Apparatus and method of delivering a focused beam of a thermodynamically stable/metastable mixture of a functional material in a dense fluid onto a receiver

Information

  • Patent Grant
  • 6471327
  • Patent Number
    6,471,327
  • Date Filed
    Tuesday, February 27, 2001
    23 years ago
  • Date Issued
    Tuesday, October 29, 2002
    22 years ago
Abstract
An apparatus and method of focusing a functional material is provided. The apparatus includes a pressurized source of fluid in a thermodynamically stable mixture with a functional material. A discharge device having an inlet and an outlet is connected to the pressurized source at the inlet. The discharge device is shaped to produce a collimated beam of functional material, where the fluid is in a gaseous state at a location before or beyond the outlet of the discharge device. The fluid can be one of a compressed liquid and a supercritical fluid. The thermodynamically stable mixture includes one of the functional material being dispersed in the fluid and the functional material being dissolved in the fluid.
Description




FIELD OF THE INVENTION




This invention relates generally to deposition and etching technologies and, more particularly, to a technology for delivering a collimated and/or focused beam of functional materials dispersed and/or dissolved in a compressible fluid that is in a supercritical or liquid state and becomes a gas at ambient conditions, to create a high-resolution pattern or image onto a receiver.




BACKGROUND OF THE INVENTION




Several conventional high-resolution deposition and etching technologies are used in the creation of value-added multi-layer products in applications ranging from semiconductor processing to imaging media manufacture. In this sense, deposition technologies are typically defined as technologies that deposit functional materials dissolved and/or dispersed in a fluid onto a receiver (also commonly referred to as a substrate, etc.) to create a pattern. Etching technologies are typically defined as technologies that create a specific pattern on a receiver through the selective alteration of portions of the receiver by delivering materials dissolved and/or dispersed in a fluid onto the receiver to physically remove selective portions of the receiver and/or chemically modify the receiver.




Technologies that deposit a functional material onto a receiver using gaseous propellants are known. For example, Peeters et al., in U.S. Pat. No. 6,116,718, issued Sep. 12, 2000, disclose a print head for use in a marking apparatus in which a propellant gas is passed through a channel, the functional material is introduced controllably into the propellant stream to form a ballistic aerosol for propelling non-colloidal, solid or semi-solid particulate or a liquid, toward a receiver with sufficient kinetic energy to fuse the marking material to the receiver. There is a problem with this technology in that the functional material and propellant stream are two different entities and the propellant is used to impart kinetic energy to the functional material. When the functional material is added into the propellant stream in the channel, a non-colloidal ballistic aerosol is formed prior to exiting the print head. This non-colloidal ballistic aerosol, which is a combination of the functional material and the propellant, is not thermodynamically stable/metastable. As such, the functional material is prone to settling in the propellant stream which, in turn, can cause functional material agglomeration leading to nozzle obstruction and poor control over functional material deposition.




Technologies that use supercritical fluid solvents to create thin films are also known. For example, R. D. Smith in U.S. Pat. No. 4,734,227, issued Mar. 29, 1988, discloses a method of depositing solid films or creating fine powders through the dissolution of a solid material into a supercritical fluid solution and then rapidly expanding the solution to create particles of the functional material in the form of fine powders or long thin fibers which may be used to make films. There is a problem with this method in that the free-jet expansion of the supercritical fluid solution results in a non-collimated/defocused spray that can not be used to create high resolution patterns on a receiver. Further, defocusing leads to losses of the functional material.




As such, there is a need for a technology that permits high speed, accurate, and precise deposition of a functional material on a receiver. There is also a need for a technology that permits functional material deposition of ultra-small (nano-scale) particles. There is also a need for a technology that permits high speed, accurate, and precise etching of a receiver that permits the creation of ultra-small (nano-scale) features on a receiver. Additionally, there is a need for a self-energized, self-cleaning technology capable of controlled solute deposition in a format that is free from receiver size restrictions. There is also a need for a technology that permits high speed, accurate, and precise patterning of a receiver that can be used to create a high resolution patterns on a receiver. There is also a need for a technology that permits high speed, accurate, and precise patterning of a receiver having reduced material agglomeration characteristics. There is also a need for a technology that permits high speed, accurate, and precise patterning of a receiver wherein the functional material to be deposited on the receiver and dense fluid which is the carrier of the functional material, are in a thermodynamically stable/metastable mixture. There is also a need for a technology that permits high speed, accurate, and precise patterning of a receiver that has improved material deposition capabilities.




SUMMARY OF THE INVENTION




An object of the present invention is to provide a technology that permits high speed, accurate, and precise deposition of a functional material on a receiver.




Another object of the present invention is to provide a technology that permits functional material deposition of ultra-small particles.




Another object of the present invention is to provide a technology that permits high speed, accurate, and precise patterning of a receiver that permits the creation of ultra-small features on the receiver.




Another object of the present invention is to provide a self-energized, self-cleaning technology capable of controlled functional material deposition in a format that is free from receiver size restrictions.




Another object of the present invention is to provide a technology that permits high speed, accurate, and precise patterning of a receiver that can be used to create high resolution patterns on the receiver.




Yet another object of the present invention is to provide a technology that permits high speed, accurate, and precise patterning of a receiver having reduced functional material agglomeration characteristics.




Yet another object of the present invention is to provide a technology that permits high speed, accurate, and precise patterning of a receiver using a mixture of functional material and dense fluid that is thermodynamically stable/metastable.




Yet another object of the present invention is to provide a technology that permits high speed, accurate, and precise patterning of a receiver that has improved material deposition capabilities.




