WO1996009851A1 - Method of preparing silver chloride electrodes for iontophoretic drug delivery devices - Google Patents
Method of preparing silver chloride electrodes for iontophoretic drug delivery devices Download PDFInfo
- Publication number
- WO1996009851A1 WO1996009851A1 PCT/US1995/012398 US9512398W WO9609851A1 WO 1996009851 A1 WO1996009851 A1 WO 1996009851A1 US 9512398 W US9512398 W US 9512398W WO 9609851 A1 WO9609851 A1 WO 9609851A1
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- silver
- silver chloride
- matrix
- chloride
- quenching
- Prior art date
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- 229910021607 Silver chloride Inorganic materials 0.000 title claims abstract description 195
- HKZLPVFGJNLROG-UHFFFAOYSA-M silver monochloride Chemical compound [Cl-].[Ag+] HKZLPVFGJNLROG-UHFFFAOYSA-M 0.000 title claims abstract description 195
- 238000000034 method Methods 0.000 title claims abstract description 92
- 238000012377 drug delivery Methods 0.000 title description 9
- 239000011159 matrix material Substances 0.000 claims abstract description 125
- BQCADISMDOOEFD-UHFFFAOYSA-N Silver Chemical compound [Ag] BQCADISMDOOEFD-UHFFFAOYSA-N 0.000 claims abstract description 108
- 229910052709 silver Inorganic materials 0.000 claims abstract description 105
- 239000004332 silver Substances 0.000 claims abstract description 105
- 238000000576 coating method Methods 0.000 claims abstract description 47
- 239000011248 coating agent Substances 0.000 claims abstract description 46
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 claims abstract description 23
- 239000010949 copper Substances 0.000 claims abstract description 23
- 229910052802 copper Inorganic materials 0.000 claims abstract description 21
- 230000008569 process Effects 0.000 claims abstract description 14
- 238000007598 dipping method Methods 0.000 claims abstract description 7
- 238000010791 quenching Methods 0.000 claims description 33
- 230000000171 quenching effect Effects 0.000 claims description 33
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims description 15
- 229910052799 carbon Inorganic materials 0.000 claims description 15
- 238000002844 melting Methods 0.000 claims description 14
- 230000008018 melting Effects 0.000 claims description 14
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 13
- 239000000463 material Substances 0.000 claims description 12
- 229910001868 water Inorganic materials 0.000 claims description 11
- 238000001816 cooling Methods 0.000 claims description 10
- 238000010438 heat treatment Methods 0.000 claims description 8
- ATJFFYVFTNAWJD-UHFFFAOYSA-N Tin Chemical compound [Sn] ATJFFYVFTNAWJD-UHFFFAOYSA-N 0.000 claims description 6
- HCHKCACWOHOZIP-UHFFFAOYSA-N Zinc Chemical compound [Zn] HCHKCACWOHOZIP-UHFFFAOYSA-N 0.000 claims description 6
- 239000011230 binding agent Substances 0.000 claims description 6
- BASFCYQUMIYNBI-UHFFFAOYSA-N platinum Chemical compound [Pt] BASFCYQUMIYNBI-UHFFFAOYSA-N 0.000 claims description 6
- 229910052718 tin Inorganic materials 0.000 claims description 6
- 229910052725 zinc Inorganic materials 0.000 claims description 6
- 239000011701 zinc Substances 0.000 claims description 6
- XKRFYHLGVUSROY-UHFFFAOYSA-N Argon Chemical compound [Ar] XKRFYHLGVUSROY-UHFFFAOYSA-N 0.000 claims description 4
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 claims description 4
- 239000012535 impurity Substances 0.000 claims description 4
- 239000000843 powder Substances 0.000 claims description 4
- 239000011261 inert gas Substances 0.000 claims description 3
- 229910052697 platinum Inorganic materials 0.000 claims description 3
- 239000007787 solid Substances 0.000 claims description 3
- 229910052786 argon Inorganic materials 0.000 claims description 2
- 239000001307 helium Substances 0.000 claims description 2
- 229910052734 helium Inorganic materials 0.000 claims description 2
- SWQJXJOGLNCZEY-UHFFFAOYSA-N helium atom Chemical compound [He] SWQJXJOGLNCZEY-UHFFFAOYSA-N 0.000 claims description 2
- 229910052757 nitrogen Inorganic materials 0.000 claims description 2
- 230000004927 fusion Effects 0.000 claims 2
- 239000003814 drug Substances 0.000 description 26
- 239000010944 silver (metal) Substances 0.000 description 25
- 229940079593 drug Drugs 0.000 description 23
- 238000011068 loading method Methods 0.000 description 11
- 150000002500 ions Chemical class 0.000 description 10
- 230000009467 reduction Effects 0.000 description 10
- 238000006243 chemical reaction Methods 0.000 description 9
- 230000010287 polarization Effects 0.000 description 9
- 238000012360 testing method Methods 0.000 description 9
- FAPWRFPIFSIZLT-UHFFFAOYSA-M Sodium chloride Chemical compound [Na+].[Cl-] FAPWRFPIFSIZLT-UHFFFAOYSA-M 0.000 description 8
- 238000003487 electrochemical reaction Methods 0.000 description 8
- 239000003792 electrolyte Substances 0.000 description 8
- 238000002360 preparation method Methods 0.000 description 8
- 238000000151 deposition Methods 0.000 description 7
- 230000008021 deposition Effects 0.000 description 7
- 230000000694 effects Effects 0.000 description 6
- 239000000376 reactant Substances 0.000 description 6
- VEXZGXHMUGYJMC-UHFFFAOYSA-M Chloride anion Chemical compound [Cl-] VEXZGXHMUGYJMC-UHFFFAOYSA-M 0.000 description 5
- 239000004020 conductor Substances 0.000 description 5
- 230000005518 electrochemistry Effects 0.000 description 5
- 239000002245 particle Substances 0.000 description 5
- 239000000758 substrate Substances 0.000 description 5
- 239000011135 tin Substances 0.000 description 5
- 150000001450 anions Chemical class 0.000 description 4
- 238000005868 electrolysis reaction Methods 0.000 description 4
- 238000002474 experimental method Methods 0.000 description 4
- 238000012545 processing Methods 0.000 description 4
- 230000032258 transport Effects 0.000 description 4
- 230000015572 biosynthetic process Effects 0.000 description 3
- 238000010349 cathodic reaction Methods 0.000 description 3
- 230000008859 change Effects 0.000 description 3
- 239000008367 deionised water Substances 0.000 description 3
- 229910021641 deionized water Inorganic materials 0.000 description 3
- 230000037427 ion transport Effects 0.000 description 3
- 238000004519 manufacturing process Methods 0.000 description 3
- 238000007086 side reaction Methods 0.000 description 3
- 239000011780 sodium chloride Substances 0.000 description 3
- 239000000243 solution Substances 0.000 description 3
- 229920000049 Carbon (fiber) Polymers 0.000 description 2
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 2
- 238000013019 agitation Methods 0.000 description 2
- 230000003444 anaesthetic effect Effects 0.000 description 2
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 2
- 239000004917 carbon fiber Substances 0.000 description 2
- 150000001768 cations Chemical class 0.000 description 2
- 239000000919 ceramic Substances 0.000 description 2
- -1 chloride anions Chemical class 0.000 description 2
- 238000013461 design Methods 0.000 description 2
- 230000001627 detrimental effect Effects 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 238000009826 distribution Methods 0.000 description 2
- 230000008030 elimination Effects 0.000 description 2
- 238000003379 elimination reaction Methods 0.000 description 2
- 239000007789 gas Substances 0.000 description 2
- 239000011551 heat transfer agent Substances 0.000 description 2
- 239000001257 hydrogen Substances 0.000 description 2
- 229910052739 hydrogen Inorganic materials 0.000 description 2
- 239000010416 ion conductor Substances 0.000 description 2
- 239000000155 melt Substances 0.000 description 2
- 230000003647 oxidation Effects 0.000 description 2
- 238000007254 oxidation reaction Methods 0.000 description 2
- 239000001301 oxygen Substances 0.000 description 2
- 229910052760 oxygen Inorganic materials 0.000 description 2
- 230000003071 parasitic effect Effects 0.000 description 2
- 238000007747 plating Methods 0.000 description 2
- 239000012266 salt solution Substances 0.000 description 2
- NDVLTYZPCACLMA-UHFFFAOYSA-N silver oxide Chemical compound [O-2].[Ag+].[Ag+] NDVLTYZPCACLMA-UHFFFAOYSA-N 0.000 description 2
- 230000000699 topical effect Effects 0.000 description 2
- QCHFTSOMWOSFHM-WPRPVWTQSA-N (+)-Pilocarpine Chemical compound C1OC(=O)[C@@H](CC)[C@H]1CC1=CN=CN1C QCHFTSOMWOSFHM-WPRPVWTQSA-N 0.000 description 1
- SNICXCGAKADSCV-JTQLQIEISA-N (-)-Nicotine Chemical compound CN1CCC[C@H]1C1=CC=CN=C1 SNICXCGAKADSCV-JTQLQIEISA-N 0.000 description 1
- NGNBDVOYPDDBFK-UHFFFAOYSA-N 2-[2,4-di(pentan-2-yl)phenoxy]acetyl chloride Chemical compound CCCC(C)C1=CC=C(OCC(Cl)=O)C(C(C)CCC)=C1 NGNBDVOYPDDBFK-UHFFFAOYSA-N 0.000 description 1
- 229930000680 A04AD01 - Scopolamine Natural products 0.000 description 1
- MHAJPDPJQMAIIY-UHFFFAOYSA-N Hydrogen peroxide Chemical compound OO MHAJPDPJQMAIIY-UHFFFAOYSA-N 0.000 description 1
- STECJAGHUSJQJN-GAUPFVANSA-N Hyoscine Natural products C1([C@H](CO)C(=O)OC2C[C@@H]3N([C@H](C2)[C@@H]2[C@H]3O2)C)=CC=CC=C1 STECJAGHUSJQJN-GAUPFVANSA-N 0.000 description 1
- STECJAGHUSJQJN-UHFFFAOYSA-N N-Methyl-scopolamin Natural products C1C(C2C3O2)N(C)C3CC1OC(=O)C(CO)C1=CC=CC=C1 STECJAGHUSJQJN-UHFFFAOYSA-N 0.000 description 1
- SNIOPGDIGTZGOP-UHFFFAOYSA-N Nitroglycerin Chemical compound [O-][N+](=O)OCC(O[N+]([O-])=O)CO[N+]([O-])=O SNIOPGDIGTZGOP-UHFFFAOYSA-N 0.000 description 1
- QCHFTSOMWOSFHM-UHFFFAOYSA-N SJ000285536 Natural products C1OC(=O)C(CC)C1CC1=CN=CN1C QCHFTSOMWOSFHM-UHFFFAOYSA-N 0.000 description 1
