System for producing patterned deposition from compressed fluid in a partially opened deposition chamber

Information

  • Patent Grant
  • 6780249
  • Patent Number
    6,780,249
  • Date Filed
    Friday, December 6, 2002
    22 years ago
  • Date Issued
    Tuesday, August 24, 2004
    20 years ago
Abstract
A system (10) produces patterned deposition on a substrate (14) from supercritical fluids. A delivery system (12) cooperates with a partial enclosure environment (30, 100, 200) retaining a movable substrate (14) for receiving precipitated functional material (44) along a fluid delivery path (13) from the delivery system (12). A shadow mask (22) is arranged in close proximity to the movable substrate (14) for forming the patterned deposition on the movable substrate (14).
Description




FIELD OF THE INVENTION




This invention relates generally to deposition from compressed fluids and, more particularly, to patterned deposition from compressed fluids onto suitable substrates with the use of masks.




BACKGROUND OF THE INVENTION




Processes that enable patterned deposition of materials onto a substrate have a number of applications, especially in the electronic microcircuit industry. Microfabrication of electronic circuits relies on the ability to create multi-layer patterns of numerous functional materials, with varying electrical properties. The technologies used for creating these multi-layer patterns may be additive, subtractive, or a combination of the two. Additive technologies deposit the functional material on the substrate in the desired pattern, i.e., the pattern is generated directly on the substrate during the deposition/layering process. Subtractive processes, on the other hand, first create a continuous layer of the functional material on the substrate. The desired pattern is then subsequently created by the selective removal of functional material from the deposited layer, i.e., the pattern is created subsequent to the deposition/layering process. A detailed description of various patterned deposition/layering processes used in the microfabrication industry may be found in “Physics of Micro/Nano-Fabrication” by Ivor Brodie and Julius J. Murray, Plenum Press, NY, 1992.




Traditional micro-fabrication processes utilize either or both the additive and subtractive processes depending upon the specific application, and are generally carried out in a high vacuum (low-pressure) environment. The high vacuum process generally involves the evaporation of functional material by heating or by ion bombardment followed by deposition onto the substrate by condensation or by a chemical reaction. In these deposition processes, the functional material is required to be thermally stable or to have a thermally stable precursor that can generate the functional material on the substrate by a chemical reaction. As skilled artisans will appreciate, these processes are not useful in generating patterned layers of thermally unstable materials.




Further, those skilled in the art will appreciate that it is common to use a mask technique for patterned deposition. Typically, the mask employed for patterning on a planar substrate surface is a photoresist material. However, when the surface is nonplanar, difficulties can be encountered in depositing and cleaning off the photoresist material, necessitating the use of shadow masks or stencils. For example, U.S. Pat. No. 4,218,532 titled “Photolithographic Technique For Depositing Thin Films,” issued Aug. 19, 1980 to Dunkleberger discloses a method for patterned deposition of thin films of metals, such as lead alloys, by vacuum evaporation onto a substrate through openings in a mask fabricated with a predetermined pattern. A shortcoming of this development is that it cannot be used for the patterned deposition of thermally unstable materials since these are not suitable for vacuum evaporation.




In U.S. Pat. No. 4,013,502 titled “Stencil Process For High Resolution Pattern Replication,” issued Mar. 22, 1977 to Staples, a process for obtaining high-resolution pattern replication using stencils is disclosed. The stencil in Staples is a mask effecting molecular beam deposition of thin films onto a substrate through openings in the stencil. In this deposition process, the molecular beam source is an electron-beam evaporator. Much like the Dunkleberger development, a shortcoming of Staples' technology is that it cannot be used for patterned deposition of thermally unstable materials that are not suitable for evaporation using an electron beam evaporator.




Furthermore, it is well known that patterned deposition of thermally unstable materials on substrates may be achieved by liquid phase processes such as electroplating electrophoresis, sedimentation, or spin coating but these processes are system specific. For example, in the case of electroplating, it is necessary that an electrochemically active solution of the functional material precursor is available. In the case of sedimentation and spin coating, a stable colloidal dispersion is necessary. In the case of electrophoresis, it is also necessary that the stable colloidal dispersion be charged. Microfabrication of multi-layer structures usually requires multiple stages, necessitating the complete removal of residual liquids/solvents at the end of every stage, which can be very energy, time, and cost intensive. Further, many of these liquid-based processes require the use of non-aqueous liquids/solvents, which are hazardous to health and the disposal of which can be prohibitively expensive. For example, in U.S. Pat. No. 5,545,307 titled “Process For Patterned Electroplating,” issued Aug. 13, 1996 to Doss et al., a process is disclosed for patterned electroplating of metals onto a substrate


14


through a mask. The Doss et al. process, however, has at least two major shortcomings. First, it is only applicable to materials that have electrochemically active precursors. Second, it uses an aqueous electroplating bath for the process that requires the coated substrate be cleaned and then dried at the end of the coating process.




