EP2111305A2 - Revêtement nanoparticulaire de surfaces - Google Patents

Revêtement nanoparticulaire de surfaces

Info

Publication number
EP2111305A2
EP2111305A2 EP08725099A EP08725099A EP2111305A2 EP 2111305 A2 EP2111305 A2 EP 2111305A2 EP 08725099 A EP08725099 A EP 08725099A EP 08725099 A EP08725099 A EP 08725099A EP 2111305 A2 EP2111305 A2 EP 2111305A2
Authority
EP
European Patent Office
Prior art keywords
coating
spray
particles
drug
polymer
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Withdrawn
Application number
EP08725099A
Other languages
German (de)
English (en)
Inventor
Robert A. Hoerr
John V. Carlson
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Nanocopoeia Inc
Original Assignee
Nanocopoeia Inc
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Priority claimed from US11/669,937 external-priority patent/US9248217B2/en
Application filed by Nanocopoeia Inc filed Critical Nanocopoeia Inc
Publication of EP2111305A2 publication Critical patent/EP2111305A2/fr
Withdrawn legal-status Critical Current

Links

Classifications

    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B05—SPRAYING OR ATOMISING IN GENERAL; APPLYING FLUENT MATERIALS TO SURFACES, IN GENERAL
    • B05D—PROCESSES FOR APPLYING FLUENT MATERIALS TO SURFACES, IN GENERAL
    • B05D1/00—Processes for applying liquids or other fluent materials
    • B05D1/02—Processes for applying liquids or other fluent materials performed by spraying
    • B05D1/04—Processes for applying liquids or other fluent materials performed by spraying involving the use of an electrostatic field
    • B05D1/06—Applying particulate materials
    • A—HUMAN NECESSITIES
    • A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61K—PREPARATIONS FOR MEDICAL, DENTAL OR TOILETRY PURPOSES
    • A61K9/00—Medicinal preparations characterised by special physical form
    • A61K9/48—Preparations in capsules, e.g. of gelatin, of chocolate
    • A61K9/50—Microcapsules having a gas, liquid or semi-solid filling; Solid microparticles or pellets surrounded by a distinct coating layer, e.g. coated microspheres, coated drug crystals
    • A61K9/51—Nanocapsules; Nanoparticles
    • A61K9/5107—Excipients; Inactive ingredients
    • A61K9/513—Organic macromolecular compounds; Dendrimers
    • A61K9/5138—Organic macromolecular compounds; Dendrimers obtained by reactions only involving carbon-to-carbon unsaturated bonds, e.g. polyvinyl pyrrolidone, poly(meth)acrylates
    • A—HUMAN NECESSITIES
    • A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61K—PREPARATIONS FOR MEDICAL, DENTAL OR TOILETRY PURPOSES
    • A61K9/00—Medicinal preparations characterised by special physical form
    • A61K9/48—Preparations in capsules, e.g. of gelatin, of chocolate
    • A61K9/50—Microcapsules having a gas, liquid or semi-solid filling; Solid microparticles or pellets surrounded by a distinct coating layer, e.g. coated microspheres, coated drug crystals
    • A61K9/51—Nanocapsules; Nanoparticles
    • A61K9/5107—Excipients; Inactive ingredients
    • A61K9/513—Organic macromolecular compounds; Dendrimers
    • A61K9/5146—Organic macromolecular compounds; Dendrimers obtained otherwise than by reactions only involving carbon-to-carbon unsaturated bonds, e.g. polyethylene glycol, polyamines, polyanhydrides
    • A61K9/5153—Polyesters, e.g. poly(lactide-co-glycolide)
    • A—HUMAN NECESSITIES
    • A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61L—METHODS OR APPARATUS FOR STERILISING MATERIALS OR OBJECTS IN GENERAL; DISINFECTION, STERILISATION OR DEODORISATION OF AIR; CHEMICAL ASPECTS OF BANDAGES, DRESSINGS, ABSORBENT PADS OR SURGICAL ARTICLES; MATERIALS FOR BANDAGES, DRESSINGS, ABSORBENT PADS OR SURGICAL ARTICLES
    • A61L27/00—Materials for grafts or prostheses or for coating grafts or prostheses
    • A61L27/28—Materials for coating prostheses
    • A61L27/34—Macromolecular materials
    • A—HUMAN NECESSITIES
    • A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61L—METHODS OR APPARATUS FOR STERILISING MATERIALS OR OBJECTS IN GENERAL; DISINFECTION, STERILISATION OR DEODORISATION OF AIR; CHEMICAL ASPECTS OF BANDAGES, DRESSINGS, ABSORBENT PADS OR SURGICAL ARTICLES; MATERIALS FOR BANDAGES, DRESSINGS, ABSORBENT PADS OR SURGICAL ARTICLES
    • A61L27/00—Materials for grafts or prostheses or for coating grafts or prostheses
    • A61L27/50—Materials characterised by their function or physical properties, e.g. injectable or lubricating compositions, shape-memory materials, surface modified materials
    • A61L27/54—Biologically active materials, e.g. therapeutic substances
    • A—HUMAN NECESSITIES
    • A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61L—METHODS OR APPARATUS FOR STERILISING MATERIALS OR OBJECTS IN GENERAL; DISINFECTION, STERILISATION OR DEODORISATION OF AIR; CHEMICAL ASPECTS OF BANDAGES, DRESSINGS, ABSORBENT PADS OR SURGICAL ARTICLES; MATERIALS FOR BANDAGES, DRESSINGS, ABSORBENT PADS OR SURGICAL ARTICLES
    • A61L29/00—Materials for catheters, medical tubing, cannulae, or endoscopes or for coating catheters
    • A61L29/08—Materials for coatings
    • A61L29/085—Macromolecular materials
    • A—HUMAN NECESSITIES
    • A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61L—METHODS OR APPARATUS FOR STERILISING MATERIALS OR OBJECTS IN GENERAL; DISINFECTION, STERILISATION OR DEODORISATION OF AIR; CHEMICAL ASPECTS OF BANDAGES, DRESSINGS, ABSORBENT PADS OR SURGICAL ARTICLES; MATERIALS FOR BANDAGES, DRESSINGS, ABSORBENT PADS OR SURGICAL ARTICLES
    • A61L29/00—Materials for catheters, medical tubing, cannulae, or endoscopes or for coating catheters
    • A61L29/14—Materials characterised by their function or physical properties, e.g. lubricating compositions
    • A61L29/16—Biologically active materials, e.g. therapeutic substances
    • A—HUMAN NECESSITIES
    • A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61L—METHODS OR APPARATUS FOR STERILISING MATERIALS OR OBJECTS IN GENERAL; DISINFECTION, STERILISATION OR DEODORISATION OF AIR; CHEMICAL ASPECTS OF BANDAGES, DRESSINGS, ABSORBENT PADS OR SURGICAL ARTICLES; MATERIALS FOR BANDAGES, DRESSINGS, ABSORBENT PADS OR SURGICAL ARTICLES
    • A61L31/00—Materials for other surgical articles, e.g. stents, stent-grafts, shunts, surgical drapes, guide wires, materials for adhesion prevention, occluding devices, surgical gloves, tissue fixation devices
    • A61L31/08—Materials for coatings
    • A61L31/10—Macromolecular materials
    • A—HUMAN NECESSITIES
    • A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61L—METHODS OR APPARATUS FOR STERILISING MATERIALS OR OBJECTS IN GENERAL; DISINFECTION, STERILISATION OR DEODORISATION OF AIR; CHEMICAL ASPECTS OF BANDAGES, DRESSINGS, ABSORBENT PADS OR SURGICAL ARTICLES; MATERIALS FOR BANDAGES, DRESSINGS, ABSORBENT PADS OR SURGICAL ARTICLES
    • A61L31/00—Materials for other surgical articles, e.g. stents, stent-grafts, shunts, surgical drapes, guide wires, materials for adhesion prevention, occluding devices, surgical gloves, tissue fixation devices
    • A61L31/14—Materials characterised by their function or physical properties, e.g. injectable or lubricating compositions, shape-memory materials, surface modified materials
    • A61L31/16—Biologically active materials, e.g. therapeutic substances
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B05—SPRAYING OR ATOMISING IN GENERAL; APPLYING FLUENT MATERIALS TO SURFACES, IN GENERAL
    • B05B—SPRAYING APPARATUS; ATOMISING APPARATUS; NOZZLES
    • B05B5/00—Electrostatic spraying apparatus; Spraying apparatus with means for charging the spray electrically; Apparatus for spraying liquids or other fluent materials by other electric means
    • B05B5/002—Electrostatic spraying apparatus; Spraying apparatus with means for charging the spray electrically; Apparatus for spraying liquids or other fluent materials by other electric means comprising means for neutralising the spray of charged droplets or particules
    • B05B5/003—Electrostatic spraying apparatus; Spraying apparatus with means for charging the spray electrically; Apparatus for spraying liquids or other fluent materials by other electric means comprising means for neutralising the spray of charged droplets or particules by mixing two sprays of opposite polarity
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B05—SPRAYING OR ATOMISING IN GENERAL; APPLYING FLUENT MATERIALS TO SURFACES, IN GENERAL
    • B05B—SPRAYING APPARATUS; ATOMISING APPARATUS; NOZZLES
    • B05B5/00—Electrostatic spraying apparatus; Spraying apparatus with means for charging the spray electrically; Apparatus for spraying liquids or other fluent materials by other electric means
    • B05B5/002—Electrostatic spraying apparatus; Spraying apparatus with means for charging the spray electrically; Apparatus for spraying liquids or other fluent materials by other electric means comprising means for neutralising the spray of charged droplets or particules
    • B05B5/004—Electrostatic spraying apparatus; Spraying apparatus with means for charging the spray electrically; Apparatus for spraying liquids or other fluent materials by other electric means comprising means for neutralising the spray of charged droplets or particules by alternating the polarity of the spray
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B05—SPRAYING OR ATOMISING IN GENERAL; APPLYING FLUENT MATERIALS TO SURFACES, IN GENERAL
    • B05D—PROCESSES FOR APPLYING FLUENT MATERIALS TO SURFACES, IN GENERAL
    • B05D1/00—Processes for applying liquids or other fluent materials
    • B05D1/34—Applying different liquids or other fluent materials simultaneously
    • A—HUMAN NECESSITIES
    • A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61L—METHODS OR APPARATUS FOR STERILISING MATERIALS OR OBJECTS IN GENERAL; DISINFECTION, STERILISATION OR DEODORISATION OF AIR; CHEMICAL ASPECTS OF BANDAGES, DRESSINGS, ABSORBENT PADS OR SURGICAL ARTICLES; MATERIALS FOR BANDAGES, DRESSINGS, ABSORBENT PADS OR SURGICAL ARTICLES
    • A61L2300/00—Biologically active materials used in bandages, wound dressings, absorbent pads or medical devices
    • A—HUMAN NECESSITIES
    • A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61L—METHODS OR APPARATUS FOR STERILISING MATERIALS OR OBJECTS IN GENERAL; DISINFECTION, STERILISATION OR DEODORISATION OF AIR; CHEMICAL ASPECTS OF BANDAGES, DRESSINGS, ABSORBENT PADS OR SURGICAL ARTICLES; MATERIALS FOR BANDAGES, DRESSINGS, ABSORBENT PADS OR SURGICAL ARTICLES
    • A61L2400/00—Materials characterised by their function or physical properties
    • A61L2400/12—Nanosized materials, e.g. nanofibres, nanoparticles, nanowires, nanotubes; Nanostructured surfaces
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B05—SPRAYING OR ATOMISING IN GENERAL; APPLYING FLUENT MATERIALS TO SURFACES, IN GENERAL
    • B05B—SPRAYING APPARATUS; ATOMISING APPARATUS; NOZZLES
    • B05B5/00—Electrostatic spraying apparatus; Spraying apparatus with means for charging the spray electrically; Apparatus for spraying liquids or other fluent materials by other electric means
    • B05B5/025—Discharge apparatus, e.g. electrostatic spray guns
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B05—SPRAYING OR ATOMISING IN GENERAL; APPLYING FLUENT MATERIALS TO SURFACES, IN GENERAL
    • B05B—SPRAYING APPARATUS; ATOMISING APPARATUS; NOZZLES
    • B05B5/00—Electrostatic spraying apparatus; Spraying apparatus with means for charging the spray electrically; Apparatus for spraying liquids or other fluent materials by other electric means
    • B05B5/025—Discharge apparatus, e.g. electrostatic spray guns
    • B05B5/03—Discharge apparatus, e.g. electrostatic spray guns characterised by the use of gas, e.g. electrostatically assisted pneumatic spraying
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B05—SPRAYING OR ATOMISING IN GENERAL; APPLYING FLUENT MATERIALS TO SURFACES, IN GENERAL
    • B05B—SPRAYING APPARATUS; ATOMISING APPARATUS; NOZZLES
    • B05B5/00—Electrostatic spraying apparatus; Spraying apparatus with means for charging the spray electrically; Apparatus for spraying liquids or other fluent materials by other electric means
    • B05B5/08—Plant for applying liquids or other fluent materials to objects
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B05—SPRAYING OR ATOMISING IN GENERAL; APPLYING FLUENT MATERIALS TO SURFACES, IN GENERAL
    • B05B—SPRAYING APPARATUS; ATOMISING APPARATUS; NOZZLES
    • B05B7/00—Spraying apparatus for discharge of liquids or other fluent materials from two or more sources, e.g. of liquid and air, of powder and gas
    • B05B7/02—Spray pistols; Apparatus for discharge
    • B05B7/06—Spray pistols; Apparatus for discharge with at least one outlet orifice surrounding another approximately in the same plane
    • B05B7/061—Spray pistols; Apparatus for discharge with at least one outlet orifice surrounding another approximately in the same plane with several liquid outlets discharging one or several liquids
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B05—SPRAYING OR ATOMISING IN GENERAL; APPLYING FLUENT MATERIALS TO SURFACES, IN GENERAL
    • B05D—PROCESSES FOR APPLYING FLUENT MATERIALS TO SURFACES, IN GENERAL
    • B05D1/00—Processes for applying liquids or other fluent materials
    • B05D1/02—Processes for applying liquids or other fluent materials performed by spraying
    • B05D1/04—Processes for applying liquids or other fluent materials performed by spraying involving the use of an electrostatic field
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B05—SPRAYING OR ATOMISING IN GENERAL; APPLYING FLUENT MATERIALS TO SURFACES, IN GENERAL
    • B05D—PROCESSES FOR APPLYING FLUENT MATERIALS TO SURFACES, IN GENERAL
    • B05D2451/00—Type of carrier, type of coating (Multilayers)

Definitions

  • the present invention relates to coating objects, and more particularly, the present invention relates to coating objects (e.g., medical devices) using electrospray technology.
  • objects e.g., medical devices
  • Local drug delivery may be achieved, for example, by coating balloon catheters, stents, and the like with therapeutic agent to be locally delivered.
  • the coating of medical devices may provide for controlled release, which includes long-term or sustained release, of a bioactive material.
  • medical devices are coated with materials to provide beneficial surface properties.
  • medical devices are often coated with radiopaque materials to allow for fluoroscopic visualization during placement in the body. It is also useful to coat certain devices to achieve enhanced biocompatibility and to improve surface properties such as lubriciousness.
  • stents are implanted within vessels in an effort to maintain the patency thereof by preventing collapse and/or impeding restenosis.
  • implantation of a stent may be accomplished by mounting the stent on the expandable portion of a balloon catheter, maneuvering the catheter through the vasculature so as to position the stent at the treatment site within the body lumen, and inflating the balloon to expand the stent so as to engage the lumen wall.
  • the stent deforms in the expanded configuration allowing the balloon to be deflated and the catheter removed to complete the implantation procedure.
  • self-expanding stents obviates the need for a balloon delivery device. Instead, a constraining sheath that is initially fitted above the stent is simply retracted once the stent is in position adjacent the treatment site.
  • Stents and stent delivery catheters are well known in the art and the various configurations thereof makes it impossible to describe each and every stent structure or related materials.
  • the success of a stent placement can be assessed by evaluating a number of factors, such as thrombosis, neointimal hyperplasia, smooth muscle cell migration, and proliferation following implantation of the stent, injury to the artery wall, overall loss of lumenal patency, stent diameter in vivo, thickness of the stent, and leukocyte adhesion to the lumenal lining of stented arteries.
  • factors such as thrombosis, neointimal hyperplasia, smooth muscle cell migration, and proliferation following implantation of the stent, injury to the artery wall, overall loss of lumenal patency, stent diameter in vivo, thickness of the stent, and leukocyte adhesion to the lumenal lining of stented arteries.
  • the chief areas of concern are early subacute thrombosis and eventual restenosis of the blood vessel due to intimal hyperplasia.