- 230000001464 adherent effect Effects 0.000 description 1
- 125000000129 anionic group Chemical group 0.000 description 1
- 230000000712 assembly Effects 0.000 description 1
- 238000000429 assembly Methods 0.000 description 1
- 244000309464 bull Species 0.000 description 1
- 125000002091 cationic group Chemical group 0.000 description 1
- 150000003841 chloride salts Chemical class 0.000 description 1
- GTKRFUAGOKINCA-UHFFFAOYSA-M chlorosilver;silver Chemical compound [Ag].[Ag]Cl GTKRFUAGOKINCA-UHFFFAOYSA-M 0.000 description 1
- 239000004927 clay Substances 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 238000007796 conventional method Methods 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 230000002950 deficient Effects 0.000 description 1
- 238000009792 diffusion process Methods 0.000 description 1
- 238000004090 dissolution Methods 0.000 description 1
- 230000009189 diving Effects 0.000 description 1
- 230000005684 electric field Effects 0.000 description 1
- 239000007772 electrode material Substances 0.000 description 1
- 238000003411 electrode reaction Methods 0.000 description 1
- 239000011532 electronic conductor Substances 0.000 description 1
- 238000011156 evaluation Methods 0.000 description 1
- 239000004744 fabric Substances 0.000 description 1
- 239000010946 fine silver Substances 0.000 description 1
- 230000004907 flux Effects 0.000 description 1
- 230000037406 food intake Effects 0.000 description 1
- 229960003711 glyceryl trinitrate Drugs 0.000 description 1
- 238000010348 incorporation Methods 0.000 description 1
- 229910010272 inorganic material Inorganic materials 0.000 description 1
- 239000011147 inorganic material Substances 0.000 description 1
- 230000003834 intracellular effect Effects 0.000 description 1
- 229910052751 metal Inorganic materials 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 1
- 238000013508 migration Methods 0.000 description 1
- 230000005012 migration Effects 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 229960002715 nicotine Drugs 0.000 description 1
- SNICXCGAKADSCV-UHFFFAOYSA-N nicotine Natural products CN1CCCC1C1=CC=CN=C1 SNICXCGAKADSCV-UHFFFAOYSA-N 0.000 description 1
- 229960001416 pilocarpine Drugs 0.000 description 1
- 229920005989 resin Polymers 0.000 description 1
- 239000011347 resin Substances 0.000 description 1
- 230000027756 respiratory electron transport chain Effects 0.000 description 1
- 238000012552 review Methods 0.000 description 1
- STECJAGHUSJQJN-FWXGHANASA-N scopolamine Chemical compound C1([C@@H](CO)C(=O)O[C@H]2C[C@@H]3N([C@H](C2)[C@@H]2[C@H]3O2)C)=CC=CC=C1 STECJAGHUSJQJN-FWXGHANASA-N 0.000 description 1
- 229960002646 scopolamine Drugs 0.000 description 1
- 239000004065 semiconductor Substances 0.000 description 1
- SDLBJIZEEMKQKY-UHFFFAOYSA-M silver chlorate Chemical compound [Ag+].[O-]Cl(=O)=O SDLBJIZEEMKQKY-UHFFFAOYSA-M 0.000 description 1
- 229910001923 silver oxide Inorganic materials 0.000 description 1
- 229910052708 sodium Inorganic materials 0.000 description 1
- 239000011734 sodium Substances 0.000 description 1
- GGCZERPQGJTIQP-UHFFFAOYSA-N sodium;9,10-dioxoanthracene-2-sulfonic acid Chemical compound [Na+].C1=CC=C2C(=O)C3=CC(S(=O)(=O)O)=CC=C3C(=O)C2=C1 GGCZERPQGJTIQP-UHFFFAOYSA-N 0.000 description 1
- 238000003756 stirring Methods 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 239000000725 suspension Substances 0.000 description 1
- 230000002459 sustained effect Effects 0.000 description 1
- 230000001225 therapeutic effect Effects 0.000 description 1
- 230000037317 transdermal delivery Effects 0.000 description 1
- 238000013271 transdermal drug delivery Methods 0.000 description 1
- 238000006276 transfer reaction Methods 0.000 description 1
- 238000002604 ultrasonography Methods 0.000 description 1
- 238000001771 vacuum deposition Methods 0.000 description 1
- 230000003313 weakening effect Effects 0.000 description 1
Classifications
-
- A—HUMAN NECESSITIES
- A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
- A61N—ELECTROTHERAPY; MAGNETOTHERAPY; RADIATION THERAPY; ULTRASOUND THERAPY
- A61N1/00—Electrotherapy; Circuits therefor
- A61N1/02—Details
- A61N1/04—Electrodes
- A61N1/0404—Electrodes for external use
- A61N1/0408—Use-related aspects
- A61N1/0428—Specially adapted for iontophoresis, e.g. AC, DC or including drug reservoirs
- A61N1/0432—Anode and cathode
-
- A—HUMAN NECESSITIES
- A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
- A61N—ELECTROTHERAPY; MAGNETOTHERAPY; RADIATION THERAPY; ULTRASOUND THERAPY
- A61N1/00—Electrotherapy; Circuits therefor
- A61N1/02—Details
- A61N1/04—Electrodes
- A61N1/0404—Electrodes for external use
- A61N1/0408—Use-related aspects
- A61N1/0428—Specially adapted for iontophoresis, e.g. AC, DC or including drug reservoirs
- A61N1/0432—Anode and cathode
- A61N1/0436—Material of the electrode
Definitions
- the present invention relates to iontophoresis and more particularly to a method of preparing a low cost manufacturable silver chloride electrode suitable for use as a cathode in iontophoretic drug delivery devices.
- transdermal drug delivery systems there are two types of transdermal drug delivery systems, i.e., "passive” and “active.”
- passive transdermal systems chemical potential gradients provide the dominant diving force to deliver the drug through the skin.
- a patch containing the drug is applied to the surface of the body and the drug moves into the body predominantly driven by diffusion controlled transport.
- passive transdermal systems include: delivery of nicotine, nitroglycerine, scopolamine, application of topical anesthetic to provide localized pain relief.
- Iontophoresis In active transdermal systems, additional user assisted driving forces, either electrical (iontophoresis) or ultrasound (pho ⁇ ophoresis), are used to control the delivery of the drugs through the skin.
- Iontophoresis In iontophoretic devices for delivering ionized drugs through the skin have been known since the early 1900's. Iontophoresis, according to Stedma ⁇ 's Medical Dictionary, is defined as "the introduction into the tissues, by means of an electric current , of the ions of a chosen medicament.” In iontophoretic transdermal systems electric potential gradients provide the dominant driving force to deliver the ionized drug through the skin.
- an iontophoretic patch containing the drug is applied to the surface of the body, controlled current is driven through the patch via electrodes in contact with the patch and the drug moves into the body predominantly driven by migration controlled transport due to electric fields setup in the iontophoretic patch by the applied current.
- iontophoretic transdermal systems include: delivery of pilocarpine in diagnosing cystic f ibrosis, delivery of topical anesthetic to name a few.
- the iontophoretic patch primarily consists at a minimum of two compartments, an anode and a cathode, each of which are individually in contact with the body.
- the electrode compartments house the electrodes in contact with the ionic media and are disposed to be in intimate ionic contact with some portion of the body through the skin, to complete the internal electrical circuit.
- the electrodes are connected externally to a power supply to complete the external electrical circuit. During operation the entire system, power source, electrode, electrolyte, the skin and the body, forms one integrated electrochemical cell
- the electrode connected to the positive pole of the power supply is called the anode and the electrode connected to the negative pole of the power supply is called the cathode.
- the current is turned on at the power supply, current flows from the anode to the cathode in the system controlled externally (to the patch) by electron transport and internally (inside the patch between the electrodes) by ion transport.
- the electrodes act as transducers coverting electron transport to ion transport via an electron transfer reaction (electrochemical reaction) at the electrode
- iontophoresis can be used to deliver the ionized drug across the skin separator into the body
- the most commonly used cathode in iontophoretic systems is the Ag/AgCI cathode.
- the standard thermodynamic reduction equilibrium potential for the Ag/AgCI couple is 0.222V vs NHE (Normal Hydrogen Electrode).
- the desired electrochemical reaction at the cathode during iontophoresis is the reduction of AgCI to Ag:
- SU 1132210 teaches preparing a silver chloride electrode on a silver matrix by treating the silver base with a hydrogen peroxide solution containing chloride.
- GB 2215844 discloses a silver/silver chloride electrode prepared by vigorously stirring fine silver particles suspended in an aqueous chloride salt solution, slowly adding an aqueous silver salt solution while maintaining the suspension so that particles at nucleatio ⁇ sites form silver chloride particles, and, recovering the silver/silver chloride particles. The resulting silver particles coated with silver chloride are then formed into an electrode.
- the silver/silver chloride electrodes were intended to be used as reference electrodes, with no functional requirement of supporting a current being driven through them as is required of a cathode for iontophoresis.
- the most common technique for preparing iontophoretic AgCI cathodes involves electrolytic oxidation of Ag to AgCI in acid chloride environment.