Moreover, it is well known that to eliminate the need for potentially harmful solvents that need drying, it is possible to use environmental and health-benign supercritical fluids such as carbon dioxide as solvents. For example, in U.S. Pat. No. 4,737,384 titled “Deposition Of Thin Films Using Supercritical Fluids,” issued Apr. 12, 1988 to Murthy et al., a process is disclosed for depositing thin films of materials that are soluble in supercritical fluids onto a substrate. Murthy et al. include the steps of exposing a substrate at supercritical temperatures and pressures to a solution comprising a metal or polymer dissolved in water or a non-polar organic solvent. The metal or polymer is substantially insoluble in the solvent under sub-critical conditions and is substantially soluble in the solvent under supercritical conditions. Reducing the pressure alone, or temperature and pressure together, to sub-critical values cause the deposition of a thin coating of the metal or polymer onto the substrate. Nonetheless, a shortcoming of the process of Murthy et al. is its limited applicability to materials that can be dissolved in compressed fluids, severely limiting the choice of materials that can be deposited on a substrate using this technology. Another shortcoming of the process of Murthy et al. is that it does not teach a process for the patterned deposition of functional materials.




In U.S. Pat. No. 4,582,731 titled “Supercritical Fluid Molecular Spray Film Deposition and Powder Formation,” issued Apr. 15, 1986 to Smith, and U.S. Pat. No. 4,734,227 titled “Method Of Making Supercritical Fluid Molecular Spray Films, Powder And Fibers,” issued Mar. 29, 1988 to Smith, independent processes are disclosed for producing solid films on a substrate by dissolving a solid material into supercritical fluid solution at an elevated pressure. In both cases, the supercritical fluid solution is then rapidly expanded in a region of relatively low pressure through a heated nozzle having a relatively short orifice. Both of the aforementioned Smith processes have similar shortcomings to those indicated above, i.e., they are only applicable to materials that are soluble in compressed fluids and do not teach a process for patterned deposition.




Therefore, a need persists in the art for a patterned deposition system that permits the patterned deposition of thermally unstable/labile materials and that eliminates the use of expensive and both environmentally and human health-hazardous solvents. A further need exists for a patterned deposition system that eliminates the need for post-deposition drying for solvent-elimination. Moreover, there is an additional need for a patterned deposition technique that is applicable for a wide range of functional materials and that is not limited by specific properties of the functional materials.




SUMMARY OF THE INVENTION




It is, therefore, an object of the invention to provide a coating deposition system that permits the patterned deposition of thermally unstable/labile materials.




Another object of the invention is to provide a coating deposition system that eliminates the need for post-deposition drying for solvent elimination.




Yet another object of the invention is to provide a coating deposition system that is applicable for a wide range of functional materials.




To achieve these and other objects and advantages of the invention, there is provided, in one aspect of the invention, a system for producing patterned deposition from compressed fluids. The system includes a means for delivering a functional material that is dissolved and/or dispersed in a compressed fluid and then precipitating the functional material by decompressing the compressed fluid to a state where the functional material is no longer soluble and/or dispersible in the compressed fluid. A controlled environment retains a substrate bearing a shadow mask. The controlled environment exposes the substrate bearing the shadow mask to receive precipitated functional material as a patterned deposition on the substrate.




There are numerous advantageous effects of the present invention over prior developments. More particularly, the present system has the ability to deposit thermally unstable/labile materials and is useful for a wider range of materials unlike prior art developments. Further, the present system is considerably more efficient and controllable than existing systems. Moreover, the present invention eliminates the need for harmful and expensive materials used for drying.











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. 1

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





FIG. 2

is enlarged schematic view of a controlled environment in one embodiment of the invention;





FIG. 3

is a schematic view of an alternative embodiment of an enclosure of the invention





FIG. 4

is a diagram schematically representing the operation of the present invention;





FIG. 5

is a schematic view of an alternative embodiment of a controlled environment or deposition chamber useful in the invention; and,





FIG. 6

is a schematic view of an alternative embodiment of another controlled environment or deposition chamber useful in the invention.











DETAILED DESCRIPTION OF THE INVENTION




Turning now to the drawings, and more particularly to

FIG. 1

, system


10


, broadly defined, for producing patterned deposition from compressed fluids includes a delivery system


12


, a deposition chamber, or alternatively controlled environment,


30


, and a substrate


14


retained in the deposition chamber, or alternatively, controlled environment


30


. Controlled environment


30


is more typically a deposition chamber, as described in detail below. A typical delivery system


12


contemplated by the invention is one disclosed, for instance, in commonly assigned in U.S. Patent Application Publication No. 2002/01184245A1 titled “Apparatus And Method Of Delivering A Focused Beam Of A Thermodynamically Stable/Metastable Mixture Of A Function Material In A Dense Fluid Onto A Receiver,” by Ramesh Jagannathan, published Aug. 29, 2002, hereby incorporated herein by reference. Each of the disclosed delivery systems is capable of delivering a precipitate functional material (as described below) and can be used in the invention.




