Aerodynamic jetting of blended aerosolized materials

Information

  • Patent Grant
  • 8796146
  • Patent Number
    8,796,146
  • Date Filed
    Tuesday, March 9, 2010
    14 years ago
  • Date Issued
    Tuesday, August 5, 2014
    9 years ago
Abstract
Method and apparatus for direct writing of passive structures having a tolerance of 5% or less in one or more physical, electrical, chemical, or optical properties. The present apparatus is capable of extended deposition times. The apparatus may be configured for unassisted operation and uses sensors and feedback loops to detect physical characteristics of the system to identify and maintain optimum process parameters.
Description
BACKGROUND OF THE INVENTION

1. Field of the Invention (Technical Field)


The present invention relates generally to the field of direct deposition of passive structures. More specifically, the invention relates to the field of maskless, precision deposition of mesoscale passive structures onto planar or non-planar targets, with an emphasis on deposition of precision resistive structures.


2. Background Art


Note that the following discussion refers to a number of publications and references. Discussion of such publications herein is given for more complete background of the scientific principles and is not to be construed as an admission that such publications are prior art for patentability determination purposes. Various methods for deposition of passive structures exist, however, thick film and thin film methods have played a dominant role in the deposition of passive structures, including but not limited to resistors or capacitors, onto various electronic and microelectronic targets. By way of example, the thick film technique typically uses a screen-printing process to deposit electronic pastes with linewidths as small as 100 microns. Thin film methods for the printing of electronic structures include vapor deposition techniques, such as chemical vapor deposition and laser-assisted chemical vapor deposition, as well as physical deposition techniques, such as sputtering and evaporation.


U.S. Pat. No. 4,938,997 discloses a method for the fabrication of thick film resistors on ceramic substrates, with tolerances consistent with those required for microelectronic circuitry. In this method, a ruthenium-based resistor material is screen printed onto the substrate and fired at temperatures in excess of 850° C. U.S. Pat. No. 6,709,944 discloses a method for fabrication of passive structures on flexible substrates by using ion bombardment to activate the surface of a substrate such as polyimide, forming a graphite-like carbon region that may be combined with another deposited material—such as titanium—to form a passive structure. U.S. Pat. No. 6,713,399 discloses a method for the fabrication of embedded resistors on printed circuit boards. The method uses a thin film process to form embedded passive structures in recesses that have been formed in a conductive layer. The method of U.S. Pat. No. 6,713,399 discloses a process that eliminates the high resistance variation seen in polymer thick film embedded resistors.


While thick film and thin film methods of passive structure fabrication are well-developed, these processes may be unsuitable for certain deposition applications. Some disadvantages of thick film processes are the relatively large minimum linewidths that are characteristic of the technique, the need for mask utilization, and the need for high-temperature processing of the deposited material. The disadvantages of typical thin film processes include the need to use masks, vacuum atmospheres, and multi-step photolithographic processes.


In contrast with conventional methods for deposition of passive structures, the M3D® process is a direct printing technique that does not require the use of vacuum chambers, masks, or extensive post-deposition processing. Commonly-owned International Patent Application Number PCT/US01/14841, published as WO 02/04698 and incorporated herein by reference, discloses a method for using an aerosol jet to deposit passive structures onto various targets, but gives no provision for lowering the tolerance of deposited structures to levels that are acceptable for manufacturing of electronic components. Indeed, the use of a virtual impactor in the invention disclosed therein eventually leads to failure of the system due to the accumulation of particles in the interior of the device. As a result, the maximum runtime before failure of the previously disclosed system is 15 to 100 minutes, with the electrical tolerances of deposited structures of approximately 10% to 30%.


Contrastingly, the present invention can deposit passive structures with conductance, resistance, capacitance, or inductance values with tolerances of less than 5%, and runtimes of several hours.