  • Therapeutic pharmacological agents have been developed to address some of the concerns associated with the placement of the stent. It is often desirable to provide localized pharmacological treatment of the vessel at the site being supported by the stent. As it would be convenient to utilize the implanted stent for such purpose, the stent may serve both as a support for a lumenal wall as well as a delivery vehicle for the pharmacological agent.
  • coatings have been applied to objects such as medical devices, including stents, by processes such as dipping, spraying, vapor deposition, plasma polymerization, as wells as electroplating and electrostatic deposition. Although many of these processes have been used to produce satisfactory coatings, there are numerous potential drawbacks associated therewith.
  • FIG. 1 is a general diagram illustrative of one embodiment of an object coating system, e.g., a nanoparticle generator system using electrospray techniques for coating surfaces that includes a dual opening nozzle in accordance with the present invention.
  • an object coating system e.g., a nanoparticle generator system using electrospray techniques for coating surfaces that includes a dual opening nozzle in accordance with the present invention.
  • FIGs. 2 A, 2B and 2C are images of a capillary electrospray dispensing end (e.g., spray head) progressing from the start of spray (FIG. 2A) to the "pulsating" mode (FIG. 2B) to the “cone-jet” mode (FIG. 2C) according to the present invention.
  • a capillary electrospray dispensing end e.g., spray head
  • FIG. 2D is a graph showing a current versus voltage curve for electrospray of a particular solution.
  • FIGs. 3 A, 3B and 3C illustratively show three types of coatings that may be selected and/or applied according to the present invention including an open matrix coating in FIG. 3A, a closed film coating in FIG. 3B, and an intermediate matrix coating in FIG. 3 C.
  • FIG. 4 shows a general diagrammatical illustration of one embodiment of an electrospray dispensing device including a ring electrode for controlling particle spread as well as for illustrating control of nozzle to target surface distance for applying one or more of the types of coatings such as generally shown in FIGs. 3A-3C.
  • FIG. 5 shows a general diagrammatical illustration of one embodiment of an electrospray dispensing device including a ring electrode for controlling particle spread as well as a gas flow for use in controlling the application of one or more of the types of coatings such as generally shown in
  • FIGs. 3A-3C are identical to FIGs. 3A-3C.
  • FIG. 6 shows a general diagrammatical illustration of one embodiment of an electrospray dispensing device that includes a triple opening nozzle in accordance with the present invention, and further includes a ring electrode for controlling particle spread as well as a gas flow for use in controlling the application of one or more of the types of coatings such as generally shown in FIGs. 3A-3C.
  • FIG. 7A shows a more detailed diagram of one embodiment of a dual opening electrospray dispensing apparatus according to the present invention that may be controlled for applying one or more of the types of coatings such as generally shown in FIGs. 3A-3C.
  • FIG. 7B shows a more detailed diagram of one embodiment of a triple opening electrospray dispensing apparatus according to the present invention that may be controlled for applying one or more of the types of coatings such as generally shown in FIGs. 3A-3C.
  • FIG. 8 shows a general diagrammatical illustration of a configuration of providing multiple electrospray nozzle structures according to the present invention that may be employed in the coating system shown generally in FIG. 1.
  • FIG. 9 shows a table of experimental conditions and outcome measures to assess impact of process parameters on achieving desired coatings according to one or more examples provided herein.
  • FIGs. 10a, 10b, 10c, 1Od, 1Oe, 1Of, 1Og and 1Oh show experiment image results for the parameter sets outlined in FIG. 9 according to one or more examples provided herein.
  • FIG. 11 shows a table of the relationship of process parameters to experimental outcome variables according to one or more examples provided herein.
  • FIG. 12 shows a graph of hysteresis effect on the relationship between voltage and current through the spray target while operating the electrospray technique according to one or more examples provided herein.
  • FIG. 13 shows a table of stent and coating weights for each lot of various coating polymers and surfaces according to one or more examples provided herein.
  • FIGs. 14, 15 and 16 show graphs of coating net weights for lots of stents provided with open matrix coatings and closed film coatings according to one or more examples provided herein.
  • FIG. 17 shows a table regarding coating transfer efficiency as a function of coating polymer, surface, and solvents, according to one or more examples provided herein.
  • FIG. 18 shows a graph of a profilometer scan showing coating thickness according to one or more examples provided herein.
  • FIGs. 19a, 19b and 19c show cross-sectional images of three coatings produced according to one or more examples provided herein.
  • FIGs. 20a, 20b, 20c, 2Od, 2Oe and 2Of show SEM images of coatings according to one or more examples provided herein.
  • FIG. 21 shows a table for use in describing the images of FIGs.
  • FIG. 22 shows an FTIR Spectra of a couple of coatings according to one or more examples provided herein.
  • FIGs. 23a and 23b show images of the effect of humidity on open matrix coatings and closed film coatings according to one or more examples provided herein.
  • FIG. 24A shows a table of solutions and parameters used in the application of one or more coatings according to one or more examples provided herein
  • FIG. 24B shows respective images (higher magnification and lesser magnification) of the resulting coatings corresponding to the Sample #'s shown in the table.
  • FIG. 25 A shows a table of solutions and parameters used in the application of one or more coatings according to one or more examples provided herein
  • FIG. 25B shows respective images (higher magnification and lesser magnification) of the resulting coatings corresponding to the Sample #'s shown in the table.
  • FIG. 26A shows a table of a solution and parameters used in the application of one or more coatings according to one or more examples provided herein, and FIG. 26B shows respective images (higher magnification and lesser magnification) of the resulting coating corresponding to the Sample # shown in the table.
  • FIG. 27A shows a table of solutions and parameters used in the application of one or more coatings according to one or more examples provided herein, and FIG. 27B shows respective images (higher magnification and lesser magnification) of the resulting coatings corresponding to the Sample #'s shown in the table.
  • FIG. 28 A shows a table of solutions and parameters used in the application of one or more coatings according to one or more examples provided herein
  • FIG. 28B shows respective images (higher magnification and lesser magnification) of the resulting coatings corresponding to the Sample #'s shown in the table.
  • FIG. 29A shows a table of solutions and parameters used in the application of one or more coatings according to one or more examples provided herein
  • FIG. 29B shows respective images (higher magnification and lesser magnification) of the resulting coatings corresponding to the Sample #'s shown in the table.
  • FIG. 30A shows a table of a solution and parameters used in the application of one or more coatings according to one or more examples provided herein
  • FIG. 30B shows respective images (higher magnification and lesser magnification) of the resulting coating corresponding to the Sample # shown in the table.
  • FIG. 31 shows a table of a solution and parameters used in the application of one or more coatings according to one or more examples provided herein.
  • FIG. 32 shows respective images (higher magnification and lesser magnification) of the resulting coating corresponding to the Sample # shown in the table of FIG. 31.
  • FIG. 33 shows a table of a solution and parameters used in the application of one or more coatings according to one or more examples provided herein.
  • FIG. 34 shows respective images (higher magnification and lesser magnification) of the resulting coating corresponding to the Sample # shown in the table of FIG. 33.
  • FIGs. 35A and 35B are SEM images of a dried hydrogel with no drug coating according to an example embodiment.
  • FIGs. 36A and 36B are SEM images of a moist hydrogel with no drug coating according to an example embodiment.
  • FIGs. 37A and 37B are SEM images of a freeze-fractured hydrogel with no drug coating according to an example embodiment.
  • FIGs. 38 A and 38B are SEM images of a freeze-dried hydrogel with no drug coating according to an example embodiment.
  • FIGs. 39A and 39B are SEM images of a freeze-dried hydrogel with griseofulvin coating according to an example embodiment.
  • FIGs. 40A and 4OB are SEM images of a metal plate coated with griseofulvin according to an example embodiment.
  • FIG. 41 is an SEM image of a surface coating morphology
  • FIG. 42 is a graph illustrating hydrogel weight change under ambient conditions.
  • FIG. 43 is a graph illustrating release of dexamethasone in ⁇ g from coated hydrogel samples over a 14 day period in accordance with example embodiments.
  • FIG. 44 is a graph illustrating release of dexamethasone in ⁇ g from a coated hydrogel samples over a 14 day period in accordance with example embodiments.
  • FIGs. 45 A, 45B and 45C are block line diagrams illustrating multiple spray head electrospray devices for coating surfaces such as non- conductive surfaces.
  • FIG. 46 illustrates cumulative dexamethasone release from PLCL and TPEl, with SEM images of the respective coating types according to an example embodiment.
  • FIG. 47 illustrates cumulative dexamethasone release from TPE4 and TPE5, with SEM images of the respective coating types according to an example embodiment.
  • FIG. 48 illustrates results for a hybrid layer of TPE4 coated on a stainless steel plate according to an example embodiment.
  • Systems and methods for coating objects e.g., coated stent structures
  • medical devices e.g., medical devices
  • systems and methods for coating objects e.g., coating of medical devices, depositing a film on any object such as for texturing the surface thereof, providing a protective layer on an object, providing a textured surface to improve cellular adherence and/or biocompatibility, constructing an active or passive layer of an integrated circuit, etc.
  • Selected types of coatings having uniform properties may be accomplished.
  • the system and methods provide for the efficient and cost effective use of coating materials. Multiple embodiments are also described for obtaining timed release of drugs, and for coating both conductive and non- conductive materials using electronanospray devices.
  • An electrospray coating system such as electrospray coating system 10 illustratively shown in FIG. 1, can be controlled so as to provide for one or more selected types of coatings according to the present invention.
  • the electrospray coating system 10 may be controlled to provide an open matrix coating on one or more surface portions of an object, a closed film coating on one or more surface portions of an object, or an intermediate matrix coating on one or more surface portions of an object.
  • FIGs. 3A-3C illustratively show three types of coatings that may be selected and/or applied according to the present invention including an open matrix coating in FIG. 3A, a closed film coating in FIG. 3B, and an intermediate matrix coating in FIG. 3C.
  • Such coatings can be selected for application on one or more surface portions of an object 600. Such selection may be performed manually or automatically.
  • the selection of the type of coating to be applied may include a user determining that it is desirable to use one or more of the types of coatings to obtain one or more types of functionality provided by the coating.
  • Selection may involve a user operating a system and setting various parameters or selecting various compositions to be used in the spraying process so as to apply a particular selected coating, or may include user selection of a coating type on a system such that the system automatically selects one or more parameters or various compositions to be used in the spraying process so as to apply a particular selected coating, or a combination of both.
  • the selected coating type may be applied using two or more different types of liquid compositions (e.g., a liquid spray composition and a liquid diluent composition provided at two or more concentric openings at a dispensing end of a nozzle structure) and/or under one or more conditions or controlled parameters according to the present invention.
  • an open matrix coating may be applied to a surface of an object by controlling the type of liquid diluent composition and/or the conductivity of a composition provided at an outer opening of a dual opening nozzle structure, or by controlling the ratio of a liquid diluent composition provided at an outer opening of a dual opening nozzle structure to the liquid spray composition provided at an inner opening of a dual opening nozzle structure.
  • an open matrix coating refers to a coating wherein a supermajority (i.e., greater than two-thirds) of the particles used to create the coating are visibly discrete but attached creating a relatively irregular coating compared to a closed film coating.
  • a supermajority i.e., greater than two-thirds
  • the particles used to form the coating can be visually separated by the viewer into discrete particles even though such particles are attached, or otherwise coupled, to one or more other particles of the coating.
  • An open matrix coating 702 is illustratively shown in FIG. 3 A applied to surface 708.
  • the open matrix coating 702 includes discrete particles 704 attached, or otherwise coupled, to one or more other particles 704 of the coating 702.
  • the open matrix coating has visibly distinct open regions 707 appearing darker than the surface 706 of the coating 702 when viewed using scanning electron microscopy (SEM).
  • Such opening regions 707 extend at least one or more nominal diameters of the particles 704 deeper into the surface 706 (e.g., from the upper most surface of the outer most particles at the surface 706 of the coating 702). At least in one embodiment, such opening regions 707 exist throughout the thickness of the coating 702 as shown in FIG. 3 A. Further, particles with distinct boundaries and shape similar to those seen on the surface 706 of the coating are visible using SEM in one or more planes beneath the surface 706 of the coating.
  • the particles are substantially round particles.
  • substantially round particles refers to particles that are not elongated fiber particles; elongated fiber particles as used herein are fiber particles that have a body length that is at least ten (10) times the diameter of a maximum cross-section taken at any point along the length of the particle.
  • a substantially round particle does not have an elongated body but is more spherically shaped, although such particles will not necessarily be spherical.
  • the surface area at the upper surface 706 of the coating 702 is a rough surface that can be characterized in one or more different manners.
  • One manner of characterizing a rough surface of the open matrix coating is based on the cross-section particle size of the particles of the coating being deposited.
  • the nominal cross-section particle size is represented by the nominal diameter through the center of the particles.
  • the nominal diameter for particles of a rough open matrix coating according to the present invention is in the range of about 1 run to about 2000 nm.
  • the cross-section nominal diameter through the center of the particles is greater than about 10 nm, in another embodiment less than about 1000 nm, in another embodiment less than about 500 nanometers, and in another embodiment less than about 200 nm.
  • a rough surface may be characterized based on a comparison of the surface area of the rough surface relative to the surface area of a completely smooth surface (i.e., a surface with no structure, e.g., valleys, peaks, etc.) having a substantially identical shape as the rough surface, e.g., the shape of the structure upon which a rough portion is formed.
  • a completely smooth surface i.e., a surface with no structure, e.g., valleys, peaks, etc.
  • a rough surface is a generally homogenous surface (i.e., a surface structure without any substantial irregularities from one part of the surface to another part of the surface such as, for example, deep depressions, large spikes, unusually large particles compared to the other particles of the layer, etc.) that has a surface area greater than about 1.2 times the surface area of a completely smooth surface having a substantially identical shape (i.e., substantially identical shapes having the same base dimensional characteristics, e.g., in the case of a planar surface the occupancy area of both the completely smooth and rough surface are equivalent).
  • the surface shape may be of a planar shape, a curved shape, or any other shape.
  • the roughness of the surface has a surface area that is greater than about 1.5 times the surface area of a completely smooth surface having a substantially identical shape.
  • the rough surface 706 of coating 702 has a generally planar shape.
  • the surface area of the rough surface 706 can be compared to a surface area (XY) (only the x axis is shown with the y axis extending into the page) of a completely smooth surface 708 having a planar shape, i.e., a shape identical to the shape of the rough surface 706. Therefore, at least in one embodiment, the surface area of rough surface 706 of the coating 702 is greater than about 1.2(XY). Yet further, in another embodiment, the surface area of rough surface 706 of the coating 702 is greater than about 2.0(XY).
  • a closed film coating refers to a coating wherein a supermajority (i.e., greater than two-thirds) of the particles used to create the coating are not visibly discrete, but rather have flowed together to form a relatively smooth coating as compared to an open matrix coating.
  • a supermajority i.e., greater than two-thirds
  • the particles used to form the coating are not visually separable into discrete particles by the viewer but rather the coating is seen as a generally smooth coating with no or little irregularity.
  • a closed film coating 712 is illustratively shown in FIG. 3B.
  • the closed film coating 712 includes substantially no discrete particles, but rather the coating 712 has an upper surface 716 that is smooth and flowing.
  • the surface area of the smooth surface 716 is substantially equal to a surface area (XY) (only the x axis is shown with the y axis extending into the page) of a completely smooth surface 718 having an identical shape, or at least is less than about 1.1(XY).
  • an intermediate matrix coating refers to a coating wherein less than a supermajority (i.e., less than two-thirds) of the particles used to create the coating are visibly discrete, however, more than superminority (i.e., more than one third) of the particles are visibly discrete (e.g., in such a coating, many particles are visibly discrete with flowing material generally existing therebetween).
  • An intermediate matrix coating 722 is illustratively shown in FIG.
  • the intermediate matrix coating 722 includes some visibly discrete particles 724, and has an upper surface 726 that is slightly rough. In other words, the surface area of the slightly rough surface 726 is less rough than an open matrix coating but rougher than a closed film coating.
  • the uniformity extends through the entire thickness of a selected coating unless otherwise stated.
  • the structure of a uniform open matrix coating i.e., wherein the particles are visibly discrete but connected to one or more other particles
  • the structure of a uniform open matrix coating is substantially the same throughout the entire thickness of the coating (e.g., the particles are visibly discrete at the surface of an object being coated as well as throughout the coating including the upper rough surface of the open matrix coating).
  • an open matrix coating may be sprayed by electrospray from a cone-jet provided with one or more flows of liquid compositions (e.g., such as using a dual opening nozzle structure such as described herein, a single opening nozzle structure, etc).
  • the one or more flows include at least two active ingredients.
  • the at least two active ingredients in the one or more flows exist in a predetermined ratio.
  • the coating includes a plurality of particles adherent to one another but discrete such as described above with reference to an open matrix coating.
  • the plurality of particles have a nominal diameter of less than 500 nanometers, and may even have a nominal diameter of less than 200 nanometers.