- the desired electrochemical reaction is:
- Electrolytic chloriding also demands use of pure silver as feed stock for the conversion process. However during the conversion process less than 50% is typically chlorided to satisfy electron conduction requirements resulting in use of pure silver as a current collector in the electrode. It must be pointed out that the cathodic reaction does not require Ag as reactant and in fact pure silver is produced as a product of the cathodic reaction.
- the use of pure Ag as current collector in electrolytic AgCI cathodes adds to the material cost of the cathode.Further in the electrolytic process the uniformity of AgCI la ⁇ down is controlled by the current distribution on the electrode in the conversion cell. Any non uniform current distribution on the electrode surface (including edge effects) will result in selective chloriding weakening the mechanical integrity and reducing the reliability of the electrodes.
- the conventional method for preparing silver chloride electrodes by electrolytically chloriding silver electrodes suffers from performance, manufacturing and cost related problems.
- the lack of low cost, easily and rapidly prepared reliable silver chloride electrodes limits the availability of iontophoretic devices.
- the present invention of a method for preparing an active silver chloride electrode provides an easily manufactured, reliable, low cost, high capacity cathode (more than 2 mA hr/cm?) which will facilitate the use of iontophoresis as a drug delivery technique.
- An active silver chloride electrode suitable for long duration use as a cathode in an iontophoretic drug delivery system may be prepared in a few seconds using the method of the present invention from low cost materials.
- the currently available preparative methods for active silver chloride electrodes require hours and high cost materials to provide an electrode with similar or deficient functional properties to electrodes prepared by the method of the present invention.
- a method for preparing a silver chloride electrode suitable for use as a cathode for an iontophoretic device includes an electrically conductive matrix which has a surface to serve as an electrode.
- the conductive matrix is placed in molten silver chloride.
- the method for preparing a silver chloride electrode preferably then includes allowing the conductive matrix sufficient residence time in the silver chloride melt to produce a substantially continuous silver chloride coating having a thickness on at least a portion of the conductive matrix.
- the method then includes withdrawing the conductive matrix from the molten silver chloride. After withdrawal of the conductive matrix from the silver chloride the method preferably includes cooling / quenching the conductive matrix and allowing a sufficient time to cool and harden the silver chloride coating.
- Suitable materials for the conductive matrix include but are not limited to, silver, copper plated with silver, platinum, zinc plated with silver, tin plated with silver, carbon, carbon plated with silver, carbon impregnated with a binding agent and plated with silver.
- the conductive matrix is preferably dipped in a vessel with molten silver chloride.
- the silver chloride application may either include electrolytically coating a silver / silver-plated matrix with silver chloride at a temperature below the melting point of silver chloride or applying a finely divided powder of silver chloride to the surface of the conductive matrix. Both of the alternative methods of application result in formation of a discontinuous coating of silver chloride on the surface of the conductive matrix.
- the method then includes heating the applied discontinuous silver chloride coating above the melting temperature of silver chloride, thus, fusing the silver chloride into a continuous coating and then hardening the now continuous coating by cooling/quenching.
- Fig. 1 is a schematic representation of an iontophoretic drug delivery device having a cathode formed by the method of the present invention
- Fig. 2a is a schematic representation of a conductive matrix before applying a silver chloride coating in accordance with the method of the present invention, wherein the conductive matrix a solid conductive matrix;
- Fig. 2b is a schematic representation of the solid conductive matrix illustrated in Fig. 2a with a silver chloride coating applied thereon in accordance with the method of the present invention
- Fig. 2c is a schematic representation of a silver chloride electrode of the present invention after a period of use as a cathode in an iontophoretic device;
- Fig.2d is a schematic representation of a conductive matrix before applying a silver chloride coating in accordance with the method of the present invention, wherein the conductive matrix is a pourous conductive matrix;
- Fig. 2e is a schematic representation of the pourous conductive matrix illustrated in Fig. 2d with a silver chloride coating applied to both sides of the matrix with the method of the present invention.
- Fig. 3 is a process flow diagram for the method of the present invention for preparing a silver chloride cathode.
- Fig. 4a is a graph depicting single electrode potential data for a AgCI coated Ag mesh cathode prepared by the method of the present invention as described in Example 1.
- Fig. 4b is a graph depicting single electrode potential data for a AgCI coated Ag plated Cu mesh cathode prepared by the method of the present invention as described in Example 2.
- an iontophoretic device 10 includes a power source 20, a controller 22, an anode assembly 30 and a cathode assembly 40 which are electrically interconnected with electrical conductors 45 to form a complete electrical circuit 60 when device 10 is mounted on a skin surface 50 of a patient and activated.
- Device 10 further includes a reservoir 31 and an anode conductive matrix 34 as part of anode assembly 30 and a reservoir 41 and a cathode conductive matrix 44 as part of cathode assembly 40 as well as a housing 100 (schematically shown in phantom), for holding the anode and cathode assemblies to the skin, to the power source, to the controller, and to each other.
- power source 20 In order for electrical current to flow through the device and the skin, electrons must move between anode assembly 30 and cathode assembly 40 through power source 20 and controller 22 through conductors 45, with an ionic flow between anode assembly 30 and cathode assembly 40 through the body of the patient.
- the function of power source 20 is to provide a source of required current and voltage to operate the iontophoretic device.
- Current conduction inside the anode/cathode reservoir is via ion transport and is utilized to deliver a medicament having a charge from one or both reservoirs into the patient through skin surface 50.
- a typical anode contains a positively lonizable drug molecule D, water and an electrolyte with chloride as anion, preferably sodium chloride.
- the cathode reservoir may contain just an electrolyte, preferably sodium chloride.
- the electrochemical reaction occurring at the anode is:
- the drug and anolyte cations will be transported from the anode patch into the body while the chlroide anions from the body will be transported into the anolyte.
- the electrochemical reaction at the cathode is:
- the catholyte anions and the chloride anions produced at the electrode will be transported into the body whereas the sodium cations from the body will be transported into the catholyte.
- a silver mesh or silver foil matrix is electrolytically chlorided, i.e., an electric current is applied to the silver matrix in a solution containing chloride ion, so that silver is oxidized to silver chloride forming a coating on the silver matrix. Since a silver matrix is required, the initial cost of the electrode is significant, and since the generation of silver chloride is done electrolytically, the deposition of silver chloride will likely be discontinuous and not uniform and generally is not physically durable. This is especially true when making high capacity electrodes or those electrodes suitable for long duration use. Generation of milligram quantities of silver chloride electrolytically requires considerable time, considerable silver and, such a process is not easily automated. As was shown above, silver is not even required for the cathode reaction, it is generated by reduction of silver chloride during the iontophoresis.
- Fig. 2b schematically shows a silver chloride electrode 70 prepared by the preferred method suitable for use in a cathode assembly in an iontophoretic delivery device.
- the preferred method includes providing a conductive matrix 44 having a surface 42 with a means for connecting 43 the conductive matrix 44 to device 10. These means 43 may be an uncoated extension of the conductive matrix, a wire, a printed circuit conductor to which the conductive matrix is electrically connected and the like.
- the method then includes providing a station which includes silver chloride.
- the station preferably includes a vessel containing molten silver chloride, and the matrix is preferably dipped into the melt.
- the preferred method then provides a quenching bath, preferably water.
- the elements for manipulating the conductive matrix may simply be forceps or tongs.
- the conductive matrix is then engaged with the manipulating elements and placed into the silver chloride station for a sufficient amount of time to allow the matrix to acquire a substantially continuous coating of the silver chloride on at least a portion of the surface of the conductive matrix.
- the conductive matrix having the coating of silver chloride on its surface is then preferably withdrawn from the silver chloride station and transferred to the quenching station.
- the matrix with the silver chloride on its surface preferably is allowed to remain for suf icient time for the silver chloride coating on the surface of the conductive matrix to cool to a hardened state.
- the quenching station includes a water bath in which the conductive matrix is placed and allowed sufficient time for the silver chloride to cool to a hardened state.
- the conductive matrix preferably is then removed from the quenching station and disengaged from the manipulative elements providing completed silver chloride electrode 70 suitable for use in a cathode assembly in an iontophoretic device.
- Suitable materials for forming the conductive matrix include, but are not limited to, silver, copper plated with silver, zinc plated with silver, platinum, tin plated with silver, carbon, carbon plated with silver, carbon with a suitable binder and carbon with a suitable binder plated with silver.
- the purpose of the silver plating on the copper, tin and the zinc matrices, is to prevent reaction of the copper, tin or the zinc with molten silver chloride. Since the silver serves only to render the conductive copper, tin or zinc inert to the molten silver chloride, the actual amount of silver required is very small.
- a suitable binder for carbon includes inorganic materials such as clay or organic resins commonly used as fluxes in the semiconductor industry mixed with carbon in a range between about thirty percent to about ninety percent carbon.
- carbon is intended to include forming a suitable matrix from carbon fibers, including woven materials, non 5 woven materials and the like.
- preferred conductive matrix 44 acquires a substantially continuous coating of silver chloride 46 when passed through the preferred molten silver chloride.
- preferred electrode 70 prepared by the method of the present invention is suitable to be installed in
- the conductive matrix is a pourous conductive matrix and as shown in Fig. 2e the silver chloride may be caoted on both sides of the pourous matrix.
- An example of a pourous matrix is a metal or metallic mesh.
- the conductive matrix on which the silver chloride is coated on both sides is pourous so that the electrons may pass through the matrix to reach and utilize the silver chloride on the other side.
- the conductive matrix is all silver.
- silver is formed by the reduction of silver chloride at the cathode by acquisition of an electron during iontophoresis.
- the present method is suitable for preparing an electrode with silver or other non-silver conductive materials as the conductive matrix.
- a silver chloride electrode where silver is used as the conductive matrix prepared by the instant method is physically more durable and uniform than one prepared electrolytically.