Referring to

FIG. 1

, delivery system


12


, capable of delivering fluids along fluid delivery path


13


in a compressed state, generally includes a source


16


of compressed fluid, a formulation reservoir


18


for containing a formulation material, a discharge assembly


20


, each being described in detail in the above U.S. Patent Applications. Delivery system


12


serves several important functions in the invention. It enables the dissolution and/or dispersal of a selected material into a compressed fluid with density greater than 0.1 g/cc


3


. Further, a solution and/or dispersion of an appropriate functional material or combination of functional materials in the chosen compressed fluid is produced in delivery system


12


. Moreover, delivery system


12


delivers the functional materials as a beam or spray into a deposition chamber


30


in a controlled manner. In this context, the chosen materials taken to a compressed fluid state with a density greater than 0.1 g/cc


3


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.




As depicted in

FIG. 1

, controlled environment


30


, such as a deposition chamber, is arranged proximate to delivery system


12


. Controlled environment


30


is positioned at one end of the fluid delivery path


13


and adjacent the discharge assembly


20


of delivery system


12


. As illustrated in

FIG. 2

, substrate


14


to be patterned with deposition material and is suitably arranged within deposition chamber


30


. In close proximity to substrate


14


, a mask


22


is preferably used (but not required) to control the location of the deposited functional material on the substrate


14


.




Referring to

FIG. 3

, in many applications, it is desirable to maintain an exact concentration of functional material within the controlled enclosure


31


. Whilst open loop systems relying on valve opening times can be used, for greater precision and reliability it is desirable to use a system such as the one illustrated in FIG.


3


. According to

FIG. 3

, enclosure


31


(applies to enclosures of

FIGS. 2

,


5


and


6


) is fitted with at least one viewing window or port


33


. Viewing window


33


can be used alone to provide a visual indication of the conditions inside the enclosure


31


. On the other hand, a viewing window


33


is also required to facilitate the use of optical emitters


35


and optical detectors


37


for the purpose of a more accurate assessment of the concentration of functional material inside the enclosure


31


. The optical emitter


35


emits a beam of light that travels across the inside of the enclosure


31


and is detected by optical detector


37


. This optical detector


37


sends an electrical signal to the microprocessor


39


in proportion to the amount of light received (which is a function of the amount of functional material inside the controlled enclosure


31


). This information can be used in many ways, most simply as a check of the process, but also as an input to a closed loop control of the input valve


24


. For example, if the concentration in the controlled enclosure


31


is low, the valve


24


is opened allowing more functional material to enter the controlled enclosure


31


. This method relies on the cleanliness of the viewing windows


33


to be effective, and therefore either by routine maintenance, calibration, or the application of a like charge as the particles to the viewing windows


33


, the viewing windows


33


themselves must be kept free of debris. Skilled artisans will appreciate that there are many variations and other detection methods that could be applied to a closed loop concentration monitoring and control method described above. For example, in an optical detection scheme, the optical emitter


35


and optical detector


37


could be on the same side of the controlled enclosure


31


relying on a reflective surface on the opposite side to reflect the beam. The scope is not limited to optical detection, any method that provides an indication of the amount of functional material such as electrical properties, physical properties, or chemical properties could be used.




Referring back to

FIG. 1

, a compressed fluid carrier contained in the source


16


of compressed fluid is any material that dissolves/solubilizes/disperses a functional material. Source


16


of compressed fluids, containing compressed fluid delivers the compressed fluid carrier at predetermined conditions of pressure, temperature, and flow rate as a compressed fluid. Compressed fluids are defined in the context of this application as those fluids that have a density of greater than 0.1 grams per cubic centimeter in the defined range of temperature and pressure of the formulation reservoir, and are gases at ambient temperature and pressure. Materials in their compressed fluid 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 fluid state, and precipitate the functional material under ambient conditions.




Fluids of interest that may be used to transport the functional material 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 to environmental compatibility, low toxicity, low cost, wide availability, and non-flammability, carbon dioxide is generally preferred.




Referring again to

FIG. 1

, formulation reservoir


18


is utilized to dissolve and/or disperse functional materials in compressed liquids or compressed fluids with or without cosolvents and/or dispersants and/or surfactants, at desired formulation conditions of temperature, pressure, volume, and concentration. The formulation may include additives to modify surface tension for charging and wetting viscosity through the use of rheology modifiers and/or thickeners, stabilizers, binders, and dopants. Functional materials may be any material that needs to be delivered to a substrate


14


, for example electroluminescent molecules, imaging dyes, nanoparticles, polymers etc.