According to a feature of the present invention, an apparatus for focusing a functional material includes a pressurized source of fluid in a thermodynamically stable mixture with a functional material. A discharge device having an inlet and an outlet is connected to the pressurized source at the inlet. The discharge device is shaped to produce a collimated beam of functional material, where the fluid is in a gaseous state at a location before or beyond the outlet of the discharge device. The fluid can be one of a compressed liquid and a supercritical fluid. The thermodynamically stable mixture includes one of the functional material being dispersed in the fluid and the functional material being dissolved in the fluid.




According to another feature of the invention, a method of focusing a functional material includes providing a pressurized source of fluid in a thermodynamically stable mixture with a functional material; and causing the functional material to collimate.




According to another feature of the invention, an apparatus for focusing a functional material includes a pressurized source of fluid in a thermodynamically stable mixture with a functional material. A discharge device having an inlet and an outlet is connected to the pressurized source at the inlet. The discharge device has a variable area portion and a constant area portion with a collimated beam of functional material being produced as the mixture moves from the inlet of the discharge device through the outlet of the discharge device and the fluid being in a gaseous state at a location relative to the discharge device. The location can be positioned within a region of the discharge device or positioned in a region beyond the discharge device.




According to another feature of the invention, a method of focusing a functional material includes providing one of a compressed liquid and a supercritical fluid in a first predetermined thermodynamic state, adding a functional material to one of the compressed liquid and the supercritical fluid; and moving the functional material and one of the compressed liquid and the supercritical fluid to a second thermodynamic state, whereby one of the compressed liquid and the supercritical fluid evaporates allowing the functional material to release in a collimated beam. In the method, moving one of the compressed liquid and the supercritical fluid and the functional material to a second thermodynamic state can include focusing the functional material.











BRIEF DESCRIPTION OF THE DRAWINGS




In the detailed description of the preferred embodiments of the invention presented below, reference is made to the accompanying drawings, in which:





FIG. 1A

is a schematic view of a preferred embodiment made in accordance with the present invention;





FIGS. 1B-1G

are schematic views of alternative embodiments made in accordance with the present invention;





FIG. 2A

is a block diagram of a discharge device made in accordance with the present invention;





FIGS. 2B-2M

are cross sectional views of a nozzle portion of the device shown in

FIG. 2A

;





FIGS. 3A-3D

are diagrams schematically representing the operation of the present invention; and





FIGS. 4A-4K

are cross sectional views of a portion of the invention shown in FIG.


1


A.











DETAILED DESCRIPTION OF THE INVENTION




The present description will be directed in particular to elements forming part of, or cooperating more directly with, apparatus in accordance with the present invention. It is to be understood that elements not specifically shown or described may take various forms well known to those skilled in the art. Additionally, materials identified as suitable for various facets of the invention, for example, functional materials, solvents, equipment, etc. are to be treated as exemplary, and are not intended to limit the scope of the invention in any manner.




Referring to

FIG. 1A

, delivery system


10


has components,


11


,


12


, and


13


that take chosen solvent and/or dispersant materials to a compressed liquid and/or supercritical fluid state, make a solution and/or dispersion of an appropriate functional material or combination of functional materials in the chosen compressed liquid and/or supercritical fluid, and deliver the functional materials as a collimated and/or focused beam onto a receiver


14


in a controlled manner. Functional materials can be any material that needs to be delivered to a receiver, for example electroluminescent materials, imaging dyes, ceramic nanoparticles etc., to create a pattern on the receiver by deposition, etching, coating, other processes involving the placement of a functional material on a receiver, etc.




In this context, the chosen materials taken to a compressed liquid and/or supercritical fluid state are gases at ambient pressure and temperature. Ambient conditions are preferably defined as temperature in the range from −100 to +100° C., and pressure in the range from 1×10


−8


-100 atm for this application.




In

FIG. 1A

a schematic illustration of the delivery system


10


is shown. The delivery system


10


has a compressed liquid/supercritical fluid source


11


, a formulation reservoir


12


, and a discharge device


13


connected in fluid communication along a delivery path


16


. The delivery system


10


can also include a valve or valves


15


positioned along the delivery path


16


in order to control flow of the compressed liquid/supercritical fluid.




A compressed liquid/supercritical fluid carrier, contained in the compressed liquid/supercritical fluid source


11


, is any material that dissolves/solubilizes/disperses a functional material. The compressed liquid/supercritical fluid source


11


delivers the compressed liquid/supercritical fluid carrier at predetermined conditions of pressure, temperature, and flow rate as a supercritical fluid, or a compressed liquid. Materials that are above their critical point, defined by a critical temperature and a critical pressure, are known as supercritical fluids. The critical temperature and critical pressure typically define a thermodynamic state in which a fluid or a material becomes supercritical and exhibits gas like and liquid like properties. Materials that are at sufficiently high temperatures and pressures below their critical point are known as compressed liquids. Materials in their supercritical fluid and/or compressed liquid state that exist as gases at ambient conditions find application here because of their unique ability to solubilize and/or disperse functional materials of interest in the compressed liquid or supercritical state.




Fluid carriers include, but are not limited to, carbon dioxide, nitrous oxide, ammonia, xenon, ethane, ethylene, propane, propylene, butane, isobutane, chlorotrifluoromethane, monofluoromethane, sulphur hexafluoride and mixtures thereof Due its characteristics, e.g. low cost, wide availability, etc., carbon dioxide is generally preferred in many applications.




The formulation reservoir


12


is utilized to dissolve and/or disperse functional materials in compressed liquids or supercritical fluids with or without dispersants and/or surfactants, at desired formulation conditions of temperature, pressure, volume, and concentration. The combination of functional material and compressed liquid/supercritical fluid is typically referred to as a mixture, formulation, etc.