- the electrode of the present invention may be loaded with 35 sufficient silver chloride to meet duration of use and quantity requirements as applicable for intended use of each electrode manufactured.
- the time required for preparation of a silver chloride electrode by the method of the present invention is measured in seconds using silver as the conductive matrix compared to hours for an silver chloride electrode of comparable capacity prepared by electrolytic deposition.
- a copper or other non-silver conductive matrix plated with silver is suitable for forming a silver chloride electrode by the method of the present invention.
- a copper matrix by itself may not be satisfactory for some applications. If a copper matrix plated with silver is used to form a silver chloride electrode by the common electrolytic generation method, there would need to be sufficient silver plated on the matrix to form the desired amount of silver chloride.
- a comparable capacity silver chloride electrode produced with a copper conductive matrix by the method of the present invention needs only sufficient silver plated onto the copper matrix to prevent undesirable side reactions between the copper and the molten silver chloride.
- All of the silver chloride needed to provide the same functional capability as the silver/silver chloride electrode, for use as a cathode in an iontophoretic device, is coated onto the conductive matrix using the same method as would be used for a pure silver matrix, thereby providing the same cathode functional capability at a greatly reduced cost.
- the silver chloride layer formed by this method would likely not be uniform, would lack physical integrity and would be discontinuous.
- the delivery of electrons can be done at a higher current for a shorter time, however, the silver chloride layer formed would surely not be u ⁇ iform.be discontinuous and would not have the physical integrity of an electrode prepared by the method of the present invention.
- the preferred method may include an intermediate cooling step followed by a return to the molten silver chloride for additional loading of silver chloride.
- the first pass through the molten silver chloride provides a coating of silver chloride having an initial thickness, with each subsequent pass adding additional thickness and additional mass.
- Each pass of the conductive matrix through the preferred molten silver chloride requires only seconds. Thus, the total time required, even for high loadings of silver chloride, is small compared to the time required for electrolytic deposition of equivalent amounts.
- the matrix with the silver chloride coating is preferably then quenched, providing a glassy, hard and durable silver chloride surface.
- the silver chloride is a vessel having molten silver chloride therein, and the matrix is dipped into the molten silver chloride for the coating step, preferably the intermediate cooling step may simply be a withdrawal from the molten silver chloride for a brief period of time followed by a replicate dipping, or it may include cooling by air or an inert gas.
- the method of the present invention also includes applying a coating of silver chloride to the conductive matrix at a temperature below the melting point of silver chloride followed by heating the silver chloride coating above its melting point to fuse it, and then quenching it to form a hard glassy surface.
- the application of silver chloride below the melting point includes, but is not limited to, powder coating, vacuum deposition, or in the case where the conductive matrix is silver, electrolytic generation of silver chloride.
- the instant method may also include automated localized heating for fusing of the silver chloride coating preferably followed by rapid quenching that would allow the use of flexible web as a carrier in an automated process.
- automated localized heating for fusing of the silver chloride coating preferably followed by rapid quenching that would allow the use of flexible web as a carrier in an automated process.
- the present use of controlled localized heating followed by rapid quenching would allow the use of a carrier web which otherwise is unable to directly withstand the melting point of silver chloride (455° C.) and enable the backing to be utilized as part of the reservoir for the cathode as well as the electrode itself, further simplifying the construction of the iontophoretic device.
- the silver chloride application and the quenching preferably includes inert atmosphere gas blanket on the molten pool to avoid incorporation of impurities into the silver chloride coating. Additionally, while the quenching preferably includes deionized water as the heat transfer agent, it may also include non-reactive gases such as nitrogen, argon, helium and the like as heat transfer agents.
- Example 1 describes the preparation of a silver chloride electrode on a silver mesh matrix.
- Example 2 describes the preparation of a silver chloride electrode on a copper mesh matrix plated with about 0.1 mil of silver. Test results are shown in Table 1 comparing the electrode of example 1 with the electrode of Example 2 in a functional model for use as an iontophoretic cathode. The results show that the performance of a silver chloride electrode formed on the silver plated copper matrix is not different than the performance of the silver chloride electrode formed on the all silver matrix.
- Figure 4a presents the single electrode potential data (versus AgCI wire reference electrode) for the cathode and the anode during the dechloriding test conducted as described in the experimental setup section.
- the cathode was 2.5cm square Ag mesh (4Ag6.5031 ) thermally coated with approximately 53mg of AgCI melt.
- the anode was 2.5cm square Ag mesh (6Agl -77); the electrolyte was 150mM saline solution at room temperature with no agitation; and the current density was 0.4mA/sq.cm.
- the polarization on the cathode at 0.4 mA/sq.cm. is 20mV initially and increases to 50mV at the end of the experiment.
- the signal stays relatively stable throughout the life of the experiment.
- the increase in polarization from 20mV to 50mV is due to concentration overpotential effects at the electrode.
- the low and stable electrode polarization is very encouragining suggesting good electrode performance and a stable electrode structure with easily accessible AgCI reactant and electrolyte.
- the cathode overpotential increases rapidly exceeding 50mV indicating a change in the electrochemistry at the electrode from silver chloride to water electrolysis.
- the electrode is practically "dead" for iontophoretic application since the electrolysis of water at the cathode will lead to detrimental pH effects.
- the coulombic experimental specific capacity of the electrode for AgCI reduction from the above data is calculated to be 9.72 mA-hr/sq.cm.
- the theoretical specific capacity calculated is 9.9 mA-hr/sq.cm.
- the percent utilization of AgCI is determined based on the ratio of the experimental specific capacity to the theoretical specific capactiy is then calculated to be 98.2%.
- Figure 4b presents the single electrode potential data (versus AgCI wire reference electrode) for the cathode and the anode during the dechloriding test conducted as described in the experimental setup section.
- the cathode was 1.0cm square Ag/Cu mesh "0.1 mil” Ag coated 4Cu7-100) thermally coated with approximately 80mg of AgCI melt.
- the anode was I.Ocm square Ag mesh (6Agl0077); the electrolyte was I ⁇ OmM saline solution at room temperature with no agitation; and the current density was 0.4mA/sq.cm.
- the polarization on the cathode at 0.4 mA/sq.cm is 20mV initially and increases to 5lmV at the end of the experiment.
- the signal stays relatively stable throughout the life of the experiment.
- the increase in polarization from 20mV to 5lmV is due to concentration overpotential effects at the electrode.
- the low and stable electrode polarization is very encouraging suggesting good electrode performance and a stable electrode structure with easily accessible AgCI reactant and electrolyte.
- the coulombic experimental capacity of the electrode for AgCI reduction from the above data is calculated to be 14.3 mA-hr/sq.cm.
- the theoretical specific capacity calculated is 14.84 mA-hr/sq.cm.
- the percent utilization of AgCI is determined based on the ratio of the experimental specific capacity to the theoretical specific capactiy is then calculated to be 96.3%.
- Table 1 presents a comparison of the electrodes of example 1 and example 2 in a functional evaluation of electrochemically accessible silver chloride for the reaction:
- Electrodes prepared according to Examples 1 and 2 were each installed as a cathode versus a silver mesh anode in test cells containing aqueous 150 millimolar sodium chloride solution. Exposed cathode area was 1 cm? varied from 1 -2.5 cm?. Testing was done under constant current control and the operating current density was 0.4 mA/cm?. The cathode potential was monitored with a Ag/AgCI reference electrode and the testing was stopped when the electrode reaction switched from AgCI reduction to hydrogen evolution (as observed from the change in the cathode polarization). The experimentally available coulombic capacity of the electrode was determined from the current density and the lifetime of the electrode for AgCI reduction electrochemistry.
- the silver conductive matrix has a higher substrate specific weight because it is a less open and thicker mesh than silver plated copper.
- the silver plated copper conductive matrix acquired a higher loading of silver chloride than the pure silver because of the different mesh dimensions. This data suggests that the mesh design can be effectvely used to vary and control AgCI loading onto the substrate.
- the specific capacity of the cathodes tested was in excess of 10 mA.hr/cm?. This implies that at 0.4 mA/cm? current density the cathodes can be safely operated with AgCI reduction electrochemistry in excess of 24 hrs. Also the utilization of the AgCI active mass (as calculated from the experimental and theoretical specific capacities) in the electrodes tested was in excess of 90% suggesting good electrode structure (ionic and electronic) and efficient use of the active electrode material.
Abstract
A method for preparing a silver chloride electrode suitable to use as a cathode for an iontophoretic device includes a conductive matrix having a surface to serve as an electrode, and silver chloride. The method further includes placing the conductive matrix into the silver chloride for a sufficient residence time, generally only a few seconds, to allow the conductive matrix to acquire a coating of silver chloride. The matrix is then withdrawn from the silver chloride and quenched, hardening the silver chloride. The matrix with the hardened silver chloride on its surface is then ready for placement in an iontophoretic device as a cathode. Preferably, the method includes dipping the conductive matrix into molten silver chloride forming a layer of silver chloride on its surface. The dipping process may be repeated to increase the thickness of the silver chloride coating when there is a requirement for more silver chloride than can be acquired in a single pass through the silver chloride. Results show that an electrode prepared on a silver plated copper matrix compares favorably with a pure silver matrix.
Description
UNITED STATES PATENT APPLICATION
Method of Preparing Silver Chloride Electrodes for Iontophoretic Drug Delivery Devices
Field of the Invention
The present invention relates to iontophoresis and more particularly to a method of preparing a low cost manufacturable silver chloride electrode suitable for use as a cathode in iontophoretic drug delivery devices.
Background of the Invention
Delivery of medicaments into the body is accomplished by a variety of techniques. Oral ingestion and hypodermic delivery are the most common. Recently, transdermal delivery systems have become an increasingly important means of administering drugs. Such systems offer advantages clearly not achievable by other modes of delivery such as: controlled programmable sustained delivery, reduced side effects, non invasive to name a few.