  • Each particle of the coating includes the at least two active ingredients in substantially the same predetermined ratio as the at least two active ingredients exist in the one or more flows. As used in this context, the term substantially refers to a deviation of +/- 20%.
  • the at least two active ingredients include a polymer and biologically active material (e.g., the biologically active ingredient may be encapsulated by the polymer or they may exist in more of a matrix form. Further, the at least two active ingredients are uniformly distributed through the thickness of the coating and open regions like those described with reference to the open matrix coating are present throughout the thickness of the coating.
  • FIG. 1 One embodiment of an electrospray coating system 10 according to the present invention is shown in FIG. 1.
  • the electrospray coating system 10 employs the generation of particles, such as, for example, nanoparticles, for use in coating objects, such as medical devices (e.g., coating such devices with polymers and/or drugs, with one selected coating or more than one selected coating).
  • particles such as, for example, nanoparticles
  • coating objects such as medical devices (e.g., coating such devices with polymers and/or drugs, with one selected coating or more than one selected coating).
  • the systems and methods according to the present invention may use one or more electrospray apparatus having dual opening nozzle structures, or one or more nozzle structures that have more than two openings at the dispensing ends thereof, such as that previously described in U.S. Patent No. 6,093,557 to Pui, et al., entitled “Electrospraying Apparatus and Method for Introducing Material into Cells," issued 25 July 2000 (e.g., dual capillary configurations), and also described in the papers entitled, "Electrospraying of Conducting Liquids for Dispersed Aerosol Generation in the 4 nm to 1.8 ⁇ m Diameter Range” by Chen, et al., J. Aerosol ScL, Vol. 26, No. 6, pp.
  • the dispensing apparatus 19 employs a dispensing apparatus 19 to establish a spray of coating particles 28 (e.g., spray of microdroplets which evaporate to form a spray of coating particles).
  • the dispensing apparatus 19 includes at least one nozzle structure 18 that includes at least two concentric openings 27, 29 (e.g., concentric about axis 39) that terminate at the dispensing end 23 thereof. Openings that terminate at the dispensing end 23 do not need to terminate in a single plane (e.g., a plane orthogonal to axis 39 along which the nozzle structure 18 extends. Rather, the termination of one of the openings may be closer to the object 15 being coated than the other (e.g., the inner opening may terminate closer to the object 15).
  • the openings receive source material to establish the spray of coating particles 28 forward of the dispensing end 23, e.g., in the direction of the object 15 to be coated.
  • the coating particles 28 are moved toward at least one surface 13 of the object 15 (e.g., medical device) to form a coating 105 thereon.
  • the object 15 is located in a defined volume (shown generally by the dashed line 17) where the coating particles 28 are provided.
  • the defined volume 17 may, for example, be a reactor chamber, a chamber of a coating system, a vacuum chamber, a pressurized and/or heated chamber, a volume of open air space, a chamber including a particular gas environment, etc.
  • the system 10 includes a source holding apparatus 30 for providing a first liquid spray composition to an inner opening 27 of the two concentric openings terminating at the dispensing end 23 of the nozzle structure 18 such as under control of control mechanism 55, e.g., hardware and/or software control, via feeder/flow control 24.
  • the system 10 further includes a source holding apparatus 32 for providing a second liquid diluent composition to an outer opening 29 of the two concentric openings terminating at the dispensing end 23 of the nozzle structure 18 under control of control mechanism 55, e.g., hardware and/or software control, via feeder/flow control 25.
  • An electrospray nozzle structure 18 can deliver a controlled feed rate of source material in the establishment of a spray of coating particles within the envelope of the nozzle structure.
  • the nozzle structure 18 is configured to operate in a cone-jet mode as further described herein to provide a spray of coating particles 28 to the defined volume 17 where the object 15 is located using the source material (e.g., the first flow of liquid spray composition and the second flow of liquid diluent composition).
  • the nozzle structure 18 of the dispensing device 19 may include a nozzle structure having any one of various configurations and employing any number of different components, e.g., dual capillary electrodes, micro-machined tapered openings alone or in combination with capillary electrodes, etc.
  • the nozzle structure may include one or more nozzle structures as described in U.S. Patent No. 6,093,557 or U.S. Patent Application US-2002-0007869-A1.
  • Various types of nozzle structures, and dispensing devices with which they may be used, are shown and described herein.
  • the nozzle structure 18 of the electrospray dispensing device 19 provides a charged spray with a high concentration of charged particles.
  • concentration of charged particles in the spray is in the range of about 10 5 particles per cubic centimeter (particles/cc) to about 10 12 particles/cc. Due to the space charge effect, i.e., the effect created by the charge repulsion of charged particles, a spray of substantially dispersed particles having the same polarity charge is provided with the particles distributed substantially uniformly across a spray area.
  • substantially dispersed particles refers to uniformly and/or nonuniformly sized particles separated by an applied repulsive electrostatic force.
  • the electrospray process is a consistent and reproducible transfer process.
  • the charged particles of the spray repel one another, agglomeration of the particles is avoided. This results in a more uniform particle size.
  • “Substantially dispersed” particles are not to be confused with monodisperse particles which involves the general degree of uniformity of the particles sprayed, e.g., the standard deviation of the particles from a nominal size.
  • the charge is applied by concentration of charge on the spray of coating particles through evaporation (at least partially) in an established electrical field 43 prior to the coating particles forming a selected coating 105 on the object 15.
  • the liquid sprayed generally evaporates to concentrate a charge of a liquid portion thereof on the coating particles, e.g., on the active ingredient of the particles. This results in the spray of charged coating particles 28 as described further herein..
  • FIG. 1 generally shows a diagrammatical illustration of the operation of the electrospray coating system 10 for establishing a charged spray 28 from the nozzle structure 18.
  • the nozzle structure 18 receives a first flow of the liquid spray composition from the material source holding apparatus 30 and a second flow of the liquid diluent composition from the material source holding apparatus 32.
  • the material source holding apparatus 30 may include a liquid spray composition including drug active ingredients and a polymer at least partially dissolved in a solvent suitable to dissolve such a polymer therein.
  • the material source holding apparatus 32 may include a liquid diluent composition including the same or a different solvent as the solvent in the liquid spray composition.
  • a conductive material 47 positions the nozzle structure 18 in a particular configuration.
  • the conductive material 47 may be adapted to be connected to a high voltage source 20.
  • the nozzle structure 18 includes a conductive structure, e.g., a capillary tube structure such as illustratively shown in FIGs. 7A and 7B, which defines orifices, e.g., openings 27 and 29, that terminate at the dispensing end 23 of the nozzle structure 18 for providing the flows of the liquid compositions.
  • the source material holding apparatus 30 and 32 may be used according to the present invention, in one embodiment a single holding apparatus for each liquid composition is used to feed the respective liquid composition to the nozzle structure 18.
  • a single holding apparatus for each liquid composition is used to feed the respective liquid composition to the nozzle structure 18.
  • any number of different and separate holding apparatus may be used or hold various different compositions and provide different compositions to one or more different nozzle structures (e.g., such as when multiple nozzle structures are used).
  • the liquid spray composition and or liquid diluent composition may be pushed or pulled through the openings at the dispensing end 23 of the nozzle structure 18, e.g., pushed by a pump.
  • a compressed gas source e.g., an inert source that is non-reactive with the composition
  • a compressed gas source may be used to provide such composition flow
  • other methods of providing such flow may also be used.
  • syringe pumps for each liquid composition may be used to establish the flow of material or the flow may also be controlled with use of a liquid pump (e.g., a syringe pump, a gravity feed pump, a pressure regulated liquid reservoir, etc.), a mass flow controller, or any other flow control devices suitable for feeding source material to the nozzle structure 18 as would be known to one skilled in the art.
  • the nozzle structure 18 positioned by and electrically coupled to the conductive structure 47 functions as a first electrode of the electrospray dispensing apparatus 19 with the dispensing end 23 of the nozzle structure 18 being positioned for dispensing charged microdroplets toward the object 15, or a surface 13 thereof.
  • the object 15 may function as a second electrode structure, e.g., a grounded object 15 as shown by ground 81.
  • An electrical potential difference is applied between the first electrode conductive structure 47 and the second electrode or grounded object 15 that is electrically isolated from the first electrode.
  • the electrodes may be formed using one or more conductive elements, and such electrodes may take one of various different configurations.
  • the second electrode may also have a suitable opposite charge applied thereto (i.e., opposite to the first electrode).
  • a first flow of the liquid spray composition from the material source holding apparatus 30 and a second flow of the liquid diluent composition from the material source holding apparatus 32 is provided through the openings 27 and 29 of the nozzle structure 18, respectively.
  • a meniscus is formed at the dispensing end 23 where the inner opening 27 has an inner diameter in the range of about 6 microns to about 2 millimeters and an outer diameter in the range of about 8 microns to about 2.5 millimeters, and the outer opening 29 has an inner diameter in the range of about 15 microns to about 5 millimeters and an outer diameter in the range of about 30 microns to about 7 millimeters.
  • Such dimensions are based on estimated clearances for different sizes of stainless steel capillaries and their wall thicknesses.
  • An electrical potential difference is applied to establish the nonuniform field 43 between the first electrode at the dispensing end 23 of the nozzle structure 18 and the second electrode (e.g., the grounded object 15).
  • a high positive voltage may be applied to the first electrode conductive structure 47 with the second electrode object 15 being grounded (e.g., the second electrode may also have a suitable opposite charge applied thereto; opposite to the first electrode.
  • a voltage difference that provides an electric field intensity greater than 4 kV/cm is used in order to provide cone-jet operation of the dispensing apparatus 19.
  • nonuniform electric field refers to an electric field created by an electrical potential difference between two electrodes.
  • the nonuniform electric field includes at least some electric field lines that are more locally concentrated at one electrode relative to the other electrode, e.g., more concentrated at the dispensing end 23 relative to the second electrode or a grounded object 15.
  • at least some of the field lines are off axis relative to the longitudinal axis 39 that extends through the center of the openings 27 and 29.
  • the grounded object 15 is positioned forward of dispensing end 23 and is of a size and/or includes at least a portion that is located at a position away from the longitudinal axis 39.
  • the second electrode may also, or in the alternative, include one or more loop electrodes, plate electrodes, grounded surfaces, etc. The object 15 may still be coated even if a different electrode structure is used to produce the charged particles.
  • a loop electrode 40 as shown in FIG. 1 may be positioned forward of the dispensing end 23 to create the electric field for providing highly charged particles in the defined volume 17 in which the object 15 is positioned.
  • the highly charged particles are moved toward a grounded object 15 as the loop electrode 40, at least in one embodiment is position in proximity to the surface of the object 15 to be coated.
  • coating the object 15 using the electrospray coating system 10 shown generally in FIG. 1 may involve providing particles in a defined volume in which the object is provided, and thereafter, moving the particles toward the object forming a coating thereon, hi addition, alternatively, the particles may be formed and moved toward the object for coating thereon simultaneously with their formation.
  • the object 15 may be grounded to set up the nonuniform electric field for producing the charged particles in the defined volume in which the object 15 is provided with the same field also providing for the movement of such charged particles towards the object 15 so as to form a coating thereon.
  • the liquid spray composition includes an active ingredient
  • the liquid spray composition is flowed through the inner opening 27 of the nozzle structure 18 and the liquid diluent composition is flowed through the outer opening 29 of the nozzle structure 18.
  • the resulting blended flow of the liquid compositions at the dispensing end 23 has an electrical conductivity associated therewith.
  • the potential difference between the first and second electrodes which creates the electric field there between, strips the liquid of one polarity of charge, i.e., the negative charge is stripped when a high positive voltage is applied to the first electrode, leaving a positively charged microdroplet to be dispensed from the dispensing end 23.
  • the meniscus at the dispensing end 23 may form a cone-jet for dispensing a spray of microdroplets including the active ingredients when forces of a nonuniform field balance the surface tension of the meniscus.
  • the spray of microdroplets further becomes more positive in the nonuniform electric field.
  • the charge of the microdroplets concentrates on the active ingredients resulting in a spray of charged coating particles.
  • the amount of charge on the microdroplet, and thus the amount of charge on a particle after evaporation, is based at least upon the conductivity of the fluid composition used to spray the microdroplet, the surface tension of the fluid composition, the dielectric constant of the fluid composition, and the feed flow rate thereof.
  • the electric charge concentrated on a particular particle is greater than about 30% of a maximum charge that can be held by the microdroplets, without the microdroplet being shattered or torn apart, i.e., greater than about 30% of the Rayleigh charge limit. At least in one another embodiment, the charge is greater than 50% of the Rayleigh charge limit. At 100%, the surface tension of the microdroplet is overcome by the electric forces causing droplet disintegration. The nonuniform electric field also provides for containment of particles and/or direction for the particles which would otherwise proceed in random directions due to the space charge effect. [0095] One skilled in the art will recognize that the voltages applied may be reversed.
  • the first electrode may be grounded with a high positive voltage applied to the second electrode.
  • the particles would have a negative charge concentrated thereon.
  • any other applied voltage configuration providing a nonuniform electric field to establish the charged spray of coating particles may be used.
  • the second electrode may be any conductive material grounded (or having a suitable opposite charge applied thereto (i.e., opposite to the first electrode)) and positioned to establish the formation of a spray of coating particles 28 from the dispensing end 23 of the nozzle structure 18, e.g., the second electrode may be a grounded ring electrode, a grounded elongated element positioned in the interior volume of a stent structure, etc.
  • the second electrode may also be located at various positions, such as just forward of the nozzle structure 18, or located farther away from the nozzle structure 18 and closer to object 15.
  • the strength of the field may be adjusted by adjustment of the distance between the first and second electrodes. Different field strengths may result in relatively different areas D upon which particle spray is provided, at least in part due to the space charge effect of the spray of particles 28.
  • one or more components of the dispensing apparatus 19 may be moved relative to the others, e.g., the object 15 relative to the nozzle structure 18 or vice versa, to facilitate adjustment of field strength, and control one or more parameters according to the present invention to form a selected type of coating.
  • the object 15 and/or the dispensing apparatus 19 may be moved in any one or more different directions as represented generally by the horizontal/vertical movement arrows 101 and radial movement arrow 102 prior to, during, or after the coating process for any particular reason.
  • Such movement of the object 15 or any elements of the coating system 10 may be performed using any apparatus configured for the desired motion.
  • the present invention is not limited to any particular structure for providing such movement. Further, the present invention is not limited to movement of any elements of the coating system 10 or the object 15 during the coating process. In other words, for example, the object 15, such as a medical device, may remain in a fixed position within the defined volume 17 as the coating process is performed.
  • FIGs. 2A-2C are images of a capillary electrospray dispensing end (e.g., nozzle spray head) progressing from the start of spray (FIG. 2A) to a "pulsating" mode (FIG. 2B) to a "cone-jet” mode (FIG. 2C) according to the present invention.
  • FIG. 2B shows a magnified view of the dispensing end (e.g., capillary tip) operating in pulsating mode and the meniscus of fluid is clearly visible.
  • the dispensing end e.g., capillary tip
  • FIG. 2C shows a graph indicating the current versus voltage curve for electrospray of a particular solution. Note that a particular voltage is needed for the nozzle to operate in cone-jet mode and that such a voltage may need adjustment to maintain a stable cone-jet mode.
  • a stable cone-jet mode of operation is of importance when applying a uniform selected type of coating to an object such as described herein.
  • a stable cone-jet refers to a cone-jet that does not flutter between a cone-jet mode and a non-cone-jet mode (e.g., pulsating mode). Further, such a stable cone-jet may exhibit a dark tip appearance with no corona discharge being present.
  • a cone-jet 100 is formed at the dispensing end 23 of the nozzle structure 18.
  • the cone-jet 100 extends from the dispensing end 23 to a point or tip 109, that, at least in one embodiment, lies on axis 39.
  • An angle 104 is formed between the cone-jet 100 and a plane 106 lying orthogonal to axis 39 at the tip 109. When the angle 104 decreases such that it looks more like the meniscus of FIG. 2B, the cone-jet is more likely to move into a pulsating mode of operation.
  • a stable cone-jet can be achieved according to the present invention as further described herein.
  • coating refers to forming a layer or structure on a surface.
  • the coated layer or structure formed on the surface may be a coating that adheres to an underlying layer or the surface 13, or a coating that does not adhere to the surface or an underlying layer. Any level of adherence to the surface 13 or an underlying layer is contemplated according to the present invention.
  • a coating formed on surface 13 of the object 15 may be formed as a sheath about a structure (e.g., a stent structure) without necessarily having adhesion between the layer and the structure.
  • an adhesion layer may be deposited on an object 15 prior to forming a coating on the object 15 such that greater adhesion is accomplished.
  • the adhesion layer may also be coated on the surface 13 of the object 15 employing methods and/or systems according to the present invention.
  • Various embodiments of the coating methods and systems described are suitable to allow one or more objects to be coated as a batch.
  • the present invention is not limited to only coating objects such as medical devices in batches, i.e., coating a group of one or more devices in one batch process followed by coating a second group of one or more devices in a second batch process.