The formulation reservoir


12


can be made out of any suitable materials that can safely operate at the formulation conditions. An operating range from 0.001 atmosphere (1.013×10


2


Pa) to 1000 atmospheres (1.013×10


8


Pa) in pressure and from −25 degrees Centigrade to 1000 degrees Centigrade is generally preferred. Typically, the preferred materials include various grades of high pressure stainless steel. However, it is possible to use other materials if the specific deposition or etching application dictates less extreme conditions of temperature and/or pressure.




The formulation reservoir


12


should be precisely controlled with respect to the operating conditions (pressure, temperature, and volume). The solubility/dispersibility of functional materials depends upon the conditions within the formulation reservoir


12


. As such, small changes in the operating conditions within the formulation reservoir


12


can have undesired effects on functional material solubility/dispensability.




Additionally, any suitable surfactant and/or dispersant material that is capable of solubilizing/dispersing the functional materials in the compressed liquid/supercritical fluid for a specific application can be incorporated into the mixture of functional material and compressed liquid/supercritical fluid. Such materials include, but are not limited to, fluorinated polymers such as perfluoropolyether, siloxane compounds, etc.




Referring to

FIGS. 1B-1D

, alternative embodiments of the invention shown in

FIG. 1A

are described. In each of these embodiments, individual components are in fluid communication, as is appropriate, along the delivery path


16


.




Referring to

FIGS. 1B and 1C

, a pressure control mechanism


17


is positioned along the delivery path


16


. The pressure control mechanism


17


is used to create and maintain a desired pressure required for a particular application. The pressure control mechanism


17


can include a pump


18


, a valve(s)


15


, and a pressure regulator


19




a


, as shown in FIG.


1


B. Alternatively, the pressure control mechanism


17


can include a pump


18


, a valve(s)


15


, and a multi-stage pressure regulator


19




b


, as shown in FIG.


1


C. Additionally, the pressure control mechanism can include alternative combinations of pressure controlling devices, etc. For example, the pressure control mechanism


17


can include additional valve(s)


15


, actuators to regulate fluid/formulation flow, variable volume devices to change system operating pressure, etc., appropriately positioned along the delivery path


16


. Typically, the pump


18


is positioned along the delivery path


16


between the fluid source


11


and the formulation reservoir


12


. The pump


18


can be a high pressure pump that increases and maintains system operating pressure, etc. The pressure control mechanism


17


can also include any number of monitoring devices, gauges, etc., for monitoring the pressure of the delivery system


10


.




A temperature control mechanism


20


is positioned along delivery path


16


in order to create and maintain a desired temperature for a particular application. The temperature control mechanism


20


is preferably positioned at the formulation reservoir


12


. The temperature control mechanism


20


can include a heater, a heater including electrical wires, a water jacket, a refrigeration coil, a combination of temperature controlling devices, etc. The temperature control mechanism can also include any number of monitoring devices, gauges, etc., for monitoring the temperature of the delivery system


10


.




The discharge device


13


includes a nozzle


23


positioned to provide directed delivery of the formulation towards the receiver


14


. The discharge device


13


can also include a shutter


22


to regulate the flow of the supercritical fluid/compressed liquid and functional material mixture or formulation. The shutter


22


regulates flow of the formulation in a predetermined manner (i.e. on/off or partial opening operation at desired frequency, etc.). The shutter


22


can be manually, mechanically, pneumatically, electrically or electronically actuated. Alternatively, the discharge device


13


does not have to include the shutter


22


(shown in FIG.


1


C). As the mixture is under higher pressure, as compared to ambient conditions, in the delivery system


10


, the mixture will naturally move toward the region of lower pressure, the area of ambient conditions. In this sense, the delivery system is said to be self-energized.




The receiver


14


can be positioned on a media conveyance mechanism


50


that is used to control the movement of the receiver during the operation of the delivery system


10


. The media conveyance mechanism


50


can be a drum, an x, y, z translator, any other known media conveyance mechanism, etc.




Referring to

FIGS. 1D and 1E

, the formulation reservoir


12


can be a pressurized vessel having appropriate inlet ports


52


,


54


,


56


and outlet ports


58


. Inlet ports


52


,


54


,


56


can be used as an inlet for functional material


52


and an inlet for compressed liquid or supercritical fluid


54


. Alternatively, inlet port


56


can be used to manually add functional material to the formulation reservoir


12


. Outlet port


58


can be used as an outlet for the mixture of functional material and compressed/supercritical fluid.




When automated delivery of the functional material is desired, a pump


60


is positioned along a functional material delivery path


62


between a source of functional material


64


and the formulation reservoir


12


. The pump


60


pumps a desired amount of functional material through inlet port


52


into the formulation reservoir


12


. The formulation reservoir


12


can also include additional inlet/outlet ports


59


for inserting or removing small quantities of functional material or functional material and compressed liquid/supercritical fluid mixtures.




Referring to

FIGS. 1D and 1E

, the formulation reservoir


12


can include a mixing device


70


used to create the mixture of functional material and compressed liquid/supercritical fluid. Although typical, a mixing device


70


is not always necessary to make the mixture of the functional material and compressed/supercritical fluid depending on the type of functional material and the type of compressed liquid/supercritical fluid. The mixing device


70


can include a mixing element


72


connected to a power/control source


74


to ensure that the functional material disperses into or forms a solution with the compressed liquid or supercritical fluid. The mixing element


72


can be an acoustic, a mechanical, and/or an electromagnetic element.