Presently there are two types of transdermal drug delivery systems, i.e., "passive" and "active." In passive transdermal systems chemical potential gradients provide the dominant diving force to deliver the drug through the skin. For these drugs, a patch containing the drug is applied to the surface of the body and the drug moves into the body predominantly driven by diffusion controlled transport. Some examples of passive transdermal systems include: delivery of nicotine, nitroglycerine, scopolamine, application of topical anesthetic to provide localized pain relief.
In active transdermal systems, additional user assisted driving forces, either electrical (iontophoresis) or ultrasound (phoπophoresis), are used to control the delivery of the drugs through the skin. Iontophoretic devices for delivering ionized drugs through the skin have been known since the early 1900's. Iontophoresis, according to Stedmaπ's Medical Dictionary, is defined as "the introduction into the tissues, by means of an electric current , of the ions of a chosen medicament." In iontophoretic transdermal systems electric potential gradients provide the dominant driving force to deliver the ionized drug through the skin. For these drugs, an iontophoretic patch containing the drug is applied to the surface of the body, controlled current is driven through the patch via electrodes in contact with the patch and the drug moves into the body predominantly driven by migration controlled transport due to electric fields setup in the iontophoretic patch
by the applied current. Some examples of iontophoretic transdermal systems include: delivery of pilocarpine in diagnosing cystic f ibrosis, delivery of topical anesthetic to name a few.
The iontophoretic patch primarily consists at a minimum of two compartments, an anode and a cathode, each of which are individually in contact with the body. The electrode compartments house the electrodes in contact with the ionic media and are disposed to be in intimate ionic contact with some portion of the body through the skin, to complete the internal electrical circuit. The electrodes are connected externally to a power supply to complete the external electrical circuit. During operation the entire system, power source, electrode, electrolyte, the skin and the body, forms one integrated electrochemical cell
The electrode connected to the positive pole of the power supply is called the anode and the electrode connected to the negative pole of the power supply is called the cathode. When the current is turned on at the power supply, current flows from the anode to the cathode in the system controlled externally (to the patch) by electron transport and internally (inside the patch between the electrodes) by ion transport. This is possible because the electrodes act as transducers coverting electron transport to ion transport via an electron transfer reaction (electrochemical reaction) at the electrode
In general positive ions (cations) will tend to carry portion of the current and move towards the cathode and the negative (anions) ions will tend to carry portion of the curent and move towards the anode Hence by loading cationic drugs in the anode compartment and/or anionic drugs in the cathode compartment, iontophoresis can be used to deliver the ionized drug across the skin separator into the body
The most commonly used cathode in iontophoretic systems is the Ag/AgCI cathode. The standard thermodynamic reduction equilibrium potential for the Ag/AgCI couple is 0.222V vs NHE (Normal Hydrogen Electrode). The desired electrochemical reaction at the cathode during iontophoresis is the reduction of AgCI to Ag:
AgCI + e* - - > Ag + Cl-
It is obvious to one of skill in the art, from the equation that only in regions where the following three minimum conditions are met will the cathodic reaction proceed: (i) accessibility to reactant AgCI, (n) accessibility to an electron conductor for reactant electrons, and (iii) accessibility to an ion conductor for product chloride ions to carry the current into solution. Hence the desired cathode must contain the required AgCI reactant in contact with an electronic conductor and an ionic conductor. The theoretical minimum amount of AgCI required to support the electrochemical reaction at the cathode can be calculated from the current density and time using Faraday's law. Thus for example, to support current density of 0.5 mA/cm? for 24 hours, one would need a minimum of 64 mg/cm^ of AgCI loading. Additional factors that would increase the AgCI loading requirements will include utilization of active mass and over design for safety.
The scientific and patent literature abounds in articles on prepartion and study of Ag/AgCI electrodes Thomas, in lon Sensitive Intracellular Microelectrodes. Academic Press, 1984, describes chloriding of silver wires for use as microelectrodes by dipping them into molten silver chloride. Additionally, Souto et al., J Appl. Electrochem.,15 (1985) pp.727-735 and Souto, Bull. Electrochem. 6(7) July 1990, pp. 691 693 describe the preparation of silver/silver chloride electrodes by heating a mixture of silver oxide and silver
chlorate molded around a silver wire. SU 1132210 teaches preparing a silver chloride electrode on a silver matrix by treating the silver base with a hydrogen peroxide solution containing chloride. GB 2215844 discloses a silver/silver chloride electrode prepared by vigorously stirring fine silver particles suspended in an aqueous chloride salt solution, slowly adding an aqueous silver salt solution while maintaining the suspension so that particles at nucleatioπ sites form silver chloride particles, and, recovering the silver/silver chloride particles. The resulting silver particles coated with silver chloride are then formed into an electrode. In the above cited reports from the literature, the silver/silver chloride electrodes were intended to be used as reference electrodes, with no functional requirement of supporting a current being driven through them as is required of a cathode for iontophoresis.
The most common technique for preparing iontophoretic AgCI cathodes involves electrolytic oxidation of Ag to AgCI in acid chloride environment. The desired electrochemical reaction is:
Ag + Cl- - - > AgCI + e-
Other parasitic side reactions include silver dissolution:
Ag - « > Ag+ + e- and oxygen evolution:
H20 - - > 1/2 02 + 2H+ -Re¬
united States Patent No. 5,084,006 discloses a cathode from a silver/silver chloride couple. United States Patent No. 5,057,072 also discloses a silver/silver chloride cathode. In both of these disclosures, herein incorporated by reference, there are teachings that the silver/silver chloride couple is generated electrolytically.
But the electrolytic production of AgCI cathodes suffers from several problems. The process is time consuming. The typical operating current density at 100% current efficiency for oxidation of Ag to AgCI is 1 mA/cm^. Preparation of an electrode at this current density to operate at O.δmA/cm^ for 24 hours would take a minimum of 12 hours. Since the processing time is high the processing cost of the electrode would also be high. If the operating current density is increased to reduce the processing time, the current efficient decreases due to the parasitic side reactions at the electrode.
Further, evolution of oxygen at the electrode will result in noπ adherent cracked AgCI films with less than desirable mechanical properties. Electrolytic chloriding also demands use of pure silver as feed stock for the conversion process. However during the conversion process less than 50% is typically chlorided to satisfy electron conduction requirements resulting in use of pure silver as a current collector in the electrode. It must be pointed out that the cathodic reaction does not require Ag as reactant and in fact pure silver is produced as a product of the cathodic reaction. The use of pure Ag as current collector in electrolytic AgCI cathodes adds to the material cost of the cathode.Further in the electrolytic process the uniformity of AgCI laγdown is controlled by the current distribution on the electrode in the conversion cell. Any non uniform current
distribution on the electrode surface (including edge effects) will result in selective chloriding weakening the mechanical integrity and reducing the reliability of the electrodes.
Hence there is a need for a method to produce reliable, inexpensive and manufacturable AgCI cathodes for iontophoretic use. Such a method is disclosed herein below and will help advance the art and availability of iontophoretic devices.
Summary of the Invention
As iontophoretic delivery of drugs becomes more widely utilized, the demand for silver chloride electrodes for use as cathodes will accordingly increase. The conventional method for preparing silver chloride electrodes by electrolytically chloriding silver electrodes suffers from performance, manufacturing and cost related problems. The lack of low cost, easily and rapidly prepared reliable silver chloride electrodes limits the availability of iontophoretic devices. The present invention of a method for preparing an active silver chloride electrode provides an easily manufactured, reliable, low cost, high capacity cathode (more than 2 mA hr/cm?) which will facilitate the use of iontophoresis as a drug delivery technique.
An active silver chloride electrode suitable for long duration use as a cathode in an iontophoretic drug delivery system may be prepared in a few seconds using the method of the present invention from low cost materials. The currently available preparative methods for active silver chloride electrodes require hours and high cost materials to provide an electrode with similar or deficient functional properties to electrodes prepared by the method of the present invention.
A method for preparing a silver chloride electrode suitable for use as a cathode for an iontophoretic device includes an electrically conductive matrix which has a surface to serve as an electrode. Preferably, the conductive matrix is placed in molten silver chloride. The method for preparing a silver chloride electrode preferably then includes allowing the conductive matrix sufficient residence time in the silver chloride melt to produce a substantially continuous silver chloride coating having a thickness on at least a portion of the conductive matrix. Preferably the method then includes withdrawing the conductive matrix from the molten silver chloride. After withdrawal of the conductive matrix from the silver chloride the method preferably includes cooling / quenching the conductive matrix and allowing a sufficient time to cool and harden the silver chloride coating.
Suitable materials for the conductive matrix include but are not limited to, silver, copper plated with silver, platinum, zinc plated with silver, tin plated with silver, carbon, carbon plated with silver, carbon impregnated with a binding agent and plated with silver.
In the silver chloride application, the conductive matrix is preferably dipped in a vessel with molten silver chloride. Alternatively, the silver chloride application may either include electrolytically coating a silver / silver-plated matrix with silver chloride at a temperature below the melting point of silver chloride or applying a finely divided powder of silver chloride to the surface of the conductive matrix. Both of the alternative methods of application result in formation of a discontinuous coating of silver chloride on the
surface of the conductive matrix. In these alternatives, the method then includes heating the applied discontinuous silver chloride coating above the melting temperature of silver chloride, thus, fusing the silver chloride into a continuous coating and then hardening the now continuous coating by cooling/quenching.
Brief Description of the Drawings
Fig. 1 is a schematic representation of an iontophoretic drug delivery device having a cathode formed by the method of the present invention;
Fig. 2a is a schematic representation of a conductive matrix before applying a silver chloride coating in accordance with the method of the present invention, wherein the conductive matrix a solid conductive matrix;
Fig. 2b is a schematic representation of the solid conductive matrix illustrated in Fig. 2a with a silver chloride coating applied thereon in accordance with the method of the present invention;
Fig. 2c is a schematic representation of a silver chloride electrode of the present invention after a period of use as a cathode in an iontophoretic device;
Fig.2d is a schematic representation of a conductive matrix before applying a silver chloride coating in accordance with the method of the present invention, wherein the conductive matrix is a pourous conductive matrix;
Fig. 2e is a schematic representation of the pourous conductive matrix illustrated in Fig. 2d with a silver chloride coating applied to both sides of the matrix with the method of the present invention; and
Fig. 3 is a process flow diagram for the method of the present invention for preparing a silver chloride cathode.