  • the methods and systems of the present invention can be utilized to continuously run objects through the systems such that the process does not have to be started and stopped for coating the objects in batches. In other words, a plurality of objects such as medical devices can be coated through a continuous process.
  • a coating sprayed may include multiple materials, different nozzle structures may be provided with different source materials for controlling and spraying different coating materials, different nozzle structures may be controlled for use during different time periods so as to provide different layers of coating materials on at least a portion of the object, multiple layers may be sprayed using the same or different source materials (e.g., forming a somewhat laminated coating), the entire object or just a portion of the object may be coated (e.g., a charge could be applied to a portion of the surface to attract all of or a majority of the sprayed particles to the charged portion), different portions of the object may be sprayed with a thicker coating than the remainder of the object, and/or masking materials may be used to mask certain portions of the object from having coating applied thereto.
  • source materials e.g., forming a somewhat laminated coating
  • the entire object or just a portion of the object may be coated (e.g., a charge could be applied to a portion of the surface to attract all of or a majority of the
  • the present invention contemplates applying one layer or multiple layers of the same or different types of coating (e.g., an open matrix coating, a closed film coating, and an intermediate matrix coating, in any combination). Such layers may perform identical or different functions (e.g., to provide for biocompatibility, to control drug release, etc.). Further, the one or more layers may be applied to conductive or non-conductive surfaces.
  • the object 15 may be a medical device amenable to the coating processes described herein.
  • the medical device, or portion of the medical device, to be coated or surface modified may be made of metal, polymers, ceramics, composites or combinations thereof, and for example, may be coated with one or more of these materials. For example, glass, plastic or ceramic surfaces may be coated.
  • the present invention may be used to form a coating on surfaces of other objects as well, e.g., metal substrates or any other surfaces that may be rendered conductive (e.g., whether flat, curved, or of any other shape).
  • the coatings described herein may be used to coat a vascular stent
  • other medical devices within the scope of the present invention include any medical devices such as those, for example, which are used, at least in part, to penetrate and/or be positioned within the body of a patient, such as, but clearly not limited to, those devices that are implanted within the body of a patient by surgical procedures.
  • Examples of such medical devices include implantable devices such as catheters, needle injection catheters, blood clot filters, vascular grafts, stent grafts, biliary stents, colonic stents, bronchial/pulmonary stents, esophageal stents, ureteral stents, aneurysm filling coils and other coiled devices, reconstructive implants, trans myocardial revascularization (“TMR”) devices, percutaneous myocardial revascularization (“PMR”) devices, lead wires, implantable spheres, pumps, dental implants, etc., as are known in the art, as well as devices such as hypodermic needles, soft tissue clips, holding devices, and other types of medically useful needles and closures. Any exposed surface of these medical devices may be coated with the methods and systems of the present invention.
  • implantable devices such as catheters, needle injection catheters, blood clot filters, vascular grafts, stent grafts, bili
  • the source material held in the source holding apparatus 30 may be any source of material (e.g., such as coating materials described herein including solvents and active ingredients) which can be provided in the defined volume in particle form as described according to the present invention.
  • the source material in source holding apparatus 30 is a liquid spray composition that may include a solution, a suspension, a microsuspension, an emulsion, a microemulsion, a gel, a hydrosol, or any other liquid compositions that when provided according to the present invention results in the generation of particles.
  • the liquid spray composition may include at least one of a biologically active ingredient, a polymer, and a solvent (e.g., a solvent suitable to at least partially dissolve the polymer).
  • a solvent e.g., a solvent suitable to at least partially dissolve the polymer.
  • such liquid spray compositions may include a biologically active ingredient, a polymer, and a solvent suitable to at least partially dissolve the polymer.
  • an active ingredient refers to any component that provides a useful function when provided in particle form, particularly when provided as nanoparticles.
  • the present invention is particularly beneficial for spraying nanoparticles and also is particularly beneficial for spraying particles including biologically active ingredients.
  • active ingredient refers to material which is compatible with and has an effect on the substrate or body with which it is used, such as, for example, drug active ingredients, chemical elements for forming nanostructures, materials for modifying local cell adherence to a device, materials for modifying tissue response to a device surface, materials for modifying systemic response to a device, materials for improving biocompatibility, and elements for film coatings, e.g., polymers, excipients, etc.
  • biologically active ingredient or “biologically active material or component” is a subset of active ingredient and refers to material which is compatible with and has an effect (which may, for example, be biological, chemical, or biochemical) on the animal or plant with which it is used and includes, for example, medicants such as medicines, pharmaceutical medicines, and veterinary medicines, vaccines, genetic materials such as polynucleic acids, cellular components, and other therapeutic agents and drugs, such as those described herein.
  • the term particle, and as such nanoparticle includes solid, partially solid, and gel-like droplets and microcapsules which incorporate solid, partially solid, gel-like or liquid matter.
  • Particles provided and employed herein may have a nominal diameter as large as 10 micrometers.
  • nanoparticle refers to a particle having a nominal diameter of less than 2000 nm.
  • the present invention is particularly beneficial in spraying nanoparticles having a nominal diameter greater than 1 nanometer (nm), particles having a nominal diameter less than 1000 nm, particles having a nominal diameter of less than 500 nm, particles having a nominal diameter of less than 200 nm, and particles having a nominal diameter of less than 100 nm.
  • the particles used for coating as described herein are, in at least one embodiment, monodisperse coating particles.
  • monodisperse coating particles are coating particles that have a geometrical standard deviation of less than 1.2.
  • the standard deviation with respect to mean particle size of particles provided according to the present invention is, at least in one embodiment, less than or equal to 20%.
  • the coating materials used in conjunction with the present invention are any desired, suitable substances such as defined above with regard to active ingredients and biologically active ingredients, hi some embodiments, the coating materials comprise therapeutic agents, applied to medical devices alone or in combination with solvents in which the therapeutic agents are at least partially soluble or dispersible or emulsified, and/or in combination with polymeric materials as solutions, dispersions, suspensions, lattices, etc.
  • therapeutic agents and “drugs”, which fall within the biologically active ingredients classification described herein, are used interchangeably and include pharmaceutically active compounds, nucleic acids with and without carrier vectors such as lipids, compacting agents (such as histones), virus, polymers, proteins, and the like, with or without targeting sequences.
  • the coating on the medical devices may provide for controlled release, which includes long-term or sustained release, of a bioactive material.
  • therapeutic or biologically active ingredients used in conjunction with the present invention include, for example, pharmaceutically active compounds, proteins, oligonucleotides, ribozymes, anti- sense genes, DNA compacting agents, gene/vector systems (i.e., anything that allows for the uptake and expression of nucleic acids), nucleic acids (including, for example, recombinant nucleic acids; naked DNA, cDNA, RNA; genomic DNA, cDNA or RNA in a non-infectious vector or in a viral vector which may have attached peptide targeting sequences; antisense nucleic acid (RNA or DNA); and DNA chimeras which include gene sequences and encoding for ferry proteins such as membrane translocating sequences ("MTS") and herpes simplex virus- 1 ("VP22”)), and viral, liposomes and cationic polymers that are selected from a number of types depending on the desired application.
  • nucleic acids including, for example, recombinant nucleic acids; naked DNA, cDNA, RNA
  • biologically active solutes include anti-thrombogenic agents such as heparin, heparin derivatives, urokinase, and PPACK (dextrophenylalanine proline arginine chloromethylketone); prostaglandins, prostacyclins/prostacyclin analogs; antioxidants such as probucol and retinoic acid; angiogenic and anti- angiogenic agents; agents blocking smooth muscle cell proliferation such as rapamycin, sirolimus, everolimus, tacrolimus, pimecrolimus, angiopeptin, and monoclonal antibodies capable of blocking smooth muscle cell proliferation; anti-inflammatory agents such as dexamethasone, prednisolone, corticosterone, budesonide, estrogen, sulfasalazine, acetyl salicylic acid, and mesalamine, chemokine antagonists, chemokine receptor antagonists, inhibitors of tissue- necrosis factor and nuclear factor-kB and other
  • coating materials and/or additional coating materials for use in coating a medical device according to the present invention are contemplated herein as would be apparent to one skilled in the art.
  • coating materials may be provided in derivatized form or as salts of compounds.
  • Polynucleotide sequences useful in practice of the invention include DNA or RNA sequences having a therapeutic effect after being taken up by a cell.
  • therapeutic polynucleotides include anti-sense DNA and RNA; DNA coding for an anti-sense RNA; or DNA coding for tRNA or rRNA to replace defective or deficient endogenous molecules.
  • the polynucleotides of the invention can also code for therapeutic proteins or polypeptides.
  • a polypeptide is understood to be any translation product of a polynucleotide regardless of size, and whether glycosylated or not.
  • Therapeutic proteins and polypeptides include, as a primary example, those proteins or polypeptides that can compensate for defective or deficient species in an animal, or those that act through toxic effects to limit or remove harmful cells from the body.
  • the polypeptides or proteins that can be incorporated into the polymer coating, or whose DNA can be incorporated include without limitation, angiogenic factors and other molecules competent to induce angiogenesis, including acidic and basic fibroblast growth factors, vascular endothelial growth factor, hif-1, epidermal growth factor, transforming growth factor ⁇ and ⁇ , platelet-derived endothelial growth factor, platelet-derived growth factor, tumor necrosis factor ⁇ , hepatocyte growth factor and insulin like growth factor; growth factors; cell cycle inhibitors including CDK inhibitors; anti-restenosis agents, including pl5, pl6, pl8, pl9, p21, p27, p53, p57, Rb, nFkB and E2F decoys, thymidine kina
  • MCP-I monocyte chemoattractant protein
  • BMP's the family of bone morphogenic proteins
  • the known proteins include BMP-2, BMP-3, BMP-4, BMP-5, BMP-6 (Vgr-1), BMP-7 (OP-I), BMP-8, BMP-9, BMP-IO, BMP-I l, BMP-12, BMP-13, BMP-14, BMP-15, and BMP-16.
  • BMP's are any of BMP-2, BMP-3, BMP-4, BMP-5, BMP-6 and BMP- 7.
  • dimeric proteins can be provided as homodimers, heterodimers, or combinations thereof, alone or together with other molecules.
  • molecules capable of inducing an upstream or downstream effect of a BMP can be provided.
  • Such molecules include any of the "hedgehog" proteins, or the DNA' s encoding them.
  • Coating materials other than therapeutic agents include, for example, polymeric materials, sugars, waxes, and fats, applied alone or in combination with therapeutic agents, and monomers that are cross-linked or polymerized. Such coating materials are applied in the form of, for example, powders, solutions, dispersions, suspensions, and/or emulsions of one or more polymers, optionally in aqueous and/or organic solvents and combinations thereof or optionally as liquid melts including no solvents. [00123] When used with therapeutic agents, the polymeric materials are optionally applied simultaneously with, or in sequence to (either before or after), the therapeutic agents.
  • Such polymeric materials employed as, for example, primer layers for enhancing subsequent coating applications e.g., application of alkanethiols or sulfhydryl-group containing coating solutions to gold-plated devices to enhance adhesion of subsequent layers
  • layers to control the release of therapeutic agents e.g., barrier diffusion polymers to sustain the release of therapeutic agents, such as hydrophobic polymers; thermal responsive polymers; pH -responsive polymers such as cellulose acetate phthalate or acrylate-based polymers, hydroxypropyl methylcellulose phthalate, and polyvinyl acetate phthalate
  • protective layers for underlying drug layers e.g., impermeable sealant polymers such as ethylcellulose
  • biodegradable layers e.g., layers comprising albumin or heparin as blood compatible biopolymers, with or without other hydrophilic biocompatible materials of synthetic or natural origin such as dextrans, cyclodextrins, polyethylene oxide, and polyvinyl pyrroli
  • the polymer component of the coatings may include any material capable of absorbing, adsorbing, entrapping, or otherwise holding the therapeutic agent to be delivered.
  • the material is, for example, hydrophilic, hydrophobic, and/or biodegradable, and is preferably selected from the group consisting of polycarboxylic acids, cellulosic polymers, gelatin, polyvinylpyrrolidone, maleic anhydride polymers, polyamides, polyvinyl alcohols, polyethylene oxides, glycosaminoglycans, polysaccharides, polyesters, polyurethanes, silicones, polyurea, polyacrylate, polyacrylic acid and copolymers, polyorthoesters, polyanhydrides such as maleic anhydride, polycarbonates, polyethylene, polypropylenes, polylatic acids, polystyrene, natural and synthetic rubbers and elastomers such as polyisobutylene (PIB),
  • PIB polyisobutylene
  • Coatings from polymer dispersions such as polyurethane dispersions (BAYHYDROL, etc.) and acrylic latex dispersions are also within the scope of the present invention.
  • Preferred polymers include polyurethanes; polyacrylic acid as described in U.S. Pat. No. 5,091,205; and aqueous coating compositions comprising an aqueous dispersion or emulsion of a polymer having organic acid functional groups and a poly-functional crosslinking agent having functional groups capable of reacting with organic acid groups, as described in U.S. Pat. No. 5,702,754.
  • polymers that may be used include poly(DL- lactide-co- ⁇ -caprolactone, 80/20) (PLCL), Chronoflex AR (CFR) which is polyurethane 22% solid in dimethylacetamide, and poly(tetrahydrofurfuryl methacrylate-co-ethyl methacrylate) PTHFMA-EM, poly-ethylene-co-vinyl acetate (PEVA), and poly-n-butyl methacrylate (PNBA).
  • polar solvents e.g., acetone and methanol
  • non-polar solvents e.g., chloroform and toluene.
  • Polar solvents are liquids that tend to have higher dielectric constants, where the higher the dielectric constant, the greater the relative polarity.
  • Such polar solvents may include, for example, but are not limited to, water, methanol, ethanol, isopropanol, acetonitrile, acetone, and tetrahydrofuran.
  • Non-polar solvents are liquids that tend to have lower dielectric constants than polar solvents, where the lower the dielectric constant, the lower the relative polarity.
  • Such non-polar solvents may include, for example, but are clearly not limited to, toluene, chloroform, hexane, and dichloromethane.
  • high dielectric constant solvents may be used.
  • Such high dielectric constant solvents include solvents having a dielectric constant equal to or greater than 10.
  • high dielectric constant solvents include water (dielectric constant of 80), methanol (dielectric constant of 33), ethanol (dielectric constant of 24), or acetone (dielectric constant of 21).
  • low dielectric constant solvents may be used.
  • Such low dielectric constant solvents include solvents having a dielectric constant less than 10.
  • low dielectric constant solvents include tetrahydrofuran (dielectric constant of 7.5), chloroform (dielectric constant of 4.8), or toluene (dielectric constant of 2.4).
  • the release rate of drugs from drug matrix layers is largely controlled, for example, by variations in the polymer structure and formulation, the diffusion coefficient of the matrix, the solvent composition, the ratio of drug to polymer, potential chemical reactions and interactions between drug and polymer, the thickness of the drug adhesion layers and any barrier layers, and the process parameters, e.g., drying, etc.
  • the coating(s) applied by the methods and apparatuses of the present invention may allow for a controlled release rate of a coating substance with the controlled release rate including both long-term and/or sustained release.
  • the source material held in the source holding apparatus 32 may be any liquid diluent composition which when provided in combination with the liquid spray composition at the dispensing end 23 of the nozzle structure results in coating particles being provided in the defined volume in particle form as described according to the present invention herein.
  • the source material in source holding apparatus 32 is a liquid diluent composition that includes at least one of a polar or non-polar solvent as described herein.
  • the liquid diluent composition includes one or more high dielectric constant solvents.
  • the liquid diluent composition has a high dielectric constant (i.e., a dielectric constant that is equal to or greater than 10).
  • the liquid diluent composition may include a high dielectric constant solvent and include a low dielectric constant solvent (e.g., mixed solvents), yet still the liquid diluent composition may have a high dielectric constant.
  • the liquid diluent composition may further include an active ingredient, such as a polymer or a drug.
  • the liquid diluent composition is a high dielectric constant composition and includes a biologically active ingredient (i.e., without a polymer).
  • the liquid diluent composition has a weight concentration of active ingredient that is less than 1 percent of the total weight concentration of the liquid diluent composition (e.g., a biologically active ingredient that is less than 1 percent of total weight concentration).
  • the liquid diluent composition has a weight concentration of active ingredient that is less than 0.5 percent of the total weight concentration of the liquid diluent composition.
  • the liquid diluent composition may further include an additive that is used to control conductivity of the liquid diluent composition.
  • the additive used to control conductivity may include a buffer solution such as a phosphate buffer (e.g., for spraying particles including peptides), an acid such as nitric acid, or a salt such as ammonium chloride.
  • a buffer solution such as a phosphate buffer (e.g., for spraying particles including peptides)
  • an acid such as nitric acid
  • a salt such as ammonium chloride.
  • an additive to increase the conductivity of the liquid diluent composition is needed to apply an open matrix coating.