Referring to

FIGS. 1D

,


1


E, and

FIGS. 4A-4J

, the formulation reservoir


12


can also include suitable temperature control mechanisms


20


and pressure control mechanisms


17


with adequate gauging instruments to detect and monitor the temperature and pressure conditions within the reservoir, as described above. For example, the formulation reservoir


12


can include a moveable piston device


76


, etc., to control and maintain pressure. The formulation reservoir


12


can also be equipped to provide accurate control over temperature within the reservoir. For example, the formulation reservoir


12


can include electrical heating/cooling zones


78


, using electrical wires


80


, electrical tapes, water jackets


82


, other heating/cooling fluid jackets, refrigeration coils


84


, etc., to control and maintain temperature. The temperature control mechanisms


20


can be positioned within the formulation reservoir


12


or positioned outside the formulation reservoir. Additionally, the temperature control mechanisms


20


can be positioned over a portion of the formulation reservoir


12


, throughout the formulation reservoir


12


, or over the entire area of the formulation reservoir


12


.




Referring to

FIG. 4K

, the formulation reservoir


12


can also include any number of suitable high-pressure windows


86


for manual viewing or digital viewing using an appropriate fiber optics or camera set-up. The windows


86


are typically made of sapphire or quartz or other suitable materials that permit the passage of the appropriate frequencies of radiation for viewing/detection/analysis of reservoir contents (using visible, infrared, X-ray etc. viewing/detection/analysis techniques), etc.




The formulation reservoir


12


is made of appropriate materials of construction in order to withstand high pressures of the order of 10,000 psi or greater. Typically, stainless steel is the preferred material of construction although other high pressure metals, metal alloys, and/or metal composites can be used.




Referring to

FIG. 1F

, in an alternative arrangement, the thermodynamically stable/metastable mixture of functional material and compressed liquid/supercritical fluid can be prepared in one formulation reservoir


12


and then transported to one or more additional formulation reservoirs


12




a


. For example, a single large formulation reservoir


12


can be suitably connected to one or more subsidiary high pressure vessels


12




a


that maintain the functional material and compressed liquid/supercritical fluid mixture at controlled temperature and pressure conditions with each subsidiary high pressure vessel


12




a


feeding one or more discharge devices


13


. Either or both reservoirs


12


and


12




a


can be equipped with the temperature control mechanism


20


and/or pressure control mechanisms


17


. The discharge devices


13


can direct the mixture towards a single receiver


14


or a plurality of receivers


14


.




Referring to

FIG. 1G

, the delivery system


10


can include ports for the injection of suitable functional material, view cells, and suitable analytical equipment such as Fourier Transform Infrared Spectroscopy, Light Scattering, UltraViolet or Visible Spectroscopy, etc. to permit monitoring of the delivery system


13


and the components of the delivery system. Additionally, the delivery system


10


can include any number of control devices


88


, microprocessors


90


, etc., used to control the delivery system


10


.




Referring to

FIG. 2A

, the discharge device


13


is described in more detail. The discharge assembly can include an on/off valve


21


that can be manually or automatically actuated to regulate the flow of the supercritical fluid or compressed liquid formulation. The discharge device


13


includes a shutter device


22


which can also be a programmable valve. The shutter device


22


is capable of being controlled to turn off the flow and/or turn on the flow so that the flow of formulation occupies all or part of the available cross-section of the discharge device


13


. Additionally, the shutter device is capable of being partially opened or closed in order to adjust or regulate the flow of formulation. The discharge assembly also includes a nozzle


23


. The nozzle


23


can be provided, as necessary, with a nozzle heating module


26


and a nozzle shield gas module


27


to assist in beam collimation. The discharge device


13


also includes a stream deflector and/or catcher module


24


to assist in beam collimation prior to the beam reaching a receiver


25


. Components


22


-


24


,


26


, and


27


of discharge device


13


are positioned relative to delivery path


16


such that the formulation continues along delivery path


16


.




Alternatively, the shutter device


22


can be positioned after the nozzle heating module


26


and the nozzle shield gas module


27


or between the nozzle heating module


26


and the nozzle shield gas module


27


. Additionally, the nozzle shield gas module


27


may not be required for certain applications, as is the case with the stream deflector and catcher module


24


. Alternatively, discharge device


13


can include a stream deflector and catcher module


24


and not include the shutter device


22


. In this situation, the stream deflector and catcher module


24


can be moveably positioned along delivery path


16


and used to regulate the flow of formulation such that a continuous flow of formulation exits while still allowing for discontinuous deposition and/or etching.




The nozzle


23


can be capable of translation in x, y, and z directions to permit suitable discontinuous and/or continuous functional material deposition and/or etching on the receiver


14


. Translation of the nozzle can be achieved through manual, mechanical, pneumatic, electrical, electronic or computerized control mechanisms. Receiver


14


and/or media conveyance mechanism


50


can also be capable of translation in x, y, and z directions to permit suitable functional material deposition and/or etching on the receiver


14


. Alternatively, both the receiver


14


and the nozzle


23


can be translatable in x, y, and z directions depending on the particular application.




