10-04 Medtronic, Inc. Method and device to monitor patients with kidney disease
US9848778B2 (en) 2011-04-29 2017-12-26 Medtronic, Inc. Method and device to monitor patients with kidney disease
EP2739325B1 (en) 2011-08-02 2017-10-04 Medtronic, Inc. Hemodialysis system having a flow path with a controlled compliant volume
US10857277B2 (en) 2011-08-16 2020-12-08 Medtronic, Inc. Modular hemodialysis system
WO2013103906A1 (en) 2012-01-04 2013-07-11 Medtronic, Inc. Multi-staged filtration system for blood fluid removal
US10905816B2 (en) 2012-12-10 2021-02-02 Medtronic, Inc. Sodium management system for hemodialysis
US11565029B2 (en) 2013-01-09 2023-01-31 Medtronic, Inc. Sorbent cartridge with electrodes
US9707328B2 (en) 2013-01-09 2017-07-18 Medtronic, Inc. Sorbent cartridge to measure solute concentrations
US9713666B2 (en) 2013-01-09 2017-07-25 Medtronic, Inc. Recirculating dialysate fluid circuit for blood measurement
US11154648B2 (en) 2013-01-09 2021-10-26 Medtronic, Inc. Fluid circuits for sorbent cartridge with sensors
US10850016B2 (en) 2013-02-01 2020-12-01 Medtronic, Inc. Modular fluid therapy system having jumpered flow paths and systems and methods for cleaning and disinfection
US9623164B2 (en) 2013-02-01 2017-04-18 Medtronic, Inc. Systems and methods for multifunctional volumetric fluid control
US9526822B2 (en) 2013-02-01 2016-12-27 Medtronic, Inc. Sodium and buffer source cartridges for use in a modular controlled compliant flow path
US10543052B2 (en) 2013-02-01 2020-01-28 Medtronic, Inc. Portable dialysis cabinet
US10010663B2 (en) 2013-02-01 2018-07-03 Medtronic, Inc. Fluid circuit for delivery of renal replacement therapies
US9827361B2 (en) 2013-02-02 2017-11-28 Medtronic, Inc. pH buffer measurement system for hemodialysis systems
US9144640B2 (en) 2013-02-02 2015-09-29 Medtronic, Inc. Sorbent cartridge configurations for improved dialysate regeneration
EP3102107A4 (en) 2013-11-04 2018-02-07 Medtronic, Inc. Method and device to manage fluid volumes in the body
US9895477B2 (en) 2013-11-26 2018-02-20 Medtronic, Inc. Detachable module for recharging sorbent materials with optional bypass
US10052612B2 (en) 2013-11-26 2018-08-21 Medtronic, Inc. Zirconium phosphate recharging method and apparatus
US10004839B2 (en) 2013-11-26 2018-06-26 Medtronic, Inc. Multi-use sorbent cartridge
US10537875B2 (en) 2013-11-26 2020-01-21 Medtronic, Inc. Precision recharging of sorbent materials using patient and session data
US9943780B2 (en) 2013-11-26 2018-04-17 Medtronic, Inc. Module for in-line recharging of sorbent materials with optional bypass
US9884145B2 (en) 2013-11-26 2018-02-06 Medtronic, Inc. Parallel modules for in-line recharging of sorbents using alternate duty cycles
US10595775B2 (en) 2013-11-27 2020-03-24 Medtronic, Inc. Precision dialysis monitoring and synchronization system
KR102033277B1 (en) 2014-05-29 2019-11-08 프레제니우스 메디칼 케어 홀딩스 인코퍼레이티드 Method for treating dialysate, dialysis system, and method for pre-evaluating dialysis patients for treatment with same
EP3160529B1 (en) 2014-06-24 2019-11-13 Medtronic Inc. Replenishing urease in dialysis systems using urease pouches
WO2015199761A1 (en) * 2014-06-24 2015-12-30 Medtronic, Inc. Sorbent pouch
WO2015199760A1 (en) 2014-06-24 2015-12-30 Medtronic, Inc. Replenisihing urease in dialysis systems using a urease introducer
EP3160534A4 (en) 2014-06-24 2018-03-07 Medtronic Inc. Stacked sorbent assembly
EP3160536A4 (en) 2014-06-24 2018-03-07 Medtronic Inc. Reserve zirconium phosphate module for use in sorbent dialysis
CN106604752B (en) 2014-06-24 2019-07-09 美敦力公司 Urase for supplementing the urase in adsorbent box introduces system
US10172991B2 (en) 2014-06-24 2019-01-08 Medtronic, Inc. Modular dialysate regeneration assembly
US10098993B2 (en) 2014-12-10 2018-10-16 Medtronic, Inc. Sensing and storage system for fluid balance
US9895479B2 (en) 2014-12-10 2018-02-20 Medtronic, Inc. Water management system for use in dialysis
US10874787B2 (en) 2014-12-10 2020-12-29 Medtronic, Inc. Degassing system for dialysis
US9713665B2 (en) 2014-12-10 2017-07-25 Medtronic, Inc. Degassing system for dialysis
CN105214624B (en) * 2015-11-02 2017-08-04 李建中 A kind of dialyzate adsorption stuffing, its preparation method and application
WO2017078965A1 (en) 2015-11-06 2017-05-11 Medtronic, Inc Dialysis prescription optimization for decreased arrhythmias
US10391473B1 (en) * 2016-02-20 2019-08-27 Electric Power Research Institute, Inc. Polymer-protected sorbent
US10874790B2 (en) 2016-08-10 2020-12-29 Medtronic, Inc. Peritoneal dialysis intracycle osmotic agent adjustment
US10994064B2 (en) 2016-08-10 2021-05-04 Medtronic, Inc. Peritoneal dialysate flow path sensing
US11013843B2 (en) 2016-09-09 2021-05-25 Medtronic, Inc. Peritoneal dialysis fluid testing system
US10981148B2 (en) 2016-11-29 2021-04-20 Medtronic, Inc. Zirconium oxide module conditioning
JP2019536570A (en) 2016-12-05 2019-12-19 テマセク ポリテクニックTemasek Polytechnic Adsorbents for dialysis devices and systems
US11167070B2 (en) 2017-01-30 2021-11-09 Medtronic, Inc. Ganged modular recharging system
US10960381B2 (en) 2017-06-15 2021-03-30 Medtronic, Inc. Zirconium phosphate disinfection recharging and conditioning
US11278654B2 (en) 2017-12-07 2022-03-22 Medtronic, Inc. Pneumatic manifold for a dialysis system
US11110215B2 (en) 2018-02-23 2021-09-07 Medtronic, Inc. Degasser and vent manifolds for dialysis
CN108653299B (en) * 2018-06-18 2020-11-10 江苏纳海生物科技有限公司 Preparation method of dialysate
US11213616B2 (en) 2018-08-24 2022-01-04 Medtronic, Inc. Recharge solution for zirconium phosphate
US11806457B2 (en) 2018-11-16 2023-11-07 Mozarc Medical Us Llc Peritoneal dialysis adequacy meaurements
US11806456B2 (en) 2018-12-10 2023-11-07 Mozarc Medical Us Llc Precision peritoneal dialysis therapy based on dialysis adequacy measurements
US11850344B2 (en) 2021-08-11 2023-12-26 Mozarc Medical Us Llc Gas bubble sensor
US11965763B2 (en) 2021-11-12 2024-04-23 Mozarc Medical Us Llc Determining fluid flow across rotary pump