  • the liquid diluent composition includes only solvents and has a high dielectric constant (e.g., includes at least one high dielectric constant solvent. With use of only solvents in the liquid diluent composition, fouling of the spray tip is less likely.
  • the coatings of the present invention are applied such that they result in a suitable thickness, depending on the coating material and the purpose for which the coating or coatings are applied. For example, coatings applied for localized drug delivery are typically applied to a thickness of at least about 1 micron and not greater than 30 microns. In one embodiment, the thickness is greater than 2 microns. Further, in another embodiment, the thickness is not greater than 20 microns. In addition, very thin coatings such as those as thin as 100 Angstroms may be provided. Much thicker coatings of more than 30 microns are also possible.
  • FIG. 7A is a more detailed diagram of one configuration of a portion 300 of an electrospraying apparatus such as shown generally in FIG. 1 including a dual concentric opening dispensing device 314 extending along axis 301 according to the present invention from a first end 304 to a second end or dispensing end 380.
  • First end 304 may be formed of conductive portions to facilitate application of voltages or ground to capillary tube 320.
  • the first end 304 includes a distributor head 316 that is coincident with axis 301 for use in establishing the spray of particles.
  • the distributor head 316 includes capillary tube 320 having an axis therethrough coincident with axis 301.
  • the capillary tube 320 includes a first end 330 sealingly positioned in aperture 385 of the first end 304 by conductive sealing element 337 at the upper surface 383 of the first end 304.
  • the capillary tube 320 further includes a second end 332 positioned for providing a liquid spray composition to the dispensing end 380 (i.e., through an inner opening 391 that terminates at the dispensing end 380 for use in generating the spray of particles as desired).
  • the capillary tube 320 may be made of any suitable material, such as, for example, platinum, silica, stainless steel, etc. and may be of any suitable size.
  • the capillary tube may, at least in one embodiment, have an outer diameter in the range of about 8 ⁇ m to about 2.5 mm, and an inner diameter in the range of about 6 ⁇ m to about 2 mm. Further, in another embodiment, the inner diameter of the capillary tube is in the range of about 10 ⁇ m to about 200 ⁇ m.
  • the distributor head 316 includes a nozzle portion or casing 322 which as illustrated in FIG. 7A is an elongate substantially cylindrical metal casing concentric with the capillary tube 320 for providing an outer opening 392 concentric with inner opening 390 for providing liquid diluent compositions to the dispensing end 380.
  • the casing 322 can be conductive or nonconductive.
  • the capillary tube 320 and the casing 322 form the dual opening capillary tube electrode of the distributor head 316 for use in providing the spray of particles when operating in a cone-jet mode.
  • the casing or nozzle portion 322 includes a first end portion 336 which tapers at section 335 thereof to a narrower second end portion 338.
  • the second end portion 338 extends from the tapered section 335 and is concentric with the second end 332 of the capillary tube 320.
  • the narrow end of the tapered section 335 extends a distance of about 5 mm to about 5 cm from the lower surface 385 of the first end 304.
  • the outer diameter of the second end portion 338 is in the range of about 2 mm to about 5 mm and the inner diameter of the second end portion 338 is in the range of about 0.1 cm to about 0.2 cm.
  • the second end 332 of the capillary tube 320 extends beyond the second end portion of the metal casing or nozzle portion 322 towards the target surface to be coated by a distance of about 2 mm to about 5 mm.
  • the nozzle portion 322 is formed of any suitable metal or nonconductive material such as stainless steel, brass, alumina, or any other suitable material.
  • the nozzle portion 322 is spaced from the capillary tube 320 by spacers 326 or other spacing structures.
  • a metal casing 322 may be deformed at particular portions, such as pin points or depressions, to create a neck for centering the capillary tube 320 therein.
  • An inlet 348 is configured for directing the liquid diluent composition 349 in aperture or opening 392 between the concentric capillary tube 320 and the nozzle portion 322.
  • the capillary tube electrode may take one of many configurations.
  • a gas inlet 354 is provided in the first end 304 to allow for input of a stream of electro-negative gases, e.g., CO 2 , SF 6 , etc., to form a gas sheath about the capillary tube 320 or flood the region about dispensing end 380.
  • This gas sheath allows the applied voltage to be raised to higher levels without corona discharge, e.g., the electrostatic breakdown voltage for the capillary tube electrode is increased.
  • the entire portion of end 304 or portions thereof may be formed of conductive materials to facilitate application of a voltage or ground to the capillary tube electrode.
  • sealing elements 337 may be nonconductive, but in one embodiment are conductive to facilitate application of a voltage or ground to capillary rube 320.
  • the region around the capillary tube 320 and the nozzle portion 322 is flooded with a gas through the port 354 to increase the electrostatic breakdown voltage for the capillary tube electrode.
  • a chamber in which the coating process is being completed is flooded with the gas through the port 354 and then a flow in the range of about 5 cc/min to about 200 cc/min is continued through the port 354.
  • a first flow of a liquid spray composition is received in the first end 330 of the capillary tube 320 and flows through opening 391.
  • the flow rate of the liquid spray composition may be greater than about 0.01 ⁇ l/min or less than about 10 ⁇ l/min; or further may be less than about 5 ⁇ l/min, or even less than about 3 ⁇ l/min.
  • a second flow of a liquid diluent composition 349 is received in the port 348 of the nozzle and provided to opening 392.
  • the flow rate of the liquid diluent composition may be greater than about 0.01 ⁇ l/min or less than about 10 ⁇ l/min; or further may be less than about 5 ⁇ l/min.
  • a relatively high voltage for example, in the range of about 2000 volts to about 6000 volts, may be applied between the object being coated and the capillary tube 320 to establish the potential difference between the first and second electrode of the spraying apparatus and cause operation in cone-jet mode.
  • capillary tube 320, metal casing 322, and sealing element 337 are conductive.
  • Spray 328 is established forward of the dispensing tip 380 of the second end 332 of the capillary tube 320 per a mode of operation as previously described.
  • the potential difference between the electrodes establishes an electric field there between, causing operation in a cone-jet mode for generation of coating particles according to the present invention.
  • the electrospray coating system 10 illustrated and described generally herein with reference to FIG. 1 can be controlled to provide for particular types of selected coatings according to the present invention.
  • one or more different parameters of the system 10 may be controlled so as to form an open matrix coating as opposed to a closed film coating.
  • the coating process using one or more controlled parameters as described herein allows for applying nanocomposite coatings onto objects such as coronary stents and/or other medical devices.
  • the cone-jet mode of operation produces highly charged, uniform, monodisperse nanoparticles comprised of one or more components that are used to coat the object.
  • Non-line-of-sight coating can be achieved (i.e., coating of surfaces not directly in the line of sight of the dispensing end 23, such as the interior surface of a stent).
  • the coating particles in such non-line-of-sight coating are directed to the surface of the object being coated by the established electrical field, which aids in the uniform coating of objects with intricate architecture.
  • Use of the dual opening nozzle structure e.g., a dual-capillary spray head
  • the electrospray process can accommodate a range of polymers and solvents that are used or likely to be used in coating objects such as stents.
  • solvents required to dissolve a polymer e.g., poly(isobutylene), poly(styrene-b-isobutylene-b-styrene, etc.
  • a polymer e.g., poly(isobutylene), poly(styrene-b-isobutylene-b-styrene, etc.
  • low dielectric constant non-polar solvents e.g., toluene
  • low dielectric constant polar solvents tetrahydrofuran
  • a liquid spray composition that includes such a hard to spray dissolved polymer can be used to coat an object.
  • control parameters may be useful in selecting a type of coating to be formed on the object 15.
  • control parameters which shall be discussed in further detail herein include controlling a flow rate of the second flow of the liquid diluent composition in the outer opening 29 relative to a flow rate of the first flow of the liquid spray composition in the inner opening 27 (e.g., controlling the ratio of the flow of the liquid diluent composition to the total flow of the liquid spray composition and liquid diluent composition dispensed at the dispensing end 23), selecting a particular liquid diluent composition to be provided in the outer opening 29 (e.g., selecting a particular liquid diluent composition having a particular conductivity); and controlling the evaporation process of the microdroplets dispensed from the dispensing end 23 of the nozzle structure 18.
  • the relative flow rate of the second flow of the liquid diluent composition in the outer opening 29 to the flow rate of the first flow of the liquid spray composition in inner opening 27 can be selected to achieve a desired coating described herein. For example, selection of a higher ratio of flow rate for the liquid diluent composition relative to the total flow rate of the liquid spray composition and liquid diluent composition dispensed at the dispensing end 23, may result in the formation of a closed film coating. [00149] As would be recognized, the ratio necessary to achieve a desired selected coating may depend on the compositions being used.
  • a closed film coating occurs.
  • a closed film coating is achieved.
  • a user with the desired compositions known can adjust the flow rates to achieve a selected type of coating by controlling the flow rate of the second flow of the liquid diluent composition in the outer opening 29 relative to the flow rate of the first flow of the liquid spray composition in inner opening 27.
  • Selecting a particular liquid diluent composition to be provided in the outer opening 29 can also be used to achieve a desired coating described herein.
  • selecting a liquid diluent composition that includes one or more high dielectric constant solvents e.g., such as a liquid diluent composition that includes at least one of acetone or methanol (both higher dielectric constant solvents) such that the liquid diluent composition has a high dielectric constant is likely to result in an open matrix coating.
  • liquid diluent composition that includes one or more low dielectric constant solvents (e.g., such as a liquid diluent composition that includes at least one of chloroform, toluene, or tetrahydrofuran (all low dielectric constant solvents)) such that the liquid diluent composition has a low dielectric constant is likely to result in a closed film coating.
  • low dielectric constant solvents e.g., such as a liquid diluent composition that includes at least one of chloroform, toluene, or tetrahydrofuran (all low dielectric constant solvents)
  • selecting a liquid diluent composition for the outer opening that has a certain dielectric constant can be used to achieve a particular selected coating.
  • liquid diluent compositions that have a high dielectric constant i.e., greater than 10. are typically required to obtain an open matrix coating.
  • selecting a particular high dielectric constant solvent for use in the liquid spray composition to be provided in the inner opening 27 may also be used to achieve a desired coating described herein.
  • selecting a solvent for use in the liquid spray composition that includes one or more high dielectric constant solvents may be beneficial in providing an open matrix coating.
  • such a high dielectric constant solvent may be added to a low dielectric constant solvent that is required to dissolve a particular polymer to provide the ability to apply an open matrix coating (e.g., making the dielectric constant of the liquid spray composition higher).
  • increasing the conductivity of the second flow of the liquid diluent composition is useful for achieving an open matrix coating on the at least one surface of the object 15.
  • Such conductivity may be achieved by selecting, at least in one embodiment, a liquid diluent composition that has a conductivity greater than l ⁇ S cm "1 (microSiemen/cm).
  • a liquid diluent composition that has a conductivity greater than 6.8 ⁇ S cm "1 is beneficial in forming an open matrix coating.
  • liquid diluent composition that has a conductivity greater than l ⁇ S cm “1 , or even greater than 6.8 ⁇ S cm “1 , provides for substantially round particles being formed in the open matrix coating. Such substantially round particles are shown in FIG. 10c,d,g,h, as opposed to elongated fiber particles shown in FIGs. 1 Oa,b,e,f. The substantially round particles are a direct result of using a high conductivity liquid diluent composition in the outer opening.
  • the conductivity of the liquid diluent composition can be manipulated using any known techniques.
  • the liquid diluent composition may include a single component having a relatively high conductivity or a relatively high conductivity component may be added to a relatively low conductivity component.
  • an acid e.g., nitric acid
  • a salt e.g., ammonium chloride
  • solvents e.g., acetone, methanol, or water
  • a lower conductivity liquid spray composition is provided at the inner opening 27.
  • the conductivity of the liquid spray composition e.g., including de-ionized water and toluene
  • the conductivity of the liquid spray composition may be in the range of about 0.3 ⁇ S cm “1 to about 1.0 ⁇ S cm “1
  • a liquid diluent composition e.g., such as that including nitric acid
  • having a conductivity in the range of about 100 ⁇ S cm "1 to about 1000 ⁇ S cm "1 may be necessary to facilitate breakup of the inner stream of liquid spray composition so as to spray the coating particles.
  • the liquid spray composition includes at least a biologically active material and a polymer.
  • the ratio of weight concentrations of polymer to biologically active material may be as high as 10:1 or as low as 5:1. However, even lower ratios may be sprayed.
  • the weight concentration of the active ingredient e.g., the polymer or the polymer and biologically active ingredient
  • the weight concentration of the active ingredient may be less than 5 percent of the total weight of the liquid spray composition, and may be less than 1 percent of the total weight concentration of the liquid spray concentration.
  • the evaporation process of the microdroplets dispensed from the dispensing end 23 of the nozzle structure 18 may be controlled to achieve a particular selected coating.
  • the time allowed for evaporation of the microdroplets may be controlled as a function of selected type of coating to be applied.
  • the time allowed for evaporation of the microdroplets before they reach the object 15 to form a coating thereon is increased so that an open matrix coating can be formed.
  • a dual opening nozzle structure 120 is shown that has a dispensing end 122.
  • the distance between the dispensing end 122 of the nozzle structure 120 and the surface 13 of the object 15 to be coated is controlled depending on the selected type of coating to be applied.
  • the distance d between the dispensing end 122 of the nozzle structure 120 and the surface 13 of the object 15 may be increased upon selection of an open matrix coating to allow more time of flight for evaporation of the microdroplets or decreased upon selection of a closed film coating to allow less time for evaporation.
  • either the nozzle structure 120 or the object 15 may be moved to adjust the distance d.
  • the coating system 10 is configured such that prior to contact with the at least one surface 13 of the object 15, the weight percent of solvent in the evaporated microdroplet is less than 85% (e.g., corresponding to a weight percent of 15% polymer in a droplet that only includes only polymer solids and the solvent). At least in one embodiment, some solvent component forms a part of the particle volume as the particle contacts the surface 13 of the object 15. With some solvent component being a part of the residual particle volume occupied by the evaporated microdroplet, adhesion of the microdroplet (including the particle) to the surface 13 of the object 15 may be enhanced. After the microdroplet has contacted the surface 13 of the object 15, the remainder portion of the solvent evaporates, leaving the particle coated on the surface 13 of the object 15.
  • an open matrix coating is facilitated by solvent evaporation such that the residual solvent immediately prior to contact with the at least one surface 13 of the object 15 is less than 85% by weight of the evaporated microdroplet.
  • the relative composition of solvent :polymer in the particle that promotes open matrix formation may be different depending on the polymer used.
  • an open matrix coating would be facilitated by solvent evaporation such that the residual solvent prior to contact with the at least one surface 13 of the object 15 is less than 80% by weight of the evaporated microdroplet.
  • a closed film coating would be facilitated by solvent evaporation such that the residual solvent immediately prior to contact with the at least one surface 13 of the object 15 is more than 90 % by weight of the evaporated microdroplet.
  • solvent evaporation the relative percentages of solvent and polymer that are given may vary according to the characteristics of the specific polymer that is used.
  • the amount of evaporation prior to the microdroplet/particle contacting the surface 13 of the object 15 may be controlled in a number of different ways for applying one or more different selected types of coatings, in addition to selecting a distance d as shown in FIG. 4.
  • the evaporation may be controlled by the type of solvent used, the temperature and pressure of a chamber in which the medical device is provided, the size of the microdroplet, the humidity, etc.
  • maintaining a temperature in the defined volume in the range of 20 degrees centigrade to 30 degrees centigrade may be necessary upon selection of an open matrix coating. The temperature typically should not exceed the glass transition temperature for a given polymer.
  • maintaining humidity in the defined volume 17 to less than 20 percent RH assists in maintaining stability of the coating process. Controlling relative humidity prevents arcing or corona discharge. If the relative humidity is kept lower, higher voltages can be used before corona discharge becomes a problem, facilitating the cone-jet formation and maintenance.
  • evaporation may also be controlled by providing a gas stream 130 in proximity to the cone-jet formed at the dispensing end 134 of a nozzle structure 132.
  • a gas For example, one or more gases such as nitrogen or carbon dioxide may be used to increase evaporation. As such, with increased evaporation, achieving an open matrix coating is more likely.
  • providing the gas stream may assist in keeping the cone-jet stable (e.g., provide anti-fouling of the dispensing end 23). Still further, the gas stream should not generate turbulence around the cone jet, as this could cause instability thereof.
  • the nonuniform electric field provides for containment of particles and/or direction for the particles which would otherwise proceed in random directions due to the space charge effect; the space charge effect being necessary to provision of monodisperse and nonconglomerated particles.
  • the space charge effect is generally dependent upon the size of the particles and the charge thereon.
  • the loop electrode 40 as shown in FIG. 4 can also be used to prevent scattering and decrease the amount of coating material necessary to coat the object 15.