Fig. 4a is a graph depicting single electrode potential data for a AgCI coated Ag mesh cathode prepared by the method of the present invention as described in Example 1.
Fig. 4b is a graph depicting single electrode potential data for a AgCI coated Ag plated Cu mesh cathode prepared by the method of the present invention as described in Example 2.
Detailed Description of the Preferred Embodiments
While this invention is satisfied by embodiments in many different forms, there is illustrated in the drawings and will herein be described in detail preferred embodiments of the invention with the understanding that the present disclosure is to be considered as exemplary of the principles of the invention and is not intended to limit the invention to the embodiments illustrated.
As shown in Fig. 1, generally an iontophoretic device 10 includes a power source 20, a controller 22, an anode assembly 30 and a cathode assembly 40 which are electrically interconnected with electrical conductors 45 to form a complete electrical circuit 60 when device 10 is mounted on a skin surface 50 of a patient and activated. Device 10 further includes a reservoir 31 and an anode conductive matrix 34 as part of anode assembly 30 and a reservoir 41 and a cathode conductive matrix 44 as part of cathode assembly 40 as well as a housing 100 (schematically shown in phantom), for holding the anode and cathode assemblies to the skin, to the power source, to the controller, and to each other.
In order for electrical current to flow through the device and the skin, electrons must move between anode assembly 30 and cathode assembly 40 through power source 20 and controller 22 through conductors 45, with an ionic flow between anode assembly 30 and cathode assembly 40 through the body of the patient. The function of power source 20 is to provide a source of required current and voltage to operate the iontophoretic device. Current conduction inside the anode/cathode reservoir is via ion transport and is utilized to deliver a medicament having a charge from one or both reservoirs into the patient through skin surface 50.
When the current is turned on in a typical operating iontophoretic device with Ag/AgCI electrode system electrochemical reactions take place at the electrodes. The result of these reactions is an electron current through the circuit and an ion flow to and from the body between the cathode and anode. Many therapeuticaliy useful drugs are ionized to a positive ion and thus will be transported in an iontophoretic process from the anode. A typical anode contains a positively lonizable drug molecule D, water and an electrolyte with chloride as anion, preferably sodium chloride. The cathode reservoir may contain just an electrolyte, preferably sodium chloride.
The electrochemical reaction occurring at the anode is:
Ag + CI- - - > AgCI + e- (1)
The drug and anolyte cations will be transported from the anode patch into the body while the chlroide anions from the body will be transported into the anolyte.
The electrochemical reaction at the cathode is:
AgCI + e- - - > Ag + Cl*. (2)
The catholyte anions and the chloride anions produced at the electrode will be transported into the body whereas the sodium cations from the body will be transported into the catholyte.
In order for drug delivery to progress satisfactorily, there generally must be substantially more equivalent silver chloride molecules in the cathode than equivalent drug molecules to be delivered from the anode. The reason for the excess silver chloride is that the ion current due to drug molecule delivery from the anode assembly is generally less than ten percent of the total ion current from the anode, the balance of the ion current being carried by smaller electrolyte ions. This directly places a greater demand on the active mass
requirement at the electrodes (Ag at anode and AgCI at cathode). Thus, for the longer duration of delivery required for many drugs, where milligram quantities of the drug are required for the desired therapeutic effect, substantial quantities of silver chloride must be available at the cathode.
In most of the commonly used iontophoretic cathodes, a silver mesh or silver foil matrix is electrolytically chlorided, i.e., an electric current is applied to the silver matrix in a solution containing chloride ion, so that silver is oxidized to silver chloride forming a coating on the silver matrix. Since a silver matrix is required, the initial cost of the electrode is significant, and since the generation of silver chloride is done electrolytically, the deposition of silver chloride will likely be discontinuous and not uniform and generally is not physically durable. This is especially true when making high capacity electrodes or those electrodes suitable for long duration use. Generation of milligram quantities of silver chloride electrolytically requires considerable time, considerable silver and, such a process is not easily automated. As was shown above, silver is not even required for the cathode reaction, it is generated by reduction of silver chloride during the iontophoresis.
The preferred method for forming silver chloride electrodes by the present invention is schematically demonstrated in Figs. 2a-2c and the process flow diagram in Fig. 3. Fig. 2b schematically shows a silver chloride electrode 70 prepared by the preferred method suitable for use in a cathode assembly in an iontophoretic delivery device. The preferred method includes providing a conductive matrix 44 having a surface 42 with a means for connecting 43 the conductive matrix 44 to device 10. These means 43 may be an uncoated extension of the conductive matrix, a wire, a printed circuit conductor to which the conductive matrix is electrically connected and the like. Preferably, the method then includes providing a station which includes silver chloride. The station preferably includes a vessel containing molten silver chloride, and the matrix is preferably dipped into the melt. The preferred method then provides a quenching bath, preferably water. For a small scale manufacture of electrodes following the method of the present invention, the elements for manipulating the conductive matrix may simply be forceps or tongs. Preferably, the conductive matrix is then engaged with the manipulating elements and placed into the silver chloride station for a sufficient amount of time to allow the matrix to acquire a substantially continuous coating of the silver chloride on at least a portion of the surface of the conductive matrix. The conductive matrix having the coating of silver chloride on its surface is then preferably withdrawn from the silver chloride station and transferred to the quenching station. In the quenching station, the matrix with the silver chloride on its surface preferably is allowed to remain for suf icient time for the silver chloride coating on the surface of the conductive matrix to cool to a hardened state. In a preferred embodiment of the method of the present invention the quenching station includes a water bath in which the conductive matrix is placed and allowed sufficient time for the silver chloride to cool to a hardened state. The conductive matrix preferably is then removed from the quenching station and disengaged from the manipulative elements providing completed silver chloride electrode 70 suitable for use in a cathode assembly in an iontophoretic device.
Suitable materials for forming the conductive matrix include, but are not limited to, silver, copper plated with silver, zinc plated with silver, platinum, tin plated with silver, carbon, carbon plated with silver, carbon with a suitable binder and carbon with a suitable binder plated with silver. The purpose of the silver plating on the copper, tin and the zinc matrices, is to prevent reaction of the copper, tin or the zinc with molten silver chloride. Since the silver serves only to render the conductive copper, tin or zinc inert to the
molten silver chloride, the actual amount of silver required is very small. A suitable binder for carbon includes inorganic materials such as clay or organic resins commonly used as fluxes in the semiconductor industry mixed with carbon in a range between about thirty percent to about ninety percent carbon. In this description carbon is intended to include forming a suitable matrix from carbon fibers, including woven materials, non 5 woven materials and the like.
As is shown in Fig. 2b, preferred conductive matrix 44 acquires a substantially continuous coating of silver chloride 46 when passed through the preferred molten silver chloride. As is shown schematically in Fig. 2b, preferred electrode 70 prepared by the method of the present invention is suitable to be installed in
10 cathode assembly 40 in iontophoretic device 10 of Fig. 1. When electode 70 of the present invention is placed in a cathode assembly 40 as shown in Fig. 1 and an iontophoretic drug delivery process is initiated by driving current through the iontophoretic device, electrode 70 undergoes an electrochemical reaction according to equation (2) and develops the structure shown in Fig. 2c. In this application, the current flow reduces silver chloride to silver forming a silver layer 48 at an interface 47 between the silver chloride layer
15 46 and the conductive matrix 44. In the preffered embodiment shown in Fig. 2d, the conductive matrix is a pourous conductive matrix and as shown in Fig. 2e the silver chloride may be caoted on both sides of the pourous matrix. An example of a pourous matrix is a metal or metallic mesh. The conductive matrix on which the silver chloride is coated on both sides is pourous so that the electrons may pass through the matrix to reach and utilize the silver chloride on the other side. 0
In many prior cathodes used in iontophoretic devices, the conductive matrix is all silver. As is seen from the drawings and with the review of the electrochemistry occurring at the electrodes during iontophoresis, it is apparent that it is not even necessary that silver be present in the cathode, except for the small amount used as plating during the present coating process to prevent undesirable reactions between the 5 non-silver conductive matrix and the molten silver chloride. Silver is formed by the reduction of silver chloride at the cathode by acquisition of an electron during iontophoresis. By elimination of the need for substantial quantities of silver, the cost of the electrode is greatly reduced, and by elimination of the need for electrolytic generation and deposition of silver chloride on the silver conductive matrix for formation of a silver chloride electrode, the silver chloride electrode becomes much more easily and rapidly manufactured. 0
However, it should be appreciated that the present method is suitable for preparing an electrode with silver or other non-silver conductive materials as the conductive matrix. A silver chloride electrode where silver is used as the conductive matrix prepared by the instant method is physically more durable and uniform than one prepared electrolytically. Additionally, the electrode of the present invention may be loaded with 35 sufficient silver chloride to meet duration of use and quantity requirements as applicable for intended use of each electrode manufactured. Furthermore, the time required for preparation of a silver chloride electrode by the method of the present invention is measured in seconds using silver as the conductive matrix compared to hours for an silver chloride electrode of comparable capacity prepared by electrolytic deposition.
40 A copper or other non-silver conductive matrix plated with silver is suitable for forming a silver chloride electrode by the method of the present invention. A copper matrix by itself may not be satisfactory for some applications. If a copper matrix plated with silver is used to form a silver chloride electrode by the common electrolytic generation method, there would need to be sufficient silver plated on the matrix to form
the desired amount of silver chloride. A comparable capacity silver chloride electrode produced with a copper conductive matrix by the method of the present invention needs only sufficient silver plated onto the copper matrix to prevent undesirable side reactions between the copper and the molten silver chloride. All of the silver chloride needed to provide the same functional capability as the silver/silver chloride electrode, for use as a cathode in an iontophoretic device, is coated onto the conductive matrix using the same method as would be used for a pure silver matrix, thereby providing the same cathode functional capability at a greatly reduced cost.