In addition, the formulation reservoir


18


can include a source that electrically charges the material particles prior to the material being ejected from the discharge assembly


20


. Charging the particles is an important step in many of the preferred embodiments. Alternatively, the marking materials can also be chosen such that the marking material stream becomes charged as it is ejected from the discharge assembly


20


and does not need additional charging. Additionally, additives that can promote charging of the marking materials can also be chosen such that the marking material stream becomes charged as it is ejected from the discharge assembly


20


. Such additives may include surfactants such as those disclosed in U.S. patent application Ser. No. 10/033,458 filed Dec. 27, 2001, titled “A Compressed Fluid Formulation” by Glen C. Irvin, Jr., et al.




Further, formulation reservoir


18


can be made out of any suitable materials that can withstand the formulation conditions. An operating range from 0.001 atmospheres (1.013×10


2


Pa) to 1000 atmospheres (1.013×10


8


Pa) in pressure and from −25° Centigrade to 1000° Centigrade is preferred. Typically, the preferred materials of construction include various grades of high pressure stainless steel. However, the material of choice is determined by temperature and pressure range of operation.




Formulation reservoir


18


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


18


and even small changes in the operating conditions within the formulation reservoir


18


can have undesired effects on functional material solubility/dispersability.




Any suitable surfactant and dispersant material that is capable of solubilizing/dispersing the functional materials in the compressed liquid for the required application can be used in this method. Such materials include but are not limited to fluorinated polymers such as perfluoropolyether and silane and siloxane compounds.




Referring to

FIGS. 1 and 4

, delivery system


12


is shown in fluid communication through orifices/nozzles


28


with enclosed, controlled environment


30


that contains substrate


14


and mask


22


. According to

FIG. 1

, valve


24


may be designed to actuate with a specific frequency or for a fixed time period so as to permit the controlled release of formulation from formulation reservoir


18


into enclosed environment


30


via orifices/nozzles


28


. According to

FIG. 4

, the controlled release of functional material


40


into enclosed environment


30


results in the evaporation of the compressed fluid


41


and the precipitation and/or aggregation of the dissolved and/or dispersed functional material


40


. The precipitated/aggregated functional material may be allowed to gravity-settle or may be settled using an electric, electrostatic, electromagnetic, or magnetic assist. Mask


22


in close proximity to substrate


14


results in the patterned deposition of functional material


40


on the substrate


14


.




Substrate


14


may 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. Substrate


14


may be porous or non-porous. Additionally, the substrate


14


can have more than one layer. Additionally, the substrate


14


may be flexible or rigid.




As best illustrated in

FIGS. 2 and 4

, mask


22


may be physical (separate) or integral. The purpose of the mask


22


is to provide a pattern for the deposition of functional solute material. Those skilled in the art will appreciate that mask design and manufacture is well established. Physical masks require direct contact between mask


22


and substrate


14


. Their advantage is that they are relatively inexpensive and can be re-used for multiple substrates


14


. However, if the substrate


14


is delicate, the physical contact may damage the substrate


14


. Precise alignment is also difficult. Integral masks


22


are structures formed on the substrate


14


prior to coating/deposition. Alignment and spacing is easier because the mask


22


is a part of the substrate


14


. However, because of the potential need to remove the mask


22


after deposition, a subsequent etching step may be necessary, potentially making this more expensive and time-consuming.




Referring to

FIG. 4

, nozzle


28


directs the flow of the functional material


40


from formulation reservoir


18


via delivery system


12


into enclosed environment


30


. Nozzle


28


is also used to attenuate the final velocity with which the functional material


40


enters the enclosed environment


30


. In our preferred application, it is desirable to rapidly spread the stream of precipitated functional material


40


using a divergent nozzle geometry. Skilled artisans will however appreciate that nozzle geometry can vary depending on a particular application, as described in U.S. Patent Application Publication No. 2002/011842A1, incorporate herein by reference.




In Operations




Operation of system


10


will now be described.

FIG. 4

is a diagram schematically representing the operation of delivery system


10


and should not be considered as limiting the scope of the invention in any manner. The description below uses a single nozzle


28


although multiple nozzles and/or multiple nozzle shapes and/or multiple delivery devices and shapes are within the contemplation of the invention. (See for instance other nozzle exemplars disclosed in U.S. Patent Application Publication No. 2002/0118245A1.




Referring to

FIG. 4

, a formulation


42


of functional material


40


in a compressed liquid


41


is prepared in the formulation reservoir


18


of the invention. Functional material


40


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

FIG. 4

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


41


making a mixture or formulation


42


. Functional material


40


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


40


used in the formulation.