  • the loop electrode 40 can be used to establish the nonuniform electric field when positioned along a plane generally orthogonal to an axis 128 along which the nozzle structure 120 extends.
  • the position, size and shape of the loop can be used to control the direction of the coating particles so as to coat the desired surfaces of the object 15.
  • the loop 40 may be provided at a distance 126 that is about lmm from the target object 15 or may be further away from the target object.
  • the loop may be as far from the target as possible but still capable of generating the desired non-uniform electric field.
  • the loop 40 may lie in approximately the same plane as the tip of the nozzle structure (e.g., orthogonal to the axis along which the nozzle structure extends).
  • one or more process techniques may be implemented to maintain a stable cone-jet during operation of the coating process so as to achieve the selected type of coating.
  • such techniques may include adjusting the voltage between the dispensing end of the nozzle structure 18 and the object 15 being coated as the thickness of the selected type of coating increases so as to maintain a stable cone-jet at the dispensing end 23 of the nozzle structure 18 and/or monitoring at least one characteristic associated with the cone-jet to determine the stability of the cone-jet based thereon, and thereafter adjusting one or more process parameters to maintain a stable cone-jet.
  • the thickness of the selected type of coating 105 increases on the object 15, the cone-jet may become unstable.
  • the electrical potential between the first and second electrode of the system 10 may no longer be sufficient to continue cone-jet mode operation.
  • adjusting the voltage between the dispensing end 23 of nozzle structure 18 and the object 15 being coated may be needed to maintain a stable cone-jet at the dispensing end of the nozzle structure 18.
  • the adjustment of the voltage may be done manually by a user or may be performed automatically as a function of one or more characteristics of the cone-jet as described further herein.
  • a detection apparatus 50 e.g., an imaging apparatus
  • the cone-jet e.g., shift in angle 104 as shown in FIG. 2C
  • the stability of the cone-jet may then be determined based on the at least one characteristic and one or more process parameters may be adjusted accordingly to maintain a stable cone-jet.
  • an imaging apparatus may be used to detect the angle 104 as shown in FIG. 2C associated with the cone-jet.
  • control apparatus 55 may determine that the cone- jet is on the verge of instability (e.g., due to increased thickness of the coating
  • the electrical potential between the dispensing end 23 and the object 15 may be increased to maintain stable cone-jet operation.
  • the detection apparatus 50 may detect one or more flutters in the cone-jet (e.g., the cone-jet going into pulsating mode temporarily from cone-jet mode). Further, the detection apparatus may use imaging of the cone-jet to detect bubbles in at least one of the liquid flows being provided thereto. If bubbles are detected or flutters are detected, one or more various actions may be taken. For example, the flow of liquid to the nozzle may be modified, the flow may be interrupted to prevent sputtering on the surface of the target, and/or the voltage may be adjusted to eliminate the instability of the cone- jet.
  • FIG. 6 shows a nozzle structure 150 that includes three concentric openings that terminate at the dispensing end 151 and which lie along axis 161.
  • the termination of such openings can be displaced from one another along the axis 161 but must be in close proximity to allow the cone-jet to form from all compositions provided at the termination of such openings.
  • inner opening 152 is provided along axis
  • FIG. 7B is a more detailed diagram of an alternate exemplary capillary electrode configuration 400 for the distributor head 316 of FIG. 7A which includes the ability to spray particles from three flows of three different liquid compositions. Like reference numbers are used in FIG. 7B for corresponding like elements of FIG. 7 A to simplify description of the alternate capillary configuration 400.
  • the capillary electrode configuration 400 includes a first capillary tube 412 having an axis coincident with axis 301 for receiving a first flow of a liquid spray composition from a source, e.g., a suspension of biologically active material, such as a drug. Further, a second capillary tube 414 is concentric with the first capillary tube 412. An annular space 487 between the inner and outer capillaries 412, 414 is used to receive a second flow of a liquid spray composition (e.g., a polymer dissolved in a suitable solvent) and provide the flow to the dispensing tip 495 for use in establishing the spray forward thereof.
  • a liquid spray composition e.g., a polymer dissolved in a suitable solvent
  • the housing portion 430 includes an aperture 483 extending from a first end 480 of the housing portion 430 to a second end 482 thereof.
  • An inlet port 420* opens into the aperture 483.
  • the inlet port 420 receives the second flow of liquid spray composition 422 to be directed in the annular space 487 about the capillary tube 412.
  • the first capillary tube 412 has a first end 413 and a second end
  • the capillary tube 412 is positioned in the aperture 483 of the housing portion 430 of generally T-shaped configuration.
  • the first end 413 of the capillary tube 412 is sealed to housing 430 using conductive element 431 at the first end 480 of the housing portion 430.
  • the capillary tube 412 extends from the second end 482 of the housing portion 430 and with the second capillary tube 414 forms the annular space 487.
  • the second capillary tube 414 includes a first end 490 and a second end 491.
  • the second capillary tube 414 is positioned so that it is concentric with the first capillary tube 412.
  • the first end 490 of the second capillary tube 412 is coupled to the second end 482 of the housing portion 430 using conductive element 432. Further, the second end 491 of the second capillary tube 414 is held in place relative to the nozzle portion 322 by spacers 326.
  • the second capillary tube 414 extends beyond the first capillary tube 412 a predetermined distance in the direction of the target surface to be coated; about 0.2 mm to about 1 mm.
  • the portion of the second capillary tube 414 at the dispensing tip 495 which extends beyond the first capillary tube is tapered at a 60 degree to 75 degree angle for obtaining stable spray pattern and operation mode, e.g., consistent spraying patterns.
  • the second capillary tube 414 extends beyond the second end 338 of the nozzle portion 322 a predetermined distance (d5), about 2 mm to about 5 mm.
  • the first capillary tube 412 has diameters like that of capillary tube 320 of FIG. 7A.
  • the second capillary tube concentric with the first capillary tube has an outer diameter of about 533.4 ⁇ m to about 546. l ⁇ m and an inner diameter of about 393.7 ⁇ m to about 431.8 ⁇ m.
  • the gap d6 at the tip of the second capillary tube 414 is in the range of about 10 ⁇ m to about 80 ⁇ m.
  • the other configuration parameters are substantially equivalent to that described with reference to FIG. 7A.
  • liquid spray compositions are provided for establishing a spray from dispensing tip 495 of the apparatus.
  • a third liquid diluent composition 349 is also provided through inlet port 348 to dispensing tip 495.
  • the present invention is not limited to the use of capillary-type nozzle structures as various suitable nozzle structures may be employed.
  • any nozzle structure suitable to provide a spray of particles according to the principles described herein may be used, e.g., slits that may provide various cone-jets, nozzle structures having portions thereof that are integral with portions of other nozzle structures, nozzle structures that form a part of a chamber wall, radially or longitudinally configured slots, or other multiple opening nozzle structures (e.g., micromachined nozzle structures that have dual or triple openings), etc.
  • an electrospray coating system 180 employs a dispensing apparatus 182 to establish one or more sprays of particles 184 (e.g., sprays of microdroplets which evaporate to form sprays of coating particles).
  • the dispensing apparatus 182 includes a plurality of nozzle structures 188 which operate in a manner like that of nozzle structure 18 as shown in FIG. 1 to provide a selected type of coating 105 on surface 13 of object 15 positioned in a defined volume (shown generally by the dashed line 190).
  • CFR a biodurable polymer, is available from CardioTech International, Wilmington, MA, USA.
  • Solvents used for these various polymers included acetone, chloroform, tetrahydrofuran (THF), methanol (solvents were HPLC grade) and phosphate buffer, pH 7.4, all available from Sigma- Aldrich, St. Louis, USA.
  • Dexamethasone (99% purity) was available from Alexis Biochemicals, San Diego, CA, USA. [00197] Solutions of polymers were prepared at different concentrations as determined by the spraying conditions.
  • Conductivity of solvent solutions was adjusted to appropriate ranges, typically by adding ⁇ l quantities of concentrated nitric acid, measured using a Orion Benchtop Conductivity Meter, model 555A with probe M (Thermo Electron Corp., Waltham, MA, USA).
  • the optimal spray solvent for each polymer was determined by comparing the various solvents specified as compatible with each polymer by the manufacturer and assessing spray performance in terms of ability to form a stable cone-jet (i.e., stable dark tip appearance, no fluttering between cone-jet and non-cone-jet mode, and no corona discharge, see FIG. 2C herein).
  • a stable cone-jet is required to maintain uniformity of particle size during the spray process.
  • optimal feed rates were determined by evaluating the voltage required to generate a stable cone-jet spray mode while, at the same time, visually inspecting the target for obvious flaws such as spatter marks on the surface that were seen when the cone-jet was disrupted. This process produced a set of voltages and feed rates for each polymer and solvent combination that were compatible with electrospray operation in the cone-jet mode.
  • the target was moved into position by a motor-driven, computer-controlled, movable stage that permitted vertical and horizontal adjustments in positioning the target with respect to the spray tip as well as a variable advancement rate of the target through the spray field.
  • the spray operation was imaged using a video inspection microscope (Panasonic) that produced real-time images of the spray tip as well as the target.
  • the spray operation was contained within a negative- pressure chamber that drew gas supply (air, nitrogen or carbon dioxide) through a filtered supply line and was vented through a filter and fume hood. Temperature and relative humidity were monitored continuously. [00202] Unless otherwise indicated, the spray apparatus used to coat objects by electrospray was equivalent to that shown in and described with reference to FIG. 7A.
  • the apparatus included a dual concentric opening dispensing device 314 extending along axis 301.
  • First end 304 was formed of conductive portions to facilitate application of voltages or ground to capillary tube 320.
  • the capillary tube 320 was formed of stainless steel and had an outer diameter of 560 ⁇ m and an inner diameter of 260 ⁇ m.
  • the distributor head 316 included a nozzle portion or casing 322 that was an elongate substantially cylindrical metal casing concentric with the capillary tube 320 for providing an outer opening 392 concentric with inner opening 391 of the capillary tube 320.
  • the casing or nozzle portion 322 included a first end portion 336 which tapered at section 335 thereof to a narrower second end portion 338.
  • the second end portion 338 extended from the tapered section 335 and is concentric with the second end 332 of the capillary tube 320.
  • the distance from the end of the tapered section 335 to the end of the metal casing 322 is about 4.7 mm.
  • the outer diameter of the second end portion 338 is about 1050 ⁇ m and the inner diameter of the second end portion 338 is about 680 ⁇ m.
  • the second end 332 of the capillary tube 320 extends beyond the second end portion of the metal casing or nozzle portion 322 towards the target surface to be coated by a distance of about 5 mm.
  • the dispensing device was constructed of various materials.
  • the conductive elements e.g., element 316
  • the apparatus was used in a chamber made of plexiglass, and insulative parts (e.g., element 383) thereof were made of a plastic, black delrin, material.
  • Coating weight was determined by weighing the spray target before and after spraying using a Cahn electrobalance, Model 21. A goal was to achieve coatings of approximately 500 ⁇ g per stent; however, we also conducted some spray experiments where very thin coatings of approximately 40 ⁇ g were applied, or where we coated only certain regions of the stent, for a coating weight of approximately 30 ⁇ g.
  • Transfer efficiency is defined as the ratio of the mass of solid material sprayed to the weight of the coating. Only the weight of coating on the target stent was determined; the weight of material that adhered to the spray fixture was not used in the calculation due to the inability to weigh the much larger fixture reliably. Most likely the portion of sprayed material that was not present on the stent was captured by the fixture due to the force of attraction generated by the strong electrical field.
  • Imaging experiments utilized light images of stents taken using a
  • the desired coating matrix was a uniform open matrix of round particles.
  • DOE Design of Experiment
  • the cone-jet mode is the operating mode that produces the most uniform particles.
  • the voltage that must be applied to achieve the cone-jet mode is related to the conductivity of the spray fluid, so in one sense it is an outcome measure defined by the feed fluid. However, it can also be controlled within a certain range to produce the cone-jet operation. As shown in FIGs. 2A-2C herein, voltage is increased, the dripping spray tip (FIG. 2A) first assumes a pulsating appearance (FIG. 2B) and eventually the cone-jet mode (FIG. 2C) which produces the most stable nanometer-sized particles.
  • FIGs. 2A-2C herein, voltage is increased, the dripping spray tip (FIG. 2A) first assumes a pulsating appearance (FIG. 2B) and eventually the cone-jet mode (FIG. 2C) which produces the most stable nanometer-sized particles.
  • FIG. 12 shows the hysteresis effect on the relationship between voltage and current through the spray target while operating electrospray in the cone-jet mode.
  • Cone-jet (CJ) operation was observed within the voltage ranges that were marked by rapid changes in the current, depending on whether voltage was increasing or decreasing.
  • FIG. 14 shows a plot for the open-matrix coating with PLCL
  • FIG. 15 for the smooth coating (i.e., closed film) with PLCL
  • FIG. 16 for the smooth coating with Chronoflex AR. Notably, in none of the lots did a single stent coating weight exceed 2 standard deviations.
  • FIG. 14 shows the coating net weights for a lot of stents produced with the open matrix PLCL coating.
  • the optimum solvent for PLCL was acetone.
  • the ideal feed rate of the polymer/acetone solution was determined to be 6.5 ⁇ l/min sprayed at a distance of 10 mm. (See, for example, DOE results for the impact of various spray operating parameters on final coating appearance.) Maintenance of the cone-jet mode required some increase of voltage during each individual spray run.
  • FIG. 15 shows coating net weights for a lot of stents produced with the smooth PLCL coating (i.e., closed film coating). To produce this coating finish, the feed rate of the polymer/acetone/chloroform solution was 10.75 ⁇ l/min sprayed at a distance of 10 mm. Voltage was stable throughout each individual spray run.
  • FIG. 16 shows coating net weights for a lot of stents produced with the smooth Chronoflex AR coating (i.e., closed film coating).
  • the optimum solvent for this polyurethane was a blend of tetrahydrofuran and methyl alcohol.
  • Polymer solution feed rate was 10.0 ⁇ l/min sprayed at a distance of 8 mm. Voltage was stable throughout the coating of each individual stent.
  • the inner capillary feed was CFR 2% and DXM 0.2% in THF 83.3% and methanol 16.7% 2.0 ⁇ l/min, with an outer capillary feed of THF 83.3% and methanol 16.7% at a flow rate of 8 ⁇ l/min.
  • the consistency of these coating runs is significant because it demonstrates that these three different coatings can be reproduced with minimal between-stent variation in coating weight. These experiments furthermore demonstrate that coatings of acceptable weights can be achieved with these particular drug/polymer combinations.
  • One process parameter is the length of spray time.
  • Coating transfer efficiency is the amount of sprayed material that is applied to the stent surface. Transfer efficiency for each of the three coatings is shown in the table of FIG. 17 which shows coating transfer efficiency as a function of coating polymer, surface and solvents. The lowest transfer efficiency was seen for the PLCL open matrix finish. The spray pattern for this finish was much broader than seen for the other two finishes due to the higher conductivity of the sprayed material. Higher conductivity fluids generate smaller nanoparticles, which appears to correlate with wider spray patterns. A broader spray pattern means that more material is applied beyond the stent target area to the fixture.
  • Coating Thickness results were assessed by two different methodologies: profilometry, which uses a surface scan on the coating and a baseline uncoated reference area, and cyromicrotomy followed by SEM imaging. [00229] profilometry was only capable of measuring thickness on flat surfaces. Samples were prepared by coating the surface of the polished 316 stainless steel squares described earlier. While coating thickness estimates were roughly equivalent to those reported above for cryomicrotomy, this method is of limited utility because it is not applicable in its present form for the curved surface of the coronary stent. An example of a scan is shown for a PLCL open matrix coating on the flat surface in FIG. 18 which is a profilometer scan made with a Tencor PlO instrument.
  • Coating thickness was estimated at approximately 10 ⁇ m. Cryomicrotomy followed by SEM imaging was of considerably greater utility. The cross-sectional images also provide a view of the uniformity of the coating. Examples of microtomed samples are shown in FIGs. 19a-c.
  • FIG. 19 shows cross-sectional images of the three coating types produced during the production lots. Extraneous material in each image is debris caused when the microtome glass knife shatters the surface during section cuts.
  • FIG. 19a shows an open matrix PLCL coating. The crystalline-appearing debris is fragments broken from the glass knife when it hits the stent surface. Coating thickness is measured to be 13.48 ⁇ m.
  • FIG. 19b shows a smooth PLCL closed film coating. Thickness is measured to be 11.44 ⁇ m.
  • FIG. 19c shows a Chronoflex AR coating. Thickness is measured to be 3.13 ⁇ m.
  • Cryomicrotomy and SEM imaging is the most practical method for assessing coating thickness. Ideally a profilometer-type assay could be developed, using cryomicrotomy/SEM imaging as a benchmark for method validation.