For a silver chloride cathode to be effective in an iontophoretic device, there must be sufficient silver chloride available to sustain the reaction, as shown in equation (2) above, which provides chloride ion for the ion current from the cathode, for the time necessary to complete the desired drug dosage delivery. For example, if it was desired to operate the device 10, as shown in Fig. 1, at four tenths of a milliamp per cm? for twenty four hours, 51.4 milligrams or 0.358 milliequivalents of silver chloride would be required per cm?. Deposition of this quantity electrolytically requires the equivalent amount of coulombs for this current and will require several hours at typical operating current densities presuming 100% current efficiency . The silver chloride layer formed by this method would likely not be uniform, would lack physical integrity and would be discontinuous. The delivery of electrons can be done at a higher current for a shorter time, however, the silver chloride layer formed would surely not be uπiform.be discontinuous and would not have the physical integrity of an electrode prepared by the method of the present invention.
In the present method, where a single pass of the conductive matrix through the preferred molten silver chloride does not provide a sufficient amount of silver chloride coating for the intended application, the preferred method may include an intermediate cooling step followed by a return to the molten silver chloride for additional loading of silver chloride. The first pass through the molten silver chloride provides a coating of silver chloride having an initial thickness, with each subsequent pass adding additional thickness and additional mass. Each pass of the conductive matrix through the preferred molten silver chloride requires only seconds. Thus, the total time required, even for high loadings of silver chloride, is small compared to the time required for electrolytic deposition of equivalent amounts. When the desired loading or thickness of silver chloride has been achieved, the matrix with the silver chloride coating is preferably then quenched, providing a glassy, hard and durable silver chloride surface. In the preferred method, the silver chloride is a vessel having molten silver chloride therein, and the matrix is dipped into the molten silver chloride for the coating step, preferably the intermediate cooling step may simply be a withdrawal from the molten silver chloride for a brief period of time followed by a replicate dipping, or it may include cooling by air or an inert gas.
In addition to the preferred method of coating the conductive matrix by dipping it into a melt of silver chloride, the method of the present invention also includes applying a coating of silver chloride to the conductive matrix at a temperature below the melting point of silver chloride followed by heating the silver chloride coating above its melting point to fuse it, and then quenching it to form a hard glassy surface. The application of silver chloride below the melting point includes, but is not limited to, powder coating, vacuum deposition, or in the case where the conductive matrix is silver, electrolytic generation of silver chloride. These below melting point applications of the present method followed by heating the coating to fuse it and form a continuous layer of AgCI, offer the opportunity to automate the formation of the electrodes on a flexible backing such as carbon fiber fabrics or films. The instant method may also include automated
localized heating for fusing of the silver chloride coating preferably followed by rapid quenching that would allow the use of flexible web as a carrier in an automated process. The present use of controlled localized heating followed by rapid quenching would allow the use of a carrier web which otherwise is unable to directly withstand the melting point of silver chloride (455° C.) and enable the backing to be utilized as part of the reservoir for the cathode as well as the electrode itself, further simplifying the construction of the iontophoretic device.
The silver chloride application and the quenching preferably includes inert atmosphere gas blanket on the molten pool to avoid incorporation of impurities into the silver chloride coating. Additionally, while the quenching preferably includes deionized water as the heat transfer agent, it may also include non-reactive gases such as nitrogen, argon, helium and the like as heat transfer agents.
Two examples are given below for preparation of silver chloride electrodes illustrating the method described in this invention. Example 1 describes the preparation of a silver chloride electrode on a silver mesh matrix. Example 2 describes the preparation of a silver chloride electrode on a copper mesh matrix plated with about 0.1 mil of silver. Test results are shown in Table 1 comparing the electrode of example 1 with the electrode of Example 2 in a functional model for use as an iontophoretic cathode. The results show that the performance of a silver chloride electrode formed on the silver plated copper matrix is not different than the performance of the silver chloride electrode formed on the all silver matrix.
Example 1
Materials: a) Silver Mesh coupon 1 cm x 4 cm (Delker Corp., Branford, CT; #4Ag6.5031) with a surface substantially free from impurities; b) Silver Chloride (Baxter #21424).
Procedure: a) Place about 25 gm silver chloride (Melting Point - 455° C) in a ceramic crucible and heat to a temperature about 525° C. b) Grasp the silver coupon with tongs and vertically dip the coupon into the molten silver chloride for about 5 seconds. c) Vertically withdraw the coupon from the molten silver chloride and vertically dip into an ambient temperature deionized water quenching bath for about 5 seconds. d) Remove the coupon from the quenching bath and release from the tongs. A substantially transparent glassy coating of silver chloride is visible on the surface of the coupon.
Figure 4a presents the single electrode potential data (versus AgCI wire reference electrode) for the cathode and the anode during the dechloriding test conducted as described in the experimental setup section. The cathode was 2.5cm square Ag mesh (4Ag6.5031 ) thermally coated with approximately 53mg of AgCI melt. The anode was 2.5cm square Ag mesh (6Agl -77); the electrolyte was 150mM saline solution at room temperature with no agitation; and the current density was 0.4mA/sq.cm.
The polarization on the cathode at 0.4 mA/sq.cm. is 20mV initially and increases to 50mV at the end of the experiment. The signal stays relatively stable throughout the life of the experiment. The increase in polarization from 20mV to 50mV is due to concentration overpotential effects at the electrode. The low and stable electrode polarization is very encouragining suggesting good electrode performance and a stable electrode structure with easily accessible AgCI reactant and electrolyte. After approximately 24 hours, the
cathode overpotential increases rapidly exceeding 50mV indicating a change in the electrochemistry at the electrode from silver chloride to water electrolysis. At this time, the electrode is practically "dead" for iontophoretic application since the electrolysis of water at the cathode will lead to detrimental pH effects.
The coulombic experimental specific capacity of the electrode for AgCI reduction from the above data is calculated to be 9.72 mA-hr/sq.cm. Using Faraday's law and the specific weight of AgCI loading, the theoretical specific capacity calculated is 9.9 mA-hr/sq.cm. The percent utilization of AgCI is determined based on the ratio of the experimental specific capacity to the theoretical specific capactiy is then calculated to be 98.2%.
Example 2
Materials: a) Copper Mesh coupon 1 cm x 4 cm (Delker Corp., Branford, CT; #4Cu7100) plated with 0.1mm silver with a surface substantially free from impurities; b) Silver Chloride (Baxter #2142-4). Procedure: a) Place about 25 gm silver chloride (Melting Point - 455° C) in a ceramic crucible and heat to a temperature about 525° C. b) Grasp the silver plated copper coupon with tongs and vertically dip the coupon into the molten silver chloride for about 5 seconds. c) Vertically withdraw the coupon from the molten silver chloride and vertically dip into an ambient temperature deionized water quenching bath for about 5 seconds. d) Remove the coupon from the quenching bath and release from the tongs. A substantially transparent glassy coating of silver chloride is visible on the surface of the coupon.
Figure 4b presents the single electrode potential data (versus AgCI wire reference electrode) for the cathode and the anode during the dechloriding test conducted as described in the experimental setup section. The cathode was 1.0cm square Ag/Cu mesh "0.1 mil" Ag coated 4Cu7-100) thermally coated with approximately 80mg of AgCI melt. The anode was I.Ocm square Ag mesh (6Agl0077); the electrolyte was IδOmM saline solution at room temperature with no agitation; and the current density was 0.4mA/sq.cm.
The polarization on the cathode at 0.4 mA/sq.cm is 20mV initially and increases to 5lmV at the end of the experiment. The signal stays relatively stable throughout the life of the experiment. The increase in polarization from 20mV to 5lmV is due to concentration overpotential effects at the electrode. The low and stable electrode polarization is very encouraging suggesting good electrode performance and a stable electrode structure with easily accessible AgCI reactant and electrolyte. After approximately 35.75 hours, the cathode overpotential increases rapidly exceeding 60mV indicating a change in the electrochemistry at the electrode from silver chloride to water electrolysis. At this time, the electrode is practically "dead" for iontophoretic application since the electrolysis of water at the cathode will lead to detrimental pH effects.
The coulombic experimental capacity of the electrode for AgCI reduction from the above data is calculated to be 14.3 mA-hr/sq.cm. Using Faraday's law and the specific weight of AgCI loading, the theoretical specific capacity calculated is 14.84 mA-hr/sq.cm. The percent utilization of AgCI is determined based on the ratio of the experimental specific capacity to the theoretical specific capactiy is then calculated to be 96.3%.
Table 1 presents a comparison of the electrodes of example 1 and example 2 in a functional evaluation of electrochemically accessible silver chloride for the reaction:
AgCI + e - - > Ag + Cl .
Electrodes prepared according to Examples 1 and 2 were each installed as a cathode versus a silver mesh anode in test cells containing aqueous 150 millimolar sodium chloride solution. Exposed cathode area was 1 cm? varied from 1 -2.5 cm?. Testing was done under constant current control and the operating current density was 0.4 mA/cm?. The cathode potential was monitored with a Ag/AgCI reference electrode and the testing was stopped when the electrode reaction switched from AgCI reduction to hydrogen evolution (as observed from the change in the cathode polarization). The experimentally available coulombic capacity of the electrode was determined from the current density and the lifetime of the electrode for AgCI reduction electrochemistry. From the weight loading of AgCI the theoretical coulombic capacity of the electrode was also calculated from Faradays Law. The utilization of the active mass was then calculated as the ratio between the experimental and theoretical specific capacities. In general, low polarizations ( < 100mV) and utilizations approaching 100% indicate good electrode performance.