Referring to

FIGS. 2B-2M

, the nozzle


23


functions to direct the formulation flow towards the receiver


14


. It is also used to attenuate the final velocity with which the functional material impinges on the receiver


14


. Accordingly, nozzle geometry can vary depending on a particular application. For example, nozzle geometry can be a constant area having a predetermined shape (cylinder


28


, square


29


, triangular


30


, etc.) or variable area converging


31


, variable area diverging


38


, or variable area converging-diverging


32


, with various forms of each available through altering the angles of convergence and/or divergence. Alternatively, a combination of a constant area with a variable area, for example, a converging-diverging nozzle with a tubular extension, etc., can be used. In addition, the nozzle


23


can be coaxial, axisymnmetric, asymmetric, or any combination thereof (shown generally in


33


). The shape


28


,


29


,


30


,


31


,


32


,


33


of the nozzle


23


can assist in regulating the flow of the formulation. In a preferred embodiment of the present invention, the nozzle


23


includes a converging section or module


34


, a throat section or module


35


, and a diverging section or module


36


. The throat section or module


35


of the nozzle


23


can have a straight section or module


37


.




The discharge device


13


serves to direct the functional material onto the receiver


14


. The discharge device


13


or a portion of the discharge device


13


can be stationary or can swivel or raster, as needed, to provide high resolution and high precision deposition of the functional material onto the receiver


14


or etching of the receiver


14


by the functional material. Alternatively, receiver


14


can move in a predetermined way while discharge device


13


remains stationary. The shutter device


22


can also be positioned after the nozzle


23


. As such, the shutter device


22


and the nozzle


23


can be separate devices so as to position the shutter


22


before or after the nozzle


23


with independent controls for maximum deposition and/or etching flexibility. Alternatively, the shutter device


22


can be integrally formed within the nozzle


23


.




Operation of the delivery system


10


will now be described.

FIGS. 3A-3D

are diagrams schematically representing the operation of delivery system


10


and should not be considered as limiting the scope of the invention in any manner. A formulation


42


of functional material


40


in a supercritical fluid and/or compressed liquid


41


is prepared in the formulation reservoir


12


. A functional material


40


, any material of interest in solid or liquid phase, can be dispersed (as shown in

FIG. 3A

) and/or dissolved in a supercritical fluid and/or compressed liquid


41


making a mixture or formulation


42


. The functional material


40


can have various shapes and sizes depending on the type of the functional material


40


used in the formulation.




The supercritical fluid and/or compressed liquid


41


, forms a continuous phase and functional material


40


forms a dispersed and/or dissolved single phase. The formulation


42


(the functional material


40


and the supercritical fluid and/or compressed liquid


41


) is maintained at a suitable temperature and a suitable pressure for the functional material


40


and the supercritical fluid and/or compressed liquid


41


used in a particular application. The shutter


22


is actuated to enable the ejection of a controlled quantity of the formulation


42


. The nozzle


23


collimates and/or focuses the formulation


42


into a beam


43


.




The functional material


40


is controllably introduced into the formulation reservoir


12


. The compressed liquid/supercritical fluid


41


is also controllably introduced into the formulation reservoir


12


. The contents of the formulation reservoir


12


are suitably mixed using mixing device


70


to ensure intimate contact between the functional material


40


and compressed liquid/supercritical fluid


41


. As the mixing process proceeds, functional material


40


is dissolved or dispersed within the compressed liquid/supercritical fluid


41


. The process of dissolution/dispersion, including the amount of functional material


40


and the rate at which the mixing proceeds, depends upon the functional material


40


itself, the particle size and particle size distribution of the functional material


40


(if the functional material


40


is a solid), the compressed liquid/supercritical fluid


41


used, the temperature, and the pressure within the formulation reservoir


12


. When the mixing process is complete, the mixture or formulation


42


of functional material and compressed liquid/supercritical fluid is thermodynamically stable/metastable in that the functional material is dissolved or dispersed within the compressed liquid/supercritical fluid in such a fashion as to be indefinitely contained in the same state as long as the temperature and pressure within the formulation chamber are maintained constant. This state is distinguished from other physical mixtures in that there is no settling, precipitation, and/or agglomeration of functional material particles within the formulation chamber unless the thermodynamic conditions of temperature and pressure within the reservoir are changed. As such, the functional material


40


and compressed liquid/supercritical fluid


41


mixtures or formulations


42


of the present invention are said to be thermodynamically stable/metastable.




The functional material


40


can be a solid or a liquid. Additionally, the functional material


40


can be an organic molecule, a polymer molecule, a metallo-organic molecule, an inorganic molecule, an organic nanoparticle, a polymer nanoparticle, a metallo-organic nanoparticle, an inorganic nanoparticle, an organic microparticles, a polymer micro-particle, a metallo-organic microparticle, an inorganic microparticle, and/or composites of these materials, etc. After suitable mixing with the compressed liquid/supercritical fluid


41


within the formulation reservoir


12


, the functional material


40


is uniformly distributed within a thermodynamically stable/metastable mixture, that can be a solution or a dispersion, with the compressed liquid/supercritical fluid


41


. This thermodynamically stable/metastable mixture or formulation


42


is controllably released from the formulation reservoir


12


through the discharge device


13


.




During the discharge process, the functional material


40


is precipitated from the compressed liquid/supercritical fluid


41


as the temperature and/or pressure conditions change. The precipitated functional material


44


is directed towards a receiver


14


by the discharge device


13


as a focussed and/or collimated beam. The particle size of the functional material


40


deposited on the receiver


14


is typically in the range from 1 nanometer to 1000 nanometers. The particle size distribution may be controlled to be uniform by controlling the rate of change of temperature and/or pressure in the discharge device


13


, the location of the receiver


14


relative to the discharge device


13


, and the ambient conditions outside of the discharge device


13


.