SUMMARY OF THE INVENTION

The present invention is an apparatus for depositing a passive structure comprising a material on a target, the apparatus comprising an atomizer for forming an aerosol comprising the material and a carrier gas, an exhaust flow controller for exhausting excess carrier gas, a deposition head for entraining the aerosol in a cylindrical sheath gas flow, a pressure sensing transducer, a cross connecting the atomizer, the deposition head, the exhaust flow controller, and the transducer, wherein the tolerance of a desired property of the passive structure is better than approximately 5%. The deposition head and atomizer are preferably connected to the cross at inlets opposite each other. The exhaust flow controller preferably exhausts excess carrier gas at a direction perpendicular to an aerosol direction of travel through the cross. The exhaust flow controller preferably reduces the carrier gas flowrate.


The apparatus preferably further comprises a processor for receiving data from the transducer, the processor determining if a leak or clog is present in the apparatus. In such case the apparatus preferably further comprises a feedback loop for automatically purging the apparatus if a clog is detected or automatically ceasing operation of the apparatus if a leak is detected. The apparatus preferably further comprises a laser whose beam passes through the flowing aerosol and a photodiode for detecting scattered light from the laser. The laser beam is preferably perpendicular to the flow direction of the aerosol and the photodiode is preferably oriented orthogonally to both the laser beam and the flow direction. The photodiode is preferably connected to a controller for automatically controlling the atomizer power.


The invention is also a method of depositing a passive structure comprising a material on a target, the method comprising the steps of: atomizing the material; entraining the atomized material in a carrier gas to form an aerosol; removing excess carrier gas from the aerosol via an opening oriented perpendicularly to a flow direction of the aerosol; monitoring a pressure of said aerosol; surrounding the aerosol with a sheath gas; and depositing the material on the target; wherein a tolerance of a desired property of the passive structure is better than approximately 5%. The method preferably further comprises the steps of determining the existence of a leak or clog based on a value of the pressure, and automatically purging the system if a clog exists or automatically ceasing operation if a leak exists. The method preferably further comprises the steps of shining a laser beam into the aerosol and measuring scattered light from the laser beam. The measuring step is preferably performed by a detector oriented orthogonally to both the laser beam and a flow direction of the aerosol. The method preferably further comprises the step of varying the power used in the atomizing step based on an amount of scattered light detected in the measuring step.


The method preferably further comprises the step of processing the material, the processing step preferably selected from the group consisting of humidifying the aerosol, drying the aerosol, heating the aerosol, heating the deposited material, irradiating the deposited material with a laser beam, and combinations thereof. Irradiating the deposited material with a laser beam preferably enables a linewidth of the deposited material to be as low as approximately 1 micron. Irradiating the deposited material with a laser beam preferably does not raise an average temperature of the target to above a damage threshold.


An object of the present invention is to pre-process a material in flight and/or post processing treatment the material after its deposition on a target resulting in a physical and/or electrical property having a value near that of a bulk material.


Another object of the present invention is to provide a deposition apparatus which is capable of long runtimes.


An advantage of the present invention is that deposited passive structures have conductance, resistance, capacitance, or inductance values with tolerances of less than 5%.


Other objects, advantages and novel features, and further scope of applicability of the present invention will be set forth in part in the detailed description to follow, taken in conjunction with the accompanying drawings, and in part will become apparent to those skilled in the art upon examination of the following, or may be learned by practice of the invention. The objects and advantages of the invention may be realized and attained by means of the instrumentalities and combinations particularly pointed out in the appended claims.





A BRIEF DESCRIPTION OF THE DRAWINGS

The accompanying drawings, which are incorporated into and form a part of the specification, illustrate several embodiments of the present invention and, together with the description, serve to explain the principles of the invention. The drawings are only for the purpose of illustrating a preferred embodiment of the invention and are not to be construed as limiting the invention. In the drawings:



FIG. 1
a is a schematic of the embodiment of the preferred M3D® apparatus of the present invention capable of extended runtimes and depositing passive structures with tolerances below 5%.



FIG. 1
b shows the general embodiment of the preferred M3D® apparatus of the present invention, configured for pneumatic atomization.



FIG. 2 is a graph showing the relationship between sheath gas pressure and total gas flow rate.