Table 1 Comparison of AgCI electrodes formed on a Silver and a Silver Plated Copper Substrate Sample Silver chloride on Silver Silver chloride on Silver plated
(Example 1 ) copper (Example 2)
Time to prepare coating < limn < Imiπ
Substrate Specific Weight gms/cπr 0.0992 0.0284
Active mass specific weight 0.053 0.0795 gms/cm2 (AgCI)
Test Current Density 0.4 04
(mA/cm^l
Polarization (mV) at 5.0 hours 20 20
10.0 23 22
15.0 51 24
Theoretical specific capacity
(mA hours/cπr)
99 14.84
Experimental specific capacity
(mA hours/cirr) 9 72 143 Percent of theory utilized 98.2 96.3
The results shown in the table describe the performance of the example electrodes (for reduction of
AgCI to Ag) when a current of 0.4 milhamps per cm? is maintained in the test cell for a period in excess of 24 hours. The test simulates the use of the electrodes as a cathode in an iontophoretic drug delivery system.
In the table the silver conductive matrix has a higher substrate specific weight because it is a less open and thicker mesh than silver plated copper. The silver plated copper conductive matrix acquired a higher loading of silver chloride than the pure silver because of the different mesh dimensions. This data suggests that the mesh design can be effectvely used to vary and control AgCI loading onto the substrate.
The specific capacity of the cathodes tested was in excess of 10 mA.hr/cm?. This implies that at 0.4 mA/cm? current density the cathodes can be safely operated with AgCI reduction electrochemistry in excess of 24 hrs. Also the utilization of the AgCI active mass (as calculated from the experimental and theoretical specific capacities) in the electrodes tested was in excess of 90% suggesting good electrode structure (ionic and electronic) and efficient use of the active electrode material.
It is noteworthy to observe that the processing time to prepare the high specific capacity electrodes on iπexpenisve substartes with good mechanical properties and with good utilization and performance as described above with the current disclosed method is typically less than a minute.
Preparation of a silver chloride electrode of similar capacity by electrolytic deposition of silver chloride on a silver substrate would require several hours of electrolytic deposition. Additionally, the electrolytically prepared electrode, since it would likely not be as uniform and is not mechanically as strong would likely not be as suitable for use in an iontophoretic device and most certainly would be more costly.
Claims
1. A method for preparing a silver chloride electrode suitable to use as a cathode an iontophoretic device, the method comprising: placing a conductive matrix into silver chloride; allowing said conductive matrix sufficient residence time in said silver chloride for said conductive matrix to acquire a substantially continuous coating of said silver chloride having a thickness on at least a portion said surface of said conductive matrix; quenching said conductive matrix and allowing a sufficient time for cooling said coating of silver chloride to a hardened state; and removing said conductive matrix having said hardened silver chloride coating thereon from said quenching bath.
2. The method of claim 1 wherein said conductive matrix comprises a conductive matrix selected from the group consisting of silver, silver plated copper, platinum, silver plated zinc, silver plated tin, carbon, silver plated carbon, carbon impregnated with a binding agent and carbon impregnated with a binding agent plated with silver.
3. The method of claim 2 wherein said conductive matrix includes a matrix formed and sized to fit an iontophoretic device.
4. The method of claim 2 wherein said step of providing said conductive matrix includes providing a preshaped conductive matrix for an iontophoretic device on a flexible material substantially resistant to said placing and said allowing steps and wherein said steps for said placing, said allowing and said quenching comprises a mechanized process.
5. The method of claim 2 wherein said silver chloride comprises a vessel having molten silver chloride therein and said placing step comprises dipping said conductive matrix into said molten silver chloride.
6. The method of claim 5 wherein said silver chloride further includes an inert gas atmosphere.
7. The method of claim 5 wherein said quenching includes a heat transfer medium selected from the group selected from the group consisting of water, nitrogen, argon and helium.
8. The method of claim 7 wherein said heat transfer medium comprises water and said quenching step comprises placing said conductive matrix having said silver chloride on said surface in said water for a sufficient time for said silver chloride to become a solid.
9. The method of claim 1 wherein said steps of said placing said conductive matrix into said silver chloride, said allowing and said quenching includes an intermediate cooling step before said quenching step and further includes said placing step and said allowing steps being sequentially repeated at least one time
before said quenching step thereby increasing said thickness of said coating of said silver chloride on said surface of said conductive matrix.
10. The method of claim 1 wherein said steps comprising placing, allowing, and quenching further include applying said silver chloride to said surface of said conductive matrix at a temperature below the melting temperature of said silver chloride thereby forming a discontinuous coating on said surface of said silver matrix, followed by heating said silver chloride above the melting temperature of said silver chloride thereby fusing said silver chloride and forming a continuous coating of said silver chloride on said matrix, said continuous coating being hardened by cooling in said quenching step.
10
11. The method of claim 10 wherein said applying said silver chloride to said surface of said conductive matrix at a temperature below the fusion temperature comprises application of a finely divided powder of silver chloride to said surface.
15 12. A method for preparing a silver chloride electrode from a silver matrix suitable to use as a cathode for an iontophoretic device comprising: placing a silver matrix having a surface into silver chloride; allowing said silver matrix sufficient residence time in said silver chloride for said silver matrix to acquire a substantially continuous coating of said silver chloride having a thickness on at least a portion said 0 surface of said silver matrix; and quenching said silver matrix for a sufficient time to cool said coating of silver chloride to a hardened state.
13. The method of claim 12 wherein said silver matrix for said electrode includes a material selected from 5 the group consisting of silver wire, silver mesh and silver sheet, said surface of said silver matrix being substantially free of impurities.
14. The method of claim 13 wherein said silver matrix includes a matrix formed from silver mesh and sized to fit an iontophoretic device. 0
15. The method of claim 13 wherein silver matrix includes providing said silver preshaped for an iontophoretic device cathode on a flexible material substantially resistant to said placing and said allowing steps and said allowing, said withdrawing, said quenching and said removing steps comprises a mechanized process. 5
16. The method of claim 12 wherein said silver chloride comprises a vessel having molten silver chloride therein and said placing step comprises dipping said silver matrix into said molten silver chloride.
17. The method of claim 16 wherein said silver chloride further comprises an inert gas atmosphere. 0
18. The method of claim 12 wherein said steps of said placing, said allowing and quenching include an intermediate cooling step before said quenching and further includes said placing step and said allowing step
being sequentially repeated at least one time before said quenching step thereby increasing said thickness of said coating of said silver chloride on said surface of said silver matrix.
1 . The method of claim 12 wherein said steps comprising placing, allowing, and quenching further include applying said silver chloride to said surface of said silver matrix at a temperature below the melting point temperature of said silver chloride thereby forming a discontinuous coating on said surface of said silver matrix, followed by heating said silver chloride above the melting temperature of said silver chloride thereby fusing said silver chloride and forming a continuous coating of said silver chloride on said matrix, said continuous coating being hardened by cooling in said quenching step.
20. The method of claim 19 wherein said applying said silver chloride to said surface of said silver matrix at a temperature below the melting point temperature of said silver chloride thereby forming a discontinuous coating on said surface comprises an aqueous electrochemical chloridation process.
21. The method of claim 19 wherein said applying said silver chloride to said surface of said silver matrix at a temperature below the fusion temperature comprises application of a finely divided powder of silver chloride to said surface.
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AU37289/95A AU3728995A (en) | 1994-09-29 | 1995-09-25 | Method of preparing silver chloride electrodes for iontophoretic drug delivery devices |
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US31531694A | 1994-09-29 | 1994-09-29 | |
US08/315,316 | 1994-09-29 |
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Cited By (4)
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WO1999038564A1 (en) * | 1998-01-28 | 1999-08-05 | Alza Corporation | Electrochemically reactive cathodes for an electrotransport device |
US6195582B1 (en) | 1998-01-28 | 2001-02-27 | Alza Corporation | Electrotransport device electrode assembly having lower initial resistance |
US6375990B1 (en) | 1997-10-09 | 2002-04-23 | Emory University | Method and devices for transdermal delivery of lithium |
WO2004089464A1 (en) * | 2003-03-31 | 2004-10-21 | Alza Corporation | Electrotransport device having a reservoir housing having a flexible conductive element |
Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
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WO1991011216A1 (en) * | 1990-01-26 | 1991-08-08 | Gensia Pharmaceuticals, Inc. | Iontophoretic transfer electrode and method |
WO1991016944A1 (en) * | 1990-05-07 | 1991-11-14 | Alza Corporation | Iontophoretic delivery device |
-
1995
- 1995-09-25 WO PCT/US1995/012398 patent/WO1996009851A1/en active Application Filing
- 1995-09-25 AU AU37289/95A patent/AU3728995A/en not_active Abandoned
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WO1991011216A1 (en) * | 1990-01-26 | 1991-08-08 | Gensia Pharmaceuticals, Inc. | Iontophoretic transfer electrode and method |
WO1991016944A1 (en) * | 1990-05-07 | 1991-11-14 | Alza Corporation | Iontophoretic delivery device |
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A.ARÉVALO & ALL: "Preparation and reproductibility of a thermal silver-silver chloride electrode", JOURNAL OF APPLIED ELECTROCHEMISTRY, vol. 15, no. 5, pages 727 - 735 * |
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Cited By (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US6375990B1 (en) | 1997-10-09 | 2002-04-23 | Emory University | Method and devices for transdermal delivery of lithium |
WO1999038564A1 (en) * | 1998-01-28 | 1999-08-05 | Alza Corporation | Electrochemically reactive cathodes for an electrotransport device |
US6195582B1 (en) | 1998-01-28 | 2001-02-27 | Alza Corporation | Electrotransport device electrode assembly having lower initial resistance |
US6505069B2 (en) | 1998-01-28 | 2003-01-07 | Alza Corporation | Electrochemically reactive cathodes for an electrotransport device |
WO2004089464A1 (en) * | 2003-03-31 | 2004-10-21 | Alza Corporation | Electrotransport device having a reservoir housing having a flexible conductive element |
US8224435B2 (en) | 2003-03-31 | 2012-07-17 | Alza Corporation | Electrotransport device having a reservoir housing having a flexible conductive element |
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