The delivery system


10


is also designed to appropriately change the temperature and pressure of the formulation


42


to permit a controlled precipitation and/or aggregation of the functional material


40


. As the pressure is typically stepped down in stages, the formulation


42


fluid flow is self-energized. Subsequent changes to the formulation


42


conditions (a change in pressure, a change in temperature, etc.) result in the precipitation and/or aggregation of the functional material


40


coupled with an evaporation (shown generally at


45


) of the supercritical fluid and/or compressed liquid


41


. The resulting precipitated and/or aggregated functional material


44


deposits on the receiver


14


in a precise and accurate fashion. Evaporation


45


of the supercritical fluid and/or compressed liquid


41


can occur in a region located outside of the discharge device


13


. Alternatively, evaporation


45


of the supercritical fluid and/or compressed liquid


41


can begin within the discharge device


13


and continue in the region located outside the discharge device


13


. Alternatively, evaporation


45


can occur within the discharge device


13


.




A beam


43


(stream, etc.) of the functional material


40


and the supercritical fluid and/or compressed liquid


41


is formed as the formulation


42


moves through the discharge device


13


. When the size of the precipitated and/or aggregated functional material


44


is substantially equal to an exit diameter of the nozzle


23


of the discharge device


13


, the precipitated and/or aggregated functional material


44


has been collimated by the nozzle


23


. When the size of the precipitated and/or aggregated functional material


44


is less than the exit diameter of the nozzle


23


of the discharge device


13


, the precipitated and/or aggregated functional material


44


has been focused by the nozzle


23


.




The receiver


14


is positioned along the path


16


such that the precipitated and/or aggregated functional material


44


is deposited on the receiver


14


. Alternatively, the precipitated and/or aggregated functional material


44


can remove a portion of the receiver


14


. Whether the precipitated and/or aggregated functional material


44


is deposited on the receiver


14


or removes a portion of the receiver


14


will, typically, depend on the type of functional material


40


used in a particular application.




The distance of the receiver


14


from the discharge assembly is chosen such that the supercritical fluid and/or compressed liquid


41


evaporates from the liquid and/or supercritical phase to the gas phase (shown generally at


45


) prior to reaching the receiver


14


. Hence, there is no need for subsequent receiver-drying processes. Further, subsequent to the ejection of the formulation


42


from the nozzle


23


and the precipitation of the functional material, additional focusing and/or collimation may be achieved using external devices such as electromagnetic fields, mechanical shields, magnetic lenses, electrostatic lenses etc. Alternatively, the receiver


14


can be electrically or electrostatically charged such that the position of the functional material


40


can be controlled.




It is also desirable to control the velocity with which individual particles


46


of the functional material


40


are ejected from the nozzle


23


. As there is a sizable pressure drop from within the delivery system


10


to the operating environment, the pressure differential converts the potential energy of the delivery system


10


into kinetic energy that propels the functional material particles


46


onto the receiver


14


. The velocity of these particles


46


can be controlled by suitable nozzle design and control over the rate of change of operating pressure and temperature within the system. Further, subsequent to the ejection of the formulation


42


from the nozzle


23


and the precipitation of the functional material


40


, additional velocity regulation of the functional material


40


may be achieved using external devices such as electromagnetic fields, mechanical shields, magnetic lenses, electrostatic lenses etc. Nozzle design and location relative to the receiver


14


also determine the pattern of functional material


40


deposition. The actual nozzle design will depend upon the particular application addressed.




The nozzle


23


temperature can also be controlled. Nozzle temperature control may be controlled as required by specific applications to ensure that the nozzle opening


47


maintains the desired fluid flow characteristics. Nozzle temperature can be controlled through the nozzle heating module


26


using a water jacket, electrical heating techniques, etc. With appropriate nozzle design, the exiting stream temperature can be controlled at a desired value by enveloping the exiting stream with a co-current annular stream of a warm or cool, inert gas, as shown in FIG.


2


G.




The receiver


14


can be any solid including an organic, an inorganic, a metallo-organic, a metallic, an alloy, a ceramic, a synthetic and/or natural polymeric, a gel, a glass, and a composite material. The receiver


14


can be porous or non-porous. Additionally, the receiver


14


can have more than one layer.




The invention has been described in detail with particular reference to certain preferred embodiments thereof, but it will be understood that variations. and modifications can be effected within the spirit and scope of the invention.