FIG. 3
a is a schematic of a cross section of a passive structure with terminations. The height of the structure is t1.



FIG. 3
b is a schematic of FIG. 3a, with an additively trimmed passive structure. The height of the structure is t2, where t2 >t1.



FIG. 4 is a schematic showing that the rightmost resistor has a greater resistance than the middle structure, by virtue of the greater length of resistor material between the pads.



FIG. 5
a is a schematic of a ladder resistor prior to direct write of additional passive structures.



FIG. 5
b is a schematic of a ladder resistor showing how structures can be added after the board has been processed and populated with other components, thereby tuning a circuit after it is mostly complete.



FIG. 6 is a schematic of a passive structure written over the edge of a target.



FIG. 7
a is a schematic of a linear passive trace with terminated resistors.



FIG. 7
b is a schematic of a serpentine passive trace with terminated resistors.



FIG. 8 is a schematic of a resistor embedded in a via between two circuit layers.



FIG. 9 depicts a method for depositing a coating on the walls and bottom of a via.



FIGS. 10
a-c are schematics using the M3D® process in a hybrid additive/subtractive technique to fabricate precision metal structures using an etch resist.





DESCRIPTION OF THE PREFERRED EMBODIMENTS
Best Modes for Carrying Out the Invention

Introduction and General Description


The M3D® process is an additive direct printing technology that operates in an ambient environment, and eliminates the need for lithographic or vacuum deposition techniques. The method is capable of depositing a passive electronic component in a predetermined pattern, and uses aerodynamic focusing of an aerosol stream to deposit patterns onto a planar or non-planar target without the use of masks or modified environments. The M3D® method is compatible with commercial thick film and polymer thick film paste compositions, and may also be used with liquid precursor-based formulations, particle-based formulations, and formulations consisting of a combination of particles and liquid precursors. The method is also capable of depositing multiple formulations onto the same target layer. This capability enables direct deposition of resistive structures with a large range of resistance values—ranging from under 50 Ω/square to over 500 KΩ/square—onto the same layer.


The M3D® method is capable of blending different formulations, for example one low-value and one high-value composition, in-transit, in a method in which multiple atomizers are preferably used to aerosolize the two compositions. The formulations are preferably deposited through a single deposition head, and blending may occur during aerosol transport, or when the aerosol droplets combine on the target. This method allows for automated tailoring of a formulation, allowing for the resistivity, or other electrical, thermal, optical, or chemical property of the deposit, to be continuously varied from the low value to the high value. The blending process can also be applied to pastes, inks, various fluids (including, but not limited to, chemical precursor solutions, particle suspensions of electronic, optical, biological and bio-compatible materials, adhesives), and combinations thereof.


As used throughout the specification and claims, “passive structure” means a structure having a desired electrical, magnetic, or other property, including but not limited to a conductor, resistor, capacitor, inductor, insulator, dielectric, suppressor, filter, varistor, ferromagnet, adhesive, and the like.


The M3D™ process preferably deposits material in an aerosolized form. Aerosolization of most particle suspensions is peferably performed using a pneumatic device, such as a nebulizer, however ultrasonic aerosolization may be used for particle suspensions consisting of small particles or low-density particles. In this case, the solid particles may be suspended in water or an organic solvent and additives that maintain the suspension. The two atomization methods allow for the generation of droplets or droplet/particles with sizes typically in, but not limited to, the 1-5 micron size range.


Ultrasonically aerosolized compositions typically have viscosities ranging from 1-10 cP. Precursor and precursor/particle compositions typically have viscosities of 10-100 cP, and are preferably aerosolized pneumatically. Compositions with viscosities of 100-1000 cP are also preferably pneumatically aerosolized. Using a suitable diluent, compositions with viscosities greater than 1000 cP may be modified to a viscosity suitable for pneumatic aerosolization.