According to

FIG. 4

, the supercritical fluid and/or compressed liquid


41


form a continuous phase and functional material


40


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


42


(i.e., 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


32


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


42


.




With reference to

FIGS. 1 and 4

, functional material


40


is controllably introduced into the formulation reservoir


18


. The compressed fluid


41


is also controllably introduced into the formulation reservoir


18


. The contents of the formulation reservoir


18


are suitably mixed using a mixing device (not shown) to ensure intimate contact between the functional material


40


and compressed fluid


41


. As the mixing process proceeds, functional material


40


is dissolved and/or dispersed within the compressed 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 fluid


41


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


18


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


42


of functional material and compressed fluid is thermodynamically stable/metastable in that the functional material is dissolved or dispersed within the compressed fluid in such a fashion as to be indefinitely contained in the same state as long as the temperature and pressure within the formulation reservoir


18


are maintained constant or in the same state for the period of the efficient operation of the process (metastable). This thermodynamically stable state is distinguished from other physical mixtures in that there is no settling, precipitation, and/or agglomeration of functional material particles within the formulation reservoir


18


unless the thermodynamic conditions of temperature and pressure within the formulation reservoir


18


are changed. As such, the functional material


40


and compressed fluid


41


mixtures or formulations


42


of the present invention are said to be thermodynamically stable.




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 microparticle, a polymer micro-particle, a metallo-organic microparticle, an inorganic microparticle, and/or composites of these materials, etc. After suitable mixing with the compressed fluid


41


within the formulation reservoir


18


, the functional material


40


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


41


. This thermodynamically stable/metastable mixture or formulation


42


is controllably released from the formulation reservoir


18


through the discharge assembly


20


.




Referring again to

FIG. 4

, during the discharge process, the functional material


40


is precipitated from the compressed fluid


41


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


44


is ejected into the deposition chamber or controlled environment


30


by the discharge assembly


20


. The particle size of the functional material


40


ejected into the chamber


30


and subsequently deposited on the substrate


14


is typically in the range from 1 nanometer to 1000 nanometers. The particle size distribution may be controlled to be more uniform by controlling the formulation (functional solute materials and their concentrations) rate of change of temperature and/or pressure in the discharge assembly


20


, and the ambient conditions inside the controlled environment


30


.




Although not specifically shown, delivery system


12


(FIG.


4


), contemplated by the invention, 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


(see for instance U.S. Patent Application Publication No. 2002/0118245A1). As the pressure is typically stepped down in stages, the formulation


42


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


42


, for instance, 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 of the compressed fluid


41


. The resulting precipitated and/or aggregated functional material


44


deposits on the substrate


14


evenly. According to

FIG. 4

, evaporation of the compressed fluid


41


can occur in a region located outside of the discharge assembly


20


within deposition chamber


30


. Alternatively, evaporation of the compressed fluid


41


can begin within the discharge assembly


20


and continue in the region located outside the discharge assembly


20


but within deposition chamber


30


. Alternatively, evaporation can occur within the discharge assembly


20


.




According to

FIG. 4

, a stream


43


of the functional material


40


and the compressed fluid


41


is formed as the formulation


42


moves through the discharge assembly


20


. When the size of the stream


43


of precipitated and/or aggregated functional material


44


is substantially equal to an exit diameter of the nozzle


28


of the discharge assembly


20


, the stream


43


of precipitated and/or aggregated functional material


44


has been collimated by the nozzle


28


. When the size of the stream


43


of precipitated and/or aggregated functional material


44


is less than the exit diameter of the nozzle


28


of the discharge assembly


20


, the stream


43


of precipitated and/or aggregated functional material


44


has been focused by the nozzle


28


. It may be desirable for a deposition chamber input to be a diverging beam to quickly spread the precipitated and/or aggregated functional material


44


and dissipate its kinetic energy. Such an input is possible without a nozzle


28


.




Referring again to

FIGS. 2

,


4


&


5


, substrate


14


resides within deposition chamber


30


such that the stream


43


of precipitated and/or aggregated functional material stream


44


is deposited onto the substrate


14


. The distance of the substrate


14


from the discharge assembly


20


is chosen such that the compressed fluid


41


evaporates prior to reaching the substrate


14


. Hence, there is no need for subsequent substrate


14


drying processes. Further, subsequent to the ejection of the formulation


42


from the nozzle


28


and the precipitation of the functional material


44


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


14


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


40


can be controlled.




Referring again to

FIG. 4

, it is also desirable to control the velocity with which individual particles


46


of functional material


40


are ejected from the nozzle


28


. Since there may be 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 substrate


14


. The velocity of these particles


46


can be controlled by suitable nozzle design (see discussion above) and by controlling the rate of change of operating pressure and temperature within the system. Further, subsequent to the ejection of the formulation


42


from nozzle


28


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. The nozzle design will depend upon the particular application addressed. (See, for instance, U.S. Patent Application Publication No. 2002/0118245A1).