Claims
  • 1. An apparatus for focusing a functional material comprising:a pressurized source of a thermodynamically stable mixture of a fluid and the functional material; and a discharge device having an inlet and an outlet, the discharge device being connected to the pressurized source at the inlet, the discharge device being shaped to produce a collimated beam of the functional material, wherein the fluid is in a gaseous state at a location beyond the outlet of the discharge device.
  • 2. The apparatus according to claim 1, wherein the fluid is a compressed liquid.
  • 3. The apparatus according to claim 1, wherein the fluid is a supercritical fluid.
  • 4. The apparatus according to claim 1, wherein the thermodynamically stable mixture includes the functional material being dispersed in the fluid.
  • 5. The apparatus according to claim 1, wherein the thermodynamically stable mixture includes the functional material being dissolved in the fluid.
  • 6. The apparatus according to claim 1, the fluid having a temperature and a pressure, wherein the discharge device includes one of a heating mechanism and a cooling mechanism selectively actuated to control at least one of the temperature and the pressure of the fluid.
  • 7. The apparatus according to claim 1, wherein the discharge device includes a nozzle having a variable area portion.
  • 8. The apparatus according to claim 1, wherein the discharge device includes a nozzle having a constant area portion.
  • 9. The apparatus according to claim 8, wherein the nozzle includes a variable area portion.
  • 10. The apparatus according to claim 1, wherein the discharge device includes a nozzle having a nozzle shield gas module.
  • 11. The apparatus according to claim 1, portions of the discharge device defining a path, wherein the discharge device includes a shutter device, the shutter device having a first position removed from the path and a second position in the path thereby controlling an amount of mixture travelling through the discharge device.
  • 12. The apparatus according to claim 11, wherein the discharge device includes a nozzle, the shutter being integrally formed within the nozzle.
  • 13. The apparatus according to claim 1, the functional material travelling along a path, the apparatus comprising:a receiver positioned at a distance removed from the path such that the functional material contacts the receiver.
  • 14. The apparatus according to claim 13, wherein the distance is between about 1 mm to about 50 cm.
  • 15. The apparatus according to claim 13, wherein the receiver is. one of a porous and non-porous material.
  • 16. The apparatus according to claim 13, wherein the receiver has at least one layer.
  • 17. The apparatus according to claim 13, wherein the receiver is a solid selected from the group consisting of an organic, an inorganic, a metallo-organic, a polymeric, a metal, an alloy, a ceramic, a synthetic, a natural polymer, a gel, a glass, and a composite material.
  • 18. The apparatus according to claim 13, wherein the functional material is deposited on the receiver.
  • 19. The apparatus according to claim 13, wherein the functional material includes a material operable to remove a portion of the receiver.
  • 20. The apparatus according to claim 1, wherein a particle size of the functional material is between 1 nanometer and 1000 nanometers.
  • 21. The apparatus according to claim 1, wherein the pressurized source of the thermodynamically stable mixture of the fluid and the functional material is a formulation reservoir, the apparatus further comprising:a source of fluid connected to the formulation reservoir.
  • 22. The apparatus according to claim 21, further comprising:a pump positioned between the source of fluid and the formulation reservoir.
  • 23. The apparatus according to claim 22, wherein the pump is a high-pressure pump.
  • 24. The apparatus according to claim 1, wherein the pressurized source of the thermodynamically stable mixture of the fluid and the functional material is a formulation reservoir, the apparatus further comprising:a temperature and pressure regulation system operably connected to the formulation reservoir such that a predetermined operating condition is maintained in the formulation reservoir.
  • 25. The apparatus according to claim 24, wherein the temperature and pressure regulation system includes a piston, the piston being moveable such that the pressure is maintained in the formulation reservoir.
  • 26. The apparatus according to claim 24, wherein the temperature and pressure regulation system includes at least one of a heating and cooling mechanism.
  • 27. The apparatus according to claim 26 wherein the temperature and pressure regulation system includes at least one of an electrical wire, a water jacket, and a refrigeration coil.
  • 28. The apparatus according to claim 1, wherein the pressurized source of the thermodynamically stable mixture of the fluid and the functional material is a formulation reservoir, the apparatus further comprising:a mixing device at least partially positioned within the formulation reservoir, the mixing device being operable to form the thermodynamically stable mixture of the functional material and the fluid.
  • 29. The apparatus according to claim 28, wherein the mixing device is one of an electromagnetic system, a mechanical system, and an acoustic system.
  • 30. The apparatus according to claim 1, wherein the pressurized source of the thermodynamically stable mixture of the fluid and the functional material is a formulation reservoir, the apparatus further comprising:a source of functional material connected to the formulation reservoir.
  • 31. The apparatus according to claim 30, further comprising:a pump positioned between the source of functional material and the formulation reservoir.
  • 32. The apparatus according to claim 1, wherein the functional material is one of a liquid and a solid.
  • 33. The apparatus according to claim 32, wherein the functional material is selected from the group consisting of an organic molecule, a polymer molecule, a metallo-organic molecule, an inorganic molecule, an organic nanoparticle, a polymer nanoparticle, a metallo-organic nanoparticle, an inorganic nanoparticle, an organic microparticles, a polymer micro-particle, a metallo-organic microparticle, an inorganic microparticle, and a composite material.
  • 34. The apparatus according to claim 1, wherein the functional material includes a first material and a second material.
  • 35. The apparatus according to claim 1, further comprising:a plurality of discharge devices connected to the source.
  • 36. The apparatus according to claim 1, wherein the discharge device is shaped to produce a focused beam.
  • 37. The apparatus according to claim 1, wherein the thermodynamically stable mixture of the fluid and the functional material is thermodynamically metastable.
  • 38. A method of delivering a functional material comprising:providing a pressurized source of a thermodynamically stable mixture of a fluid and the functional material; and causing the functional material to collimate, wherein the fluid is in a gaseous state at a location beyond an outlet of the discharge device.
  • 39. The method according to claim 38, wherein causing the functional material to collimate includes discharging the mixture through a discharge device shaped to produce a collimated beam of functional material.
  • 40. The method according to claim 39, wherein discharging the mixture includes controlling the discharge such that a predetermined amount of functional material is released.
  • 41. The method according to claim 38, wherein the fluid is a compressed liquid.
  • 42. The method according to claim 38, wherein the fluid is a supercritical fluid.
  • 43. The method according to claim 38, wherein the functional material is dissolved in the fluid.