Family Cites Families (11)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR2154983A5 (en) * 1971-10-01 1973-05-18 Thomson Csf Artificial kidney machine - uses closed circuit regeneration of small volume of dialysis liquid
FR2170868B1 (en) * 1972-02-04 1976-07-09 Rhone Poulenc Ind
JPS6359353A (en) * 1986-08-30 1988-03-15 Res Dev Corp Of Japan High-molecular urea adsorbent
US5969052A (en) * 1996-12-31 1999-10-19 Kimberly Clark Worldwide, Inc. Temperature sensitive polymers and water-dispersible products containing the polymers
GB0018467D0 (en) * 2000-07-27 2000-09-13 Strakan Pharm Ltd Adhesives
WO2002040039A2 (en) 2000-11-20 2002-05-23 Dow Global Technologies Inc. In vivo use of water absorbent polymers
US20050233003A1 (en) * 2001-09-28 2005-10-20 Solubest Ltd. Hydrophilic dispersions of nanoparticles of inclusion complexes of salicylic acid
US9346029B2 (en) * 2005-06-06 2016-05-24 The University Of British Columbia Polymer-based serum albumin substitute
DE102006026948B3 (en) * 2006-06-09 2007-12-06 Rewatronik Gmbh Heating arrangement for soldering surface-mounted devices comprises a heat storage device for partially storing and releasing heat from a gas stream heated and passed through the heating arrangement and an infrared radiator
JP2007244393A (en) * 2007-05-14 2007-09-27 Sumika Agrotech Co Ltd Method for preparing seedling-raising culture soil, seedling-raising culture soil and set for preparing seedling-raising culture soil
US8220643B2 (en) 2008-06-06 2012-07-17 Fresenius Medical Care Holdings, Inc. Urea sorbent

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2014151322A1 (en) 2013-03-14 2014-09-25 Fresenius Medical Care Holdings, Inc. Universal portable machine for online hemodiafiltration using regenerated dialysate
US9433720B2 (en) 2013-03-14 2016-09-06 Fresenius Medical Care Holdings, Inc. Universal portable artificial kidney for hemodialysis and peritoneal dialysis
US10549023B2 (en) 2013-03-14 2020-02-04 Fresenius Medical Care Holdings, Inc. Universal portable artificial kidney for hemodialysis and peritoneal dialysis
US10792414B2 (en) 2013-03-14 2020-10-06 Fresenius Medical Care Holdings, Inc. Universal portable machine for online hemodiafiltration using regenerated dialysate
EP3777914A1 (en) 2013-03-14 2021-02-17 Fresenius Medical Care Holdings, Inc. Universal portable machine for online hemodiafiltration using regenerated dialysate
US11246972B2 (en) 2013-03-14 2022-02-15 Fresenius Medical Care Holdings, Inc. Universal portable machine for online hemodiafiltration using regenerated dialysate
US11701459B2 (en) 2013-03-14 2023-07-18 Fresenius Medical Care Holdings, Inc. Universal portable artificial kidney for hemodialysis and peritoneal dialysis

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US20130313188A1 (en) 2013-11-28

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