  • Coating surface characteristics were initially evaluated through pilot studies and SEM imaging. After optimizing process variables for a particular polymer/drug combination and the desired surface architecture, we needed to demonstrate that these surface characteristics could be reliably and consistently produced. Using the uniform lots of coated stents, the consistency of coating surface characteristics was assessed by randomly selecting and SEM- imaging three stents from each lot in the non-expanded state and three stents after balloon expansion to 3 mm. Representative images for each coating (as shown by the key to the images provided in the table of FIG. 21) are shown in FIGs. a-f. Small type information too small to read at the bottom of each image is summarized in the key.
  • Methods for testing coating adherence under likely stress conditions include, for example, balloon expansion. Adherence could be improved for some polymers, if necessary, with use of a surface priming treatment on the stent surface.
  • the open matrix PLCL coating showed minor cracking at the strut points after balloon expansion, providing information for further coating optimization.
  • Liquid spray compositions e.g., solids and solvents
  • IF inner flow
  • OF outer flow
  • FIG. 24B shows images of the coatings resulting from the spraying of the samples in cone-jet mode. The images for each solution are provided in higher and lesser magnification.
  • the solution (0.9% poly(styrene-b-isobutylene-b-styrene (abbreviated SIBS)+0.1% paclitaxel (PTx) in 85% tetrahydrofuran (THF) and 14% methanol (MEOH) could be sprayed as open matrix coating.
  • SIBS poly(styrene-b-isobutylene-b-styrene
  • PTx paclitaxel
  • THF 85% tetrahydrofuran
  • MEOH methanol
  • FIG. 25B shows images of the coatings resulting from the spraying of the samples in cone-jet mode.
  • the images for each solution are provided in higher and lesser magnification.
  • the solution (0.9%SIBS+0.1%PTx in 99%THF) didn't spray in cone-jet mode initially because of the low conductivity.
  • More volatile and conductive solvent such as methanol was used in outer nozzle so that the open-matrix coating was achieved.
  • the closed film coating was obtained by adding the outer flow and changing the ratio between the inner and outer flow.
  • FIG. 26A The solution sample listed in the table of FIG. 26A was sprayed under the conditions provided therein.
  • FIG. 26B shows images of the coating resulting from the spraying of the samples in cone-jet mode. The images for each solution are provided in higher and lesser magnification.
  • the solution (2.25%SIBS+0.25%PTx in 97.5%THF) has high viscosity, which prevented it from being sprayed at cone-jet mode.
  • Solvent blend was introduced into outer nozzle so that the closed film coating was achieved.
  • FIG. 27A shows images of the coatings resulting from the spraying of the samples in cone-jet mode.
  • the images for each solution are provided in higher and lesser magnification.
  • the solution (4.5%SIBS+0.5%PTx in 95%THF) has high viscosity, which prevents it from being sprayed at cone-jet mode.
  • Solvent blend was introduced into outer nozzle so that the open-matrix and the closed film coatings were achieved.
  • FIG. 28B shows images of the coatings resulting from the spraying of the samples in cone-jet mode.
  • the images for each solution are provided in higher and lesser magnification.
  • An open matrix coating could be easily achieved with this solution (4.5%PLCL+0.5%DEX in 95%Acetone) because of the low boiling point and higher conductivity of acetone.
  • the acetone and chloroform blend was used as outer solvent.
  • FIG. 29B shows images of the coatings resulting from the spraying of the samples in cone-jet mode.
  • the images for each solution are provided in higher and lesser magnification.
  • Open matrix coating could be easily achieved with this solution (5%PLCL in 95%Acetone) because of the low boiling point and higher conductivity of acetone.
  • the acetone and chloroform blend was used as outer solvent.
  • FIG. 29B shows images of the coating resulting from the spraying of the sample in cone-jet mode.
  • the image for the solution was provided in higher and lesser magnification.
  • the solution (1.8%PLCL+0.2%DEX in 82%THF and 16%MEOH) didn't spray at cone-jet mode initially.
  • a small amount of methanol was added into outer nozzle to provide some conductivity.
  • a closed film coating was achieved by this way.
  • FIG. 32 shows images of the coating resulting from the spraying of the sample in cone-jet mode.
  • the images for the solution are provided in higher and lesser magnification.
  • MEK has a boiling point of 79 - 80.5C, but the conductivity is lower than methanol, which was the reason why this solution (0.9%SIBS+0.1%PTx in 69.7%THF and 29.3%MEK) didn't spray at cone-jet mode initially.
  • a solvent blend of methanol and THF was added into outer nozzle to provide more conductivity. An open matrix coating was achieved by this way.
  • FIG. 34 shows images of the coating resulting from the spraying of the sample in cone-jet mode. The images for the solution are provided in higher and lesser magnification. Unlike the other example 1-10, this solution sample was sprayed using a triple concentric opening nozzle, like that described with reference to FIG. 7B. The triple nozzle was used to encapsulate the drug with the PLCL. Acetone was used at the outermost nozzle. [00248] The apparatus used to spray the coating was equivalent to that shown in and described with reference to FIG. 7A modified with the dual capillary tube distributor head 400 shown in and described with reference to FIG. 7B.
  • the apparatus used was configured with a center capillary tube 413 having an outer diameter of about 558.8 ⁇ m (.022 inches) and an inner diameter of about 304.8 ⁇ m (.012 inches).
  • the second capillary tube 414 concentric with the center capillary tube had an outer diameter of about 1041.4 ⁇ m (.041 inches) and an inner diameter of about 685.8 ⁇ m (.027 inches).
  • the distance dl shown in FIG. 7B from the end of tapered section 335 to the end of the metal casing 322 is about 1143 ⁇ m (.045 inches).
  • the diameter d2 of the first end 336 of the nozzle portion or metal casing 322 is about 6426 ⁇ m (.253 inches).
  • the outer diameter d4 of the second end 338 of the nozzle portion 322 is about 1549 ⁇ m (.061 inches) and an inner diameter d3 of about 889 ⁇ m (.035 inches).
  • the distance d5 from the tip of the second end 338 of the nozzle portion 322 to the tip of the end of the second capillary tube 414 is about 508 ⁇ m (.020 inches).
  • the gap d6 at the tip of the second capillary tube 414 is about 685.8 ⁇ m (.027 inches).
  • the conductive elements were constructed of stainless steel, the apparatus was used in a chamber made of plexiglass, and insulative parts thereof were made of a plastic, black delrin, material. A voltage of 4300 volts was applied to conductive element 312. The distance from the dispensing tip 495 of the second capillary tube 414 to the target was about 8 mm.
  • the inner capillary flow rate was 0.75 ⁇ l/min and the stream contained 2% dexamethasone in a 2:3 blend of acetone and ethanol.
  • the second capillary flow rate was 1.5 ⁇ l/min and the stream was 5% PLCL in acetone.
  • the third and outer nozzle flow rate was 5 ⁇ l/min and contained acetone only.
  • the system was able to apply a range of polymers of differing performance qualities and solvent requirements. For each condition studied, a set of operating parameters was successfully identified that provided a cone-jet spray throughout the coating as well as the desired surface architecture. The system proved to be reliable and flexible enough to accommodate solvents over a range of polarities and conductivities.
  • a key element to the successful spray operation was the ability to merge solvent streams at the spray tip (e.g., a lower conductivity liquid spray composition including a polymer, drug and suitable solvent with a higher conductivity liquid diluent composition such as one that includes an addition of nitric acid).
  • This feature of the spray nozzle design has permitted us to spray both polar solvents and non-polar solvents of extremely low conductivity.
  • Important objectives related to scale-up for manufacturing were identified. The system produced even coatings on all intricate surfaces of a stent without webbing or coating voids. Coating weights were uniform within a tight range during lot production. Reproducible coatings were produced with different surface characteristics, including the preservation of particle architecture.
  • various modifications for the spray apparatus may be made to so as to include monitoring and controlling the process in view thereof with respect to any of the following: surface dust and fibers that contaminated the spray surface; imprecise controls on gas flow and composition through the spray chamber; inadequate evaporation rates of solvents; temperature fluctuations in ambient air; humidity fluctuations in ambient air; the need to eliminate gas bubbles from the spray feed material; the need to adjust the voltage of the power supply manually; need of bright lighting for video imaging and impact of ultraviolet light on cure of certain polymers; overspray of polymer and potentially toxic drug material and inability to clean all surfaces of the spray chamber without dismantling it; and build-up of coating overspray on the fixture leading to changes in the voltage settings required to operate in cone-jet mode.
  • such modification may include additional mechanisms to provide management of air or gas stream quality flow through improved filtration, temperature and moisture control, as well as flow rate controls. Improved control features will also enable operators to modify or facilitate solvent evaporation by improved temperature and gas control.
  • automation of voltage control may be used.
  • such automation may include video imaging assessment of the cone- jet(s) during operation and, where indicated, feedback adjustments and/or immediate termination of spray operations. For example, if the cone-jet becomes unstable and begins to "spit," this can result in discharge of excessive solvent and cause blemishes on the coated surface. The "spit" can be seen visually and the effects reduced by stopping the spray or masking the spray surface, but there is often insufficient time to react.
  • material containment and safe handling as well as treatment of the vented air or other gases passing through the spray chamber may be used to remove any stray particles.
  • Alexis F Venkatraman SS, Rath SK, Boe F. In vitro study of release mechanisms of paclitaxel and rapamycin from drug-incorporated biodegradable stent matrices. J Controlled Release 98:67-74 (2004).
  • Chen D-R Pui DYH, Kaufman SL. Electrospraying of
  • a coating that includes one or more drugs may be applied to many different types of surfaces with an open or closed matrix as a function of spraying parameters.
  • the surface of a pre- formed, hydrated hydrogel polymer surface using ElectroNanospray may be coated with a drug containing layer with various drug sustained release profiles.
  • a coating of drug and polymer may be applied to the surface of a pre- formed, hydrated hydrogel polymer surface using electronanospray, resulting in a coating which provided sustained release of the drug over 1 to 2 weeks.
  • a drug especially a hydrophobic drug
  • a drug and polymer combination may be applied to the surface of the hydrogel, also in nanoparticle form, such that the combination adhered to the surface and provided a sustained release of drug from the hydrogel for an extended period.
  • the sustained release of the drug from the hydrogel was for longer than 24 hours.
  • hydrogels have been used to deliver drugs by incorporating them directly into the hydrogel matrix. Hydrogels themselves, with or without drug loading, have also been used as coatings on different types of implants.
  • the hydrogel was removed from a buffer in a fully hydrated state, placed upon a grounded target, and its surface sprayed with drug and solvent alone or a mixture of a biodegradable polymer such as Poly(DL-lactide-co- ⁇ -caprolactone, 80/20) (PLCL) and drug (dexamethasone) in a ratio of 10: 1 using ElectroNanospray.
  • PLCL Poly(DL-lactide-co- ⁇ -caprolactone, 80/20)
  • drug drug
  • Other hydrogel material may be used with likely similar results.
  • Soft contact lenses of varying compositions are examples of such additional hydrogel materials.
  • an electrospray coating system 10 employs a dispensing apparatus 19 to establish a spray of coating particles 28 (e.g., spray of microdroplets which evaporate to form a spray of coating particles).
  • the dispensing apparatus 19 includes at least one nozzle structure 18 that includes at least two concentric openings 27, 29 (e.g., concentric about axis 39) that terminate at the dispensing end 23 thereof.
  • a drug and polymer combination in solvent may be delivered in the inner concentric opening 27 of the dual capillary spray nozzle, and a solvent alone may delivered in an outer concentric opening 29 of the nozzle in one embodiment.
  • Various spray conditions were evaluated using a design of experiments matrix approach, using either a 2% / 0.2% mixture of PLCL and dexamethasone or a 5% / 0.5% mixture.
  • the discs were placed in a 10 ml volume of phosphate buffered saline and incubated on a shaker bath at 37 degrees C. Buffer was removed and replaced at various time intervals, starting as early as 1 hour after incubation up to 14 days. The removed buffer was assayed by high performance liquid chromatograpy (HPLC) for dexamethasone concentration and the amount of drug released into the incubation medium over the time span since the previous sample was calculated. These results were plotted as a function of time and dexamethasone mass in micrograms. The methods and results are detailed below in a summary.
  • HPLC high performance liquid chromatograpy
  • the hydrogel can be preformed in its final configuration (i.e. not prior to polymerization); the degree of drug loading can be controlled; the drug can be applied as a nanoparticulate matrix; the drug can be encapsulated in a biodegradable, bioerodable polymer that is also applied to the hydrogel' s surface; this coating can result in gradual release of the drug from the hydrogel 's surface.
  • the drug need not be eluted quickly from the hydrogel' s surface despite maintenance of the hydrogel in an aqueous buffer solution.
  • the method and device may be used to provide antimicrobial treatment or anti-inflammatory treatment to an implant or surface applied hydrogel (e.g. contact lens) that has a dwell time of one day or longer as a means of making the hydrogel use safer or less irritating to the body. It may also be used as a means of applying an implantable or topical therapy of another sort.
  • hydrogels are being discussed as possible replacements for metallic coronary stents.
  • An antiinflammatory compound such as a steroid (e.g., dexamethasone), a nonsteroidal antiinlammatory agent (e.g. ibuprofen or indomethacin), an antiproliferative agent (e.g. paclitaxel or rapamycin) may be applied to the hydrogel prior to implantation to prevent scarring at the site of implantation. Other antiproliferative or antiinfective drugs may also be used.
  • Hydrogel discs similar in flexible contact lens material in appearance and flexibility, may be coated with a poorly water-soluble antifungal agent, griseofulvin, using ElectroNanospray. Control images were developed for the hydrogel to determine its underlying structural appearance using SEM cryostage imaging. Hydrogel appears to form a good target for the spray process. Particles were adherent to the surface with preserved nanoparticulate architecture. Several images are provided to illustrate to support these statements.
  • hydrogel specimens were imaged using
  • FIGs. 35A and 35B are different magnifications of an example sample image of dried hydrogel with no drug coating. This sample was relatively smooth with minor surface defects.
  • FIGs. 36A and 36B For imaging the hydrated gel sample, a cryostage technique was used. The hydrogel sample was first equilibrated in deionized water for 24 h at room temperature and then very quickly frozen using liquid nitrogen. Imaging of the frozen moist sample with no drug coating is shown with different amplifications in FIGs. 36A and 36B and was taken at 5.0 kV. This image showed a finely particulate surface that may represent ice crystals. [00276] Cryo fracturing of the frozen specimen was done to obtain a cross- sectional interior view. The frozen specimen was fractured with a sharp scalpel, then sputter-coated with gold for 480 s (FIGs. 37A and 37B).
  • griseofulvin (0.09023 g), a poorly water soluble antifungal agent, was dissolved in a mixture of ethanol (9 ml) and acetone (6 ml).
  • a hydrogel sample approximately 5 mm in largest diameter, removed from a borate buffer solution and placed on a metallic spray platform beneath the ElectroNanospray device's dual capillary spray head.
  • the solution was sprayed in the cone jet mode at 4.17 kV at 5 ⁇ l/min and a distance of 15.6 mm from the hydrogel. Spray time was 20 minutes.
  • the surface pattern seen in the SEM image shown in FIGs. 39A and 39B show a uniform, closely packed surface of approximately 200 nm particles at 20,00OX magnification.
  • FIGs. 4OA and 40B For comparison purposes, an image of a stainless steel plate coated with griseofulvin is shown in FIGs. 4OA and 40B. The particles are more clumped together in grape-like clusters, but approximately the same size as those seen in FIGs. 37 A and 37B.
  • nanoparticles of the hydrophobic anti-fungal drug griseofulvin may be applied to the hydrogel material with ElectroNanospray, a coating that provides sustained release of a model drug from the hydrogel over a minimum of 1 day or longer may be obtained.
  • a polymer stabilizing material may be used to help control drug release.
  • Dexamethasone provides a reasonable model drug for example. Spray methods for the combination of the biodegradable polymer, poly(DL-lactide-co- ⁇ -caprolactone, 80/20) or PLCL, and the steroid antiinflammatory agent dexamethasone were performed, and HPLC analytical methods were used for measuring dexamethasone release over time.
  • FIG. 41 One example image of a surface coated based on this model system is shown in FIG. 41. This image was taken from a generic stainless steel coronary stent coated with dexamethasone and PLCL. Note the open matrix particulate nature of the surface morphology. This is even more open than the previously shown image of the gel coated with griseofulvin. This coating has been remarkably consistent on a wide range of substrates.
  • Spray experiments were then designed to determine if spray coating conditions could (a) apply dexamethasone and PLCL to the surface of the hydrogel and (b) how changes in those parameters affected the rate of release from the surface. In one embodiment, a prolonged release pattern may be desired rather than a "burst" of drug release in the first few hours.