  • 44. The method according to claim 38, wherein the functional material is dispersed in the fluid.
  • 45. The method according to claim 38, wherein causing the functional material to collimate includes focusing the functional material.
  • 46. The method according to claim 38, further comprising:delivering the functional material to a receiver.
  • 47. The method according to claim 46, further comprising: depositing the functional material on the receiver.
  • 48. The method according to claim 46, further comprising: using the functional material to remove a portion of the receiver.
  • 49. An apparatus for delivering a beam of a functional material comprising:a pressurized source of a thermodynamically stable mixture of a fluid and the functional material; and a discharge device having an inlet and an outlet, the discharge device being connected to the pressurized source at the inlet, the discharge device including a variable area portion and a constant area portion, wherein a collimated beam of functional material is produced as the mixture moves from the inlet of the discharge device through the outlet of the discharge device, the fluid being in a gaseous state at a location relative to the discharge device.
  • 50. The apparatus according to claim 49, wherein the location is positioned within a region of the discharge device.
  • 51. The apparatus according to claim 49, wherein the location is positioned in a region beyond the discharge device.
  • 52. The apparatus according to claim 49, wherein the variable area portion has a converging shape.
  • 53. The apparatus according to claim 52, wherein the constant area portion has a circular cross section.
  • 54. The apparatus according to claim 49, wherein the variable area portion has a converging shape and diverging shape.
  • 55. The apparatus according to claim 54, wherein the constant area portion has a circular cross section.
  • 56. The apparatus according to claim 49, wherein the variable area portion has a diverging shape.
  • 57. The apparatus according to claim 56, wherein the constant area portion has a circular cross section.
  • 58. The apparatus according to claim 49, wherein the constant area portion has a circular cross section.
  • 59. The apparatus according to claim 49, wherein the fluid is a compressed liquid.
  • 60. The apparatus according to claim 49, wherein the fluid is a supercritical fluid.
  • 61. The apparatus according to claim 49, wherein the thermodynamically stable mixture includes the functional material being dispersed in the fluid.
  • 62. The apparatus according to claim 49, wherein the thermodynamically stable mixture includes the functional material being dissolved in the fluid.
  • 63. The apparatus according to claim 49, further comprising:a source of fluid; and a high pressure pump connected to the source of fluid and the pressurized source of the thermodynamically stable mixture of the fluid and the functional material.
  • 64. The apparatus according to claim 63, further comprising:a receiver positioned relative to the discharge device such that the functional material is deposited on the receiver.
  • 65. The apparatus according to claim 49, further comprising:a shutter device positioned between the pressurized source and the outlet of the discharge device, the shutter device being moveable between an open position and a closed position such that release of the functional material is controlled.
  • 66. The apparatus according to claim 49, wherein the pressurized source of the thermodynamically stable mixture of the fluid and the functional material is a formulation reservoir, the apparatus further comprising:a temperature and pressure regulation system operably connected to the formulation reservoir such that a predetermined operating condition is maintained in the formulation reservoir.
  • 67. The apparatus according to claim 66, wherein the temperature and pressure regulation system includes a piston, the piston being moveable such that the pressure is maintained in the formulation reservoir.
  • 68. The apparatus according to claim 66, wherein the temperature and pressure regulation system includes at least one of a heating and a cooling mechanism.
  • 69. The apparatus according to claim 49, wherein the pressurized source of the thermodynamically stable mixture of the fluid and the functional material is a formulation reservoir, the apparatus further comprising:a mixing device at least partially positioned within the formulation reservoir, the mixing device being operable to form the thermodynamically stable mixture of the functional material and the fluid.
  • 70. The apparatus according to claim 69, wherein the mixing device is one of an electromagnetic system, a mechanical system, and an acoustic system.
  • 71. The apparatus according to claim 49, wherein the pressurized source of the thermodynamically stable mixture of the fluid and the functional material is a formulation reservoir, the apparatus further comprising:a source of functional material connected to the formulation reservoir.
  • 72. The apparatus according to claim 71, further comprising:a pump positioned between the source of functional material and the formulation reservoir.
  • 73. A method of delivering a functional material comprising:providing one of a compressed liquid and a supercritical fluid in a first predetermined thermodynamic state; adding the functional material to one of the compressed liquid and the supercritical fluid; and moving the functional material and one of the compressed liquid and the supercritical fluid to a second thermodynamic state, whereby one of the compressed liquid and the supercritical fluid evaporates allowing the functional material to release in a collimated beam.
  • 74. The method according to claim 73, wherein moving one of the compressed liquid and the supercritical fluid and the functional material to a second thermodynamic state includes focusing the functional material.
  • 75. An apparatus for delivering a functional material comprising:a pressurized source of a thermodynamically stable mixture of a fluid and the functional material; and a discharge device having an inlet and an outlet, the discharge device being connected to the pressurized source at the inlet, the discharge device being shaped to produce a beam of functional material, wherein the fluid is in a gaseous state at a location beyond the outlet of the discharge device.
  • 76. The apparatus according to claim 75, wherein the fluid is a compressed liquid.
  • 77. The apparatus according to claim 75, wherein the fluid is a supercritical fluid.
  • 78. The apparatus according to claim 75, wherein the thermodynamically stable mixture includes the functional material being dispersed in the fluid.
  • 79. The apparatus according to claim 75, wherein the thermodynamically stable mixture includes the functional material being dissolved in the fluid.
  • 80. The apparatus according to claim 75, wherein the discharge device includes a nozzle having a constant area portion.
  • 81. The apparatus according to claim 80, wherein the nozzle includes a variable area portion.
  • 82. The apparatus according to claim 75, wherein the discharge device includes a nozzle having a variable area portion.
  • 83. The apparatus according to claim 82, wherein the variable area portion includes a converging portion and a diverging portion.
  • 84. The apparatus according to claim 75, wherein the discharge device is shaped to produce a focused beam of functional material.
US Referenced Citations (5)
Number Name Date Kind
4555712 Arway et al. Nov 1985 A
4734227 Smith Mar 1988 A
5020774 Christianson Jun 1991 A
5178325 Nielsen Jan 1993 A
6116718 Peeters et al. Sep 2000 A
Foreign Referenced Citations (2)
Number Date Country
11-319618 Nov 1999 JP
WO 9919080 Apr 1999 WO