Moreover, the temperature of nozzle


28


may also be controlled. Referring to

FIG. 4

, the temperature of nozzle


28


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 (not shown) using a waterjacket, electrical heating techniques, etc. (See, for instance, U.S. Patent Application Publication No. 2002/0118245A1). 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.




Embodiment I




Referring to

FIG. 2

, controlled environment


30


is designed for use at extremes of pressure. Incorporated in the controlled environment


30


is a pressure modulator


105


. The pressure modulator


105


, as shown, resembles a piston. This is for illustration only. Skilled artisans will also appreciate that pressure modulator


105


could also be a pump or a vent used in conjunction with an additional pressure source. An example of an additional pressure source is the source


109


of compressed fluid. This source


109


is modulated with a flow control device or valve


108


to enable functional material to enter the deposition chamber


30


via a fluid delivery path


13


. The pressure inside the deposition chamber


30


is carefully monitored by a pressure sensor


103


and can be set at any pressure less than that of the delivery system


12


(including levels of vacuum) to facilitate precipitation/aggregation. In addition, the deposition chamber


30


is provided with temperature sensor


104


and temperature modulator


106


. Temperature modulator


106


is shown as an electric heater but could consist of any of the following (not shown): heater, a waterjacket, a refrigeration coil, and a combination of temperature control devices.




Referring to

FIGS. 1

,


2


, and


4


, deposition chamber


30


generally serves to hold the substrate


14


and the mask


22


and facilitates the deposition of the precipitated functional material


44


. To enable a more complete and even distribution of the functional material


40


, electric or electrostatic charges can be applied to the substrate


14


and/or mask


22


. Through the ejection process in the discharge assembly


20


, the particles are known to become charged. If desired, additional charge can be applied to them using a particle charging device


107


(FIG.


2


). The functional material


40


, now charged can be attracted or repelled from various surfaces to aid in the deposition process. According to

FIG. 2

, charging devices


102




a


,


102




b


are provided for both the substrate


14


and mask


22


, respectively. For illustrative purposes only, a positive charge (+) is shown on substrate


14


and a negative charge (−) is shown on mask


22


. The polarity may be changed to suit the application. A charge equal to that of the functional material


40


is applied to the mask


22


, whereas a charge opposite of that of the functional material


40


is applied to the substrate


14


to attract the functional material. Obviously there can be no electrical conduction between the two to maintain the charge differential. This may limit the material selection of one or both, or add the requirement for an additional insulating layer (not shown). In a similar manner, it may be beneficial to create other electric or electrostatic charges on the deposition chamber


30


or on any other mechanical elements within the deposition chamber


30


. As shown in

FIG. 6

, an internal baffle


122


may be used to provide a more even distribution of functional material


40


within the deposition chamber


200


. A charge may be applied to the internal baffling by a baffle charging device


123


.




Referring again to

FIG. 2

, deposition chamber


30


also provides easy access for the insertion and removal of the substrate


14


through access port


101


. This process will potentially be automated by mechanical devices which are not shown. Access port


101


of deposition chamber


30


also provides access for the insertion and removal of the mask


22


as well as for the proper placement of the mask


22


. Mask alignment relative to the substrate


14


is key to this application and may be manual or preferably, automated. Though it is shown oriented with the substrate


14


facing upwards, this is not a requirement of the invention. When attracting particles electrostatically, it may be advantageous to orient the substrate


14


facing downward. In this manner, no debris from the deposition chamber


30


could inadvertently fall onto the substrate


14


.




The controlled environment can be used for post deposition processing of the deposited material on the substrate. Post deposition processing may involve the control of humidity, temperature, atmospheric conditions including pressure, and chemical composition of the atmosphere. As an example, many processes require the curing of the materials to obtain desired functionality at elevated temperature. The thermal control that is already built into the enclosure can be utilized for this purpose. Alternatively, the post processing required can be done outside the enclosure.




It should be appreciated that deposition chamber


30


should also be designed so that there are no dead volumes that may result in the accumulation of precipitated functional materials


44


and so that it may be easily cleaned. As such, it may be further partitioned into more than one sub-chamber to facilitate the above (not shown). It may also be equipped with suitable mechanical devices to aid the precipitation and deposition of functional material


40


. An example of such a device would be a mechanical agitator.