  • Materials The polymer poly(DL-lactide-co- ⁇ -caprolactone,
  • PLCL inherent viscosity 0.77 dL/g in chloroform
  • Dexamethasone (99% purity) was purchased from Alexis Biochemicals, San Diego, CA, USA. Hydrogel discs similar to soft contact lenses in appearance and flexibility were obtained in buffer solution. These were placed in phosphate buffered saline (PBS) and maintained at 4°C until the day of the coating experiments, when they were brought to ambient temperature in the buffer. Two different concentrations of polymer/drug were used: 2% PLCL/0.2% dexamethasone and 5% PLCL/0.5% dexamethasone.
  • PBS phosphate buffered saline
  • FIGs. 41 and 42 illustrate dexamethasone release over a 14-day period, grouped by the concentration of dexamethasone used in the spray experiment matrix.
  • FIG. 41 is a graph showing release of dexamethasone ( ⁇ g) from the coated hydrogel samples over a 14 day period. Concentration of PLCL polymer was 2% and concentration of dexamethasone was 0.2% in the spray fluid of the inner capillary. Acetone was the solvent.
  • FIG. 42 is a graph showing release of dexamethasone ( ⁇ g) from the coated hydrogel samples over a 14 day period. Concentration of PLCL polymer was 5% and concentration of dexamethasone was 0.5% in the spray fluid of the inner capillary. Acetone was the solvent.
  • the hydrogel could be pre-formed and coated later with the desired therapeutic agent.
  • coatings may be formed to provide different drug release profiles.
  • the coatings may be engineered to provide a desired specific drug release profile.
  • Types of coatings may also be varied in terms of single type of coating or hybrid types of coating to provide rapid versus delayed release.
  • polymers, or polymeric materials may also be used in the coating processes.
  • Polyurethane, poly(lactide- co-caprolactone), isobutylene copolymers and other polymeric materials may also be used.
  • drugs such as, for example, paclitaxel or other drugs may also be used. Combinations of two or more drugs may also be provided in a single coating. In yet further embodiments, different drugs may be applied in different types of coatings on the same substrate, such as single and hybrid coatings to obtain multiple release profiles.
  • Various metallic and non-metallic surfaces may also be coated with open and closed matrix coatings.
  • Such substrates in various embodiments include but are not limited to stainless steel, foamed tantalum, hydrogel (in both dry and hydrated state), plastic (polymeric) materials.
  • the coatings which may be applied to such substrates include but are not limited to poly(lactide-co-caprolactone), arborescent polyisobutylenes (arbPIBS), and hydrophobic drugs (dexamethasone).
  • various methods of charging the surface to enable coatings to both spray and bind to surfaces are utilized.
  • An ionizer may be used to charge a surface with negative (positive) charge. Positive and negative particles may be sprayed from adjacent spray heads as described below. Successive passes with positive and negative spray streams may also be performed.
  • Conductive elements carbon black
  • non-conductive materials such as a plastic may be coated using one or more spray heads to alternately charge a surface of a sample to be coated.
  • Block schematic diagrams of various multiple spray head arrangements are illustrated in FIGs. 45 A, 45B and 45C.
  • a first sprayhead 4510 and a second sprayhead 4520 are illustrated as directed toward a sample 4530 to be sprayed. Motion of the sample is illustrated by arrows proximate the sample in the various figures.
  • the sprayheads include coaxial concentric openings for delivering different fluids to a spray. They may be the same or similar to those shown in FIG. 1 and FIGs. 7A and 7B. [00298] In FIG.
  • the sprayheads 4510 and 4520 are illustrated as substantially parallel to each other and are approximately the same distance from the sample 4530, which is located beneath their nozzles.
  • the motion of the sample is orthogonal to the sprayheads, but may also represent a relative motion between the sprayheads and the sample, one or both of which may be moved to provide such relative motion.
  • the sprayheads are spaced apart a sufficient distance such that their sprays do not interact prior to reaching the sample, hi further embodiments, the distance is minimized, or may be increased depending on space constraints in the context of use. In further embodiments, the sprays from each of the sprayheads may be alternated in time with some or no overlap, allowing a closer spacing of the sprayheads if desired.
  • the sprayheads 4510 and 4520 are angled inward to point toward the sample. In one embodiment, the angle between them as approximately 45 degrees, but may be varied between parallel as in FIG. 45 A to even greater than 45 degrees.
  • the sprayheads 4510 and 4520 are positioned opposite each other from the sample 4530, which rotates while being sprayed.
  • Sprayheads were either pointed straight down or at a 45 degree angle to each other.
  • Sprayhead #1 had a positive high voltage charge and had polymer solution dispensed to it.
  • Sprayhead #2 had a wire inserted in the inner capillary (electrode) and had a negative high voltage charge.
  • Sprayhead #2 basically became a high voltage electrode.
  • the plastic cover slip was mounted to a 1 A" wide grounded piece of stainless steel (reference number 4540) approximately 12mm below sprayhead. The coverslip was moved back and forth (y-axis) from under sprayhead #1 to sprayhead #2. The result was a coating of polymer on the coverslip. The coating was more even if the plastic was moved in the x-axis under the sprayhead. This method also would if the polarity of the sprayheads was switched, as long as one was positive and one was negative.
  • sprayhead #1 was pointing straight down over coverslip which was mounted on a .5" diameter rotating grounded cylinder (reference number 4550). The distance from the tip of the sprayhead to the top edge of the cylinder was approximately 10mm. Sprayhead #1 had a positive high voltage charge and had a polymer solution dispensed to it. Sprayhead #2 was pointing straight up under the cylinder mounted rotating coverslip. The distance from the tip of the sprayhead to the bottom edge of the cylinder was approximately 10mm. Sprayhead #2 had a negative high voltage charge and had a non-polymer solution dispensed to it. The rotating cylinder was run through the sprayheads in the x-direction slowly back and forth. [00305] The plastic became positively charged under sprayhead #1 and negatively charged under sprayhead #2, so when the plastic went under sprayhead #1 again, the polymer particles were attracted to the plastic coverslip.
  • the target was moved into position by a motor-driven, computer-controlled movable stage that permitted vertical and horizontal adjustments in positioning the target with respect to the spray tip as well as a variable advancement rate of the target through the spray field.
  • the spray operation was imaged using a video inspection microscope (Panasonic) that produced real time images of the spray tip as well as the target.
  • the spray operation was contained within a negative pressure chamber that drew gas supply (air, nitrogen or carbon dioxide) through a filtered supply line and was vented through a filter and fume hood. Temperature and relative humidity were monitored continuously.
  • the system may include several features in further embodiments, such as computer controlled parameters, improved spray chamber isolation, a configurable spray platform that permits two or more spray heads, a re-designed spray nozzle for improved ease of manufacture, improved feed pumps, video imaging of multiple spray heads and the target, and software control with the ability to program process steps.
  • Chronoflex AR (CFR) is polyurethane 22% solid in dimethylacetamide.
  • CFR a drug-eluting material, was purchased from CardioTech International, Wilmington, MA, USA.
  • Aborescent block co-polymers of polyisobutylene and polystyrene, TPEl, TPE4, and TPE5 were obtained from Dr. Judit Puskas at the University of Akron.
  • Biochemicals, San Diego, CA, USA and paclitaxel was purchased from (LC Laboratories, Woburn, MA, USA).
  • Solutions of polymers were prepared at different concentrations as determined by the spraying conditions. A variety of polymer concentrations and solvent combinations were investigated; acceptable concentrations (weight/volume) and primary solvents included PLCL 5% in acetone; CFR 2% in THF, and TPE1-5, 1% in THF. Dexamethasone was added to polymer solutions, with final concentrations varying from 10 to 20% of the polymer weight, resulting in a 10:1 to 5:1 polymer: dexamethasone ratio by weight respectively. Conductivity of solvent solutions was adjusted to appropriate ranges, typically by adding ⁇ l quantities of concentrated nitric acid, measured using a Orion Benchtop Conductivity Meter (Thermo Electron Corp., Waltham, MA, USA).
  • the optimal spray solvent for each polymer was determined by comparing the various solvents specified as compatible with each polymer by the manufacturer and assessing spray performance in terms of ability to form a stable cone jet (i.e. stable dark tip appearance, no fluttering between cone jet and non-cone jet mode and no corona discharge).
  • optimal feed rates were determined by evaluating the voltage required to generate a stable cone jet spray mode while at the same time, visually inspecting the target for obvious flaws, such as spit marks on the surface that were seen when the cone jet was disrupted. This process produced a set of voltages and feed rates for each polymer and solvent combination that were compatible with electrospray operation in the cone jet mode.
  • DOE Design of Experiment
  • Optimized conditions used to coat the samples used for the drug release studies were as follows, listed per coating surface polymer and type of finish: PLCL Open Matrix: Inner capillary feed was PLCL 5% and DXM 0.5% in acetone at a flow rate of 1.5 ⁇ l /min. The outer capillary feed was acetone with added nitric acid to achieve a conductivity of 6.8 ⁇ S/cm and at a flow rate of 5 ⁇ l/min.
  • PLCL Closed Film Inner capillary feed was PLCL 5% and
  • TPEl open matrix Inner capillary feed was TPE 1 1 % and DXM
  • TPEl closed film Inner capillary feed was TPE 1 1 % and DXM
  • the outer capillary feed was THF 5 parts to 2 parts ethanol at a flow rate of 3 ⁇ l/min.
  • TPE4 open matrix Inner capillary feed was TPE4 1 % and DXM
  • THF 90% and methanol 10% 0.1% in THF 90% and methanol 10% at a flow rate of 2.0 ⁇ l/min.
  • the outer capillary feed was THF 90% and methanol 10% with added nitric acid to achieve a conductivity of 0.4 ⁇ S/cm and at a flow rate of 3 ⁇ l/min.
  • TPE4 closed film Inner capillary feed was TPE4 90% and DXM
  • TPE5 open Inner capillary feed was TPE5 1 % and DXM 0.1 % in THF 86% and methanol 14% at a flow rate of 0.5 ⁇ l/min.
  • the outer capillary feed was TPE5 0.5% and DXM 0.05% in THF 86% and methanol 14% at a flow rate of 3 ⁇ l/min.
  • TPE5 closed Inner capillary feed was TPE5 1 % and DXM 0.1 % in THF 7 parts to one part ethanol at a flow rate of 2.0 ⁇ l/min.
  • the outer capillary feed was THF 5 parts to 2 parts ethanol at a flow rate of 3.0 ⁇ l/min.
  • Coating weight at the ⁇ g scale was determined by weighing the spray target before and after spraying using a Cahn electrobalance, Model 31. Imaging
  • Stents were imaged using scanning electron microscopy (SEM) to verify coating qualities, surface uniformity, and lack of void areas or webbing at strut junction points. Images were taken on multiple points over the outer and inner surfaces of the struts, at low (45X) and high (5000X and 20,000X) magnifications.
  • HPLC methods to quantify dexamethosone (DXM) and three peptides (luteinizing hormone releasing hormone (human; LHRH), angiotensin I, and insulin chain B) were developed using an HP 1090 system equipped with a narrowbore column (Zorbax SB C-18, 2.1 mm i.d. x 150 mm, 3.5 ⁇ m) and UV detector. Data integration and processing were performed with Agilent ChemStation software (Rev. A.08.03). Peak areas were obtained by subtracting the baseline (from a "blank" injection of the sample matrix) from the experimental chromatogram.
  • DXM was analyzed with the following method: 20/80 to 100/0 to 20/80 acetonitrile/water in 3 min and 3.01 min at 0.6 mL/min, end run at 6 min; 65 0 C; 10 ⁇ L injection volume. DXM, which was detected at 243 nm, eluted at 2.27 min.
  • the peptides (all obtained from Sigma-Aldrich) were analyzed with the following method: 20/80 to 50/50 to 20/80 acetonitrile/water buffered with 0.1 % (v/v) perchloric acid in 5 min and 5.01min at 0.4 mL/min, end run at 9 min; 65 0 C; 10 ⁇ L injection volume; 210 nm detection wavelength.
  • the retention of the peptides was measured before and after the ElectroNanospray process described earlier. LHRH eluted at 2.61 min, angiotensin I eluted at 3.54 min, and insulin B chain eluted at 4.71 min.
  • FIGs. 46 and 47 cumulative dexamethasone release results, in terms of percent coating dose, are reported for two different coating morphologies that were obtained for each polymer. The distinct coating morphologies were achieved by varying flow rate, distance to target, solvent or co-solvent blend, and to a lesser degree, rate of passage of the target beneath the spray tip.
  • FIG. 46 illustrates cumulative dexamethasone release from PLCL and TPEl, with SEM images of the respective coating types.
  • FIG. 47 illustrates cumulative dexamethasone release from TPE4 and TPE5, with SEM images of the respective coating types. Release data obtained from TPE4 on stents; TPE5 on stainless steel squares. Drug release results for TPE5 are particularly interesting. Three different curves are shown, one for the smooth film and the other two for open matrix particulate coatings, where two different amounts of methanol were used in the co-solvent blend. The co-solvent with the higher methanol percentage showed a release profile intermediate between the smooth film and the lower methanol blend. This is the first time we have observed shown that the solvent composition used during the application can affect the rate of drug release from the coating.
  • results are shown for a hybrid layer of TPE4 coated on a stainless steel plate. Release results for this hybrid coating were intermediate between the smooth film and open matrix particle coating.
  • An SEM image at 5,000X shows cross section created by cryomicrotome, where open matrix particle coating is on surface overlying the smooth film.
  • the graph shows dexamethasone cumulative release from TPE4 open matrix particle coating and smooth film compared to a hybrid coating similar to one in the image, where the smooth film represented 300 ⁇ g and the open matrix particle coating 100 ⁇ g of total coating weight.
  • the peptides may be sprayed in solution with at least 50 percent acetone or alcohol and co-spraying with and without PLCL. Material eluted from these coating experiments was also analyzed by HPLC; preliminary results show that retention times also do not change. It should be emphasized that this provides only a limited indication of structural integrity of the peptide.
  • Coating morphologies may directly impact the rate and quantity of drug release from a given polymer/drug system.
  • the polyisobutylene outer layer is modified, which could impact both drug release as well as biocompatibility.
  • the degree of control offered by ElectroNanospray is a potentially important advance.

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Abstract

L'invention concerne un revêtement d'hydrogel nanoparticulaire qui peut être formé par un procédé d'électropulvérisation de nanoparticules sur une surface, comprenant la fourniture d'une combinaison de médicament et de polymère dans un solvant à un tube capillaire d'une buse de pulvérisation coaxiale à deux tubes capillaires. Ceci permet d'obtenir un revêtement comprenant un médicament qui se libère avec le temps. Des matrices ouvertes et fermées peuvent être formées sélectivement pour aider à modifier les périodes de libération contrôlée.
EP08725099A 2007-01-31 2008-01-31 Revêtement nanoparticulaire de surfaces Withdrawn EP2111305A2 (fr)

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US88759707P 2007-01-31 2007-01-31
US11/669,937 US9248217B2 (en) 2006-01-31 2007-01-31 Nanoparticle coating of surfaces
PCT/US2008/001410 WO2008094700A2 (fr) 2007-01-31 2008-01-31 Revêtement nanoparticulaire de surfaces

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US6433154B1 (en) 1997-06-12 2002-08-13 Bristol-Myers Squibb Company Functional receptor/kinase chimera in yeast cells
AU6162501A (en) 2000-05-16 2001-11-26 Univ Minnesota High mass throughput particle generation using multiple nozzle spraying
US7247338B2 (en) 2001-05-16 2007-07-24 Regents Of The University Of Minnesota Coating medical devices
US9248217B2 (en) 2006-01-31 2016-02-02 Nanocopocia, LLC Nanoparticle coating of surfaces
WO2007089881A2 (fr) 2006-01-31 2007-08-09 Regents Of The University Of Minnesota Revetement d'objets par electropulverisation
US9108217B2 (en) 2006-01-31 2015-08-18 Nanocopoeia, Inc. Nanoparticle coating of surfaces
CN103566414B (zh) * 2013-08-13 2016-01-13 重庆大学 一种核壳结构纳微粒涂层血管支架及其制备方法
CN115957379A (zh) * 2021-10-13 2023-04-14 北京化工大学 一种神经修复膜及其制备方法和应用

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GB9225098D0 (en) * 1992-12-01 1993-01-20 Coffee Ronald A Charged droplet spray mixer
NL1003442C2 (nl) * 1996-06-27 1998-01-07 Univ Delft Tech Werkwijze voor het bereiden van een poeder, een met de genoemde werkwijze bereid poeder, een elektrode en een inrichting voor toepassing bij de genoemde werkwijze.
US5948483A (en) * 1997-03-25 1999-09-07 The Board Of Trustees Of The University Of Illinois Method and apparatus for producing thin film and nanoparticle deposits
US7247338B2 (en) * 2001-05-16 2007-07-24 Regents Of The University Of Minnesota Coating medical devices
WO2006086654A2 (fr) * 2005-02-11 2006-08-17 Battelle Memorial Institute Nanopreparations
US9248217B2 (en) * 2006-01-31 2016-02-02 Nanocopocia, LLC Nanoparticle coating of surfaces

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