Embodiment II




Turning now to

FIG. 5

, another embodiment of deposition chamber


100


, contemplated by the invention, is shown. It contains many of the same features previously described in the discussion of

FIG. 2

, with the addition of a medium


111


which divides the deposition chamber


100


into a preparation sub-chamber


100




a


, and a deposition sub-chamber


100




b


. The materials in these sub-chambers


100




a


,


100




b


are allowed to flow through controllable dual chamber interface valve


110


. Each sub-chamber


100




a


,


100




b


is configured with independent control of pressure and temperature through the use of pressure sensors


103


, temperature sensors


104


, pressure modulators


105


, and temperature modulators


106


. The preparation sub-chamber


100




a


differs from the formulation reservoir


18


(

FIG. 1

) in that the functional material


40


can be (but is not necessarily) precipitated. The addition of a preparation sub-chamber


100




a


to the system allows for a potentially large volume of prepared deposition material to be ready and maintained at a higher than ambient pressure while still allowing the changing of substrate


14


and deposition material through the access port


101


.




Embodiment III




In

FIG. 6

, a simplified deposition chamber


200


is illustrated. In this embodiment, no provision is made for maintaining a pressure above that of ambient. Many of the other features described in

FIGS. 2 and 5

are still possible, but by no longer requiring the deposition chamber


200


to support an elevated pressure, certain additional advantages can be realized. For example, the substrate


14


no longer is required to be contained in deposition chamber


200


. This is illustrated in

FIG. 6

by showing a moving substrate in the form of a web


120


that is transported by conveyors


121


. In such a system, it is possible to perform continuous coating operations. In this case, a separate mask would likely not be used except for the case of a step and repeat process. Rather, a mask integral to the substrate, as previously described, is the preferred method of achieving patterned deposition. Alternatively, a similar approach, illustrated in

FIGS. 2 and 5

, could be used also without need for access port


101


.




Additional aspects of the invention may include multiple deposition chambers


30


,


100


, or


200


, as illustrated in

FIGS. 2

,


5


, and


6


, for coating multiple layers onto substrate


14


. Alternatively, multiple masks


22


may be used such that a mask with a specific configurational structure of aperture patterns is used and subsequently replaced with another shadow mask of different configurational structure of aperture patterns on the same substrate


14


. Multiple masks, indexing of a mask, multiple layers, and multiple material processes are commonly used in the manufacture of displays, therefore details and methods to provide proper registration such as through the use of optical fiducials are well known. The sequential process used for deposition of colored material(s) for display products applications may be interspersed with other processes, including deposition of other material(s) and/or post treatment of deposited material(s), as needed, to create a desired product.




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. These are to be treated as exemplary, and are not intended to limit the scope of the invention in any manner.


















10




system






12




delivery system






13




fluid delivery path






14




substrate






16




source of compressed fluid






18




formulation reservoir






20




discharge assembly






22




mask






24




closed loop control of the input valve






28




orifices/nozzles






30




deposition chamber or controlled environment






31




enclosure






32




shutter






33




viewing window






35




optical emitter






37




optical detector






39




microprocessor






40




functional material






41




compressed fluids






42




formulation of functional material 40






43




stream of functional material 40






44




precipitated and/or aggregated functional material






46




functional material particles






47




nozzle opening






100




alternative embodiment of deposition chamber or controlled







environment






100a




preparation sub-chamber






100b




deposition sub-chamber






101




access port






103




pressure sensor






102a




charging device






102b




charging device






104




temperature sensor






105




pressure modulator






106




Temperature Modulator






107




particle charging device






108




flow control valve






109




source of compressed fluids






110




interface valve






111




medium






120




web






121




conveyor






122




internal baffle






123




baffle charging device






200




another alternative embodiment of deposition chamber







or controlled environment













Claims
  • 1. A system for producing a patterned deposition on a movable substrate from a compressed fluid, comprising:means for controllably delivering a functional material in a compressed state and then converting said functional material into a precipitate functional material; and, a partial enclosure being in fluid communications with said means of controllably delivering said functional material for receiving said precipitate functional material, said partial enclosure having an inlet end and an outlet end for moving said movable substrate therebetween, said movable substrate bearing a shadow mask being exposed to a pattern deposition of charged precipitate functional material and wherein said partial enclosure is electrostatically charged to prevent deleterious particles from adhering thereto.
  • 2. The system recited in claim 1 wherein said partial enclosure comprises a pressure modulator for maintaining pressure at a predetermined pressure level.
  • 3. The system recited in claim 2 wherein said partial enclosure comprises a temperature modulator for maintaining temperature at a predetermined temperature level.
  • 4. The system recited in claim 2 wherein said temperature modulator comprises an electric heater.
  • 5. The system recited in claim 2 wherein said pressure modulator is a piston-like element.
  • 6. The system recited in claim 1 wherein said partial enclosure comprises means for monitoring temperature and pressure levels inside said partial enclosure.
  • 7. The system recited in claim 1 wherein said movable substrate is provided with an electrical charge thereby forming an electrically charged movable substrate to attract charged precipitate functional material in said partial enclosure.
  • 8. The system recited in claim 7 wherein said movable substrate comprises a material selected from the group consisting of: an organic solid material, an inorganic solid material, a metallo-organic material, a ceramic material, an alloy material, a synthetic material, a natural polymeric material, a gel material, a vitreous material, and a composite material.
  • 9. The system recited in claim 7 wherein said electrically charged movable substrate has a polarity opposite that of said charged precipitate functional material.
  • 10. The system recited in claim 1 wherein said shadow mask is provided with an electrical charge forming an electrically charged shadow mask, said electrically charged shadow mask and said charged precipitate functional material having the same polarity.
  • 11. The system recited in claim 1 further comprising means for orienting said movable substrate relative to a stream of charged precipitate functional material.
  • 12. The system recited in claim 11 wherein said movable substrate has an orientation relative to said stream of precipitate functional material that indirectly exposes said movable substrate to said stream of precipitate functional material.
  • 13. The system recited in claim 1 wherein said means for controllably delivering said functional material exposes said precipitate functional material to a pressure higher than the pressure inside said partial enclosure.
  • 14. The system recited in claim 1 wherein said partial enclosure is further provided with a first electrostatic charging element for imparting a charge on said precipitate functional material.
  • 15. The system recited in claim 14 wherein said partial enclosure is further provided with a second electrostatic charging element for imparting an electrostatic charge on said movable substrate.
  • 16. The system recited in claim 15 wherein said partial enclosure is further provided with a third electrostatic charging element for imparting an electrostatic charge on said shadow mask.
  • 17. The system recited in claim 15 wherein a charge applied to said movable substrate is applied for a predetermined duration, said predetermined duration being determinate of an amount of precipitate functional material deposited on said movable substrate.
  • 18. The system recited in claim 1 wherein said functional material comprises a material selected from the group consisting of:electroluminescent molecules, imaging dyes, ceramic nano-particles, and polymeric materials.
  • 19. The system recited in clam 1 wherein said compressed fluid comprises a material selected from the group consisting of:carbon dioxide, nitrous oxide, ammonia, xenon, ethane, ethylene, propane, propylene, butane, isobutane, chlorotrifluoromethane, monofluromethane, sulfur hexafluoride, and mixtures thereof.
  • 20. The system recited in claim 1 wherein an optical emitter cooperates with an optical detector determining the concentration of functional material inside said partial enclosure.
  • 21. The system recited in claim 20 wherein said partial enclosure has at least one viewing port for observing activity inside said partial enclosure.
  • 22. The system recited in claim 20 wherein a reflective surface is arranged in said partial enclosure opposite said optical emitter for reflecting energy from said optical emitter that is detected by said optical detector.
  • 23. The system recited in claim 20 wherein said optical detector transmits an electrical signal to a microprocessor thereby generating data for future processing.
  • 24. The system recited in claim 1 wherein said means for controllably delivering comprises a discharge assembly having a nozzle for ejecting a stream of precipitate functional material into said partial enclosure.
  • 25. The system recited in claim 24 wherein said nozzle is a divergent nozzle.
  • 26. The system recited in claim 25 wherein said precipitate functional material is further propelled from said nozzle in the presence of an electromagnetic field in said partial enclosure.
  • 27. The system recited in claim 25 wherein said precipitate functional material is further propelled from said nozzle in the presence of at least one mechanical shield arranged in said partial enclosure.
  • 28. The system recited in claim 25 wherein said precipitate functional material is further propelled from said nozzle in the presence of at least one magnetic lens arranged in said partial enclosure.
  • 29. The system recited in claim 25 wherein said precipitate functional material is further propelled from said nozzle in the presence of at least one electrostatic lens arranged in said partial enclosure.
  • 30. The system recited in claim 24 wherein said nozzle is provided with a heating means to promote a predetermined fluid flow rate.
  • 31. The system recited in claim 1 wherein said movable substrate and said means for controllably delivering are spaced apart by a predetermined distance that enables the compressed fluid to evaporate from a liquid or compressed phase to a gas phase prior to depositing on said movable substrate.
  • 32. The system recited in claim 1 wherein said functional material is dissolved in said compressed state.
  • 33. The system recited in claim 1 wherein said functional material is dispersed in said compressed state.
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4218532 Dunkleberger Aug 1980 A
4582731 Smith Apr 1986 A
4734227 Smith Mar 1988 A
4734451 Smith Mar 1988 A
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Entry
U.S. patent application Ser. No. 10/033,458, Irvin, Jr., filed Dec. 27, 2001.
Ivor, Brodie and Julius J. Muray, “The Physics Of Micro/Nano-Fabrication” Plenum Press, New York, 1992.