The preferred apparatus of the present invention, which is capable of depositing passive structures having tolerances below 5% with extended runtimes, is shown in FIG. 1a. FIG. 1b shows the M3D® apparatus configured for pneumatic atomization, and details the most general embodiment of the apparatus. An inert carrier gas or carrier fluid is preferably used to deliver the aerosolized sample to the deposition module. In the case of ultrasonic atomization, the aerosol-laden carrier gas preferably enters the deposition head immediately after the aerosolization process. The carrier gas may comprise compressed air, an inert gas (which may comprise a solvent vapor), or a mixture of both. The pneumatic aerosolization process requires a carrier gas flow rate that preferably exceeds the maximum allowable gas flow rate through deposition head 22. To enable the use of large carrier gas flow rates (for example, approximately 0.2 to 2 liter/min), a virtual impactor is preferably used to reduce the flowrate of the carrier gas, without appreciable loss of particles or droplets. The number of stages used in the virtual impactor may vary, and is dependent on the amount of carrier gas that must be removed. The stream is introduced into the M3D® deposition head, where an annular flow is developed, consisting of an inner aerosol stream surrounded by a sheath gas. The co-flowing configuration is capable of focusing the aerosol stream to approximately one-tenth the size of the orifice diameter.


When fabricating passive structures using an annular flow, the aerosol stream preferably enters through ports mounted on deposition head 22 and is directed towards the orifice. Aerosol carrier gas flow controller 10 preferably controls the mass throughput. Inside the deposition head, the aerosol stream is preferably initially collimated by passing through a millimeter-size orifice. The emergent particle stream is then combined with a sheath gas or fluid, forming an annular distribution consisting of an inner aerosol-laden carrier gas and an outer sheath gas or fluid. The sheath gas most commonly comprises compressed air or an inert gas, where one or both may contain a modified solvent vapor content. The sheath gas enters through the sheath air inlet below the aerosol inlet and forms an annular flow with the aerosol stream. Gas flow controller 12 preferably controls the sheath gas. The combined streams exit the chamber through an orifice directed at target 28. This annular flow focuses the aerosol stream onto target 28 and allows for deposition of features with dimensions as small as 10 microns or lower. The purpose of the sheath gas is to form a boundary layer that both focuses the aerosol stream and prevents particles from depositing onto the orifice wall. This shielding effect minimizes clogging of the orifices. The diameter of the emerging stream (and therefore the linewidth of the deposit) is controlled by the orifice size, the ratio of sheath gas flow rate to carrier gas flow rate, and the spacing between the orifice and target 28. In a typical configuration, target 28 is attached to a platen that moves in two orthogonal directions under computer control via X-Y linear stages, so that intricate geometries may be deposited. An alternate configuration allows for deposition head 22 to move in two orthogonal directions while maintaining target 28 in a fixed position. Yet another configuration allows for movement of deposition head 22 in one direction, while target 28 moves in a direction orthogonal to that of deposition head 22. The process also enables the deposition of three-dimensional structures.


In the M3D® method, once the sheath gas is combined with the aerosol stream, the flow does not need to pass through more than one orifice in order to deposit sub-millimeter linewidths. In the deposition of a 10-micron line, the M3D® method typically achieves a flow diameter constriction of approximately 250, and may be capable of constrictions in excess of 1000, for this “single-stage” deposition. No axial constrictors are used, and the flows typically do not reach supersonic flow velocities, thus preventing the formation of turbulent flow, which could potentially lead to a complete constriction of the flow.


Aerosolization and Virtual Impaction


In the preferred operation of the system of the present invention detailed in FIG. 1a, Collison-type pneumatic atomizer 32 aerosolizes the material in the sample vial. The aerosol-laden gas stream is delivered to cross 30 that bridges atomizer 32, deposition head 22, exhaust flow controller 34, and pressure sensing transducer 36. Cross 30 is preferably configured so that the aerosol flow inlet is opposite the aerosol flow outlet. The outlet is connected to the M3D® deposition head. Excess carrier gas is preferably exhausted from the system 90° from the aerosol inlet/outlet line of travel. Mass flow controller 34 is preferably used to control the amount of gas that is exhausted from the system. Controlling the exhaust flow using a flow controller increases the precision of the deposition process by aiding in the control of the mass flux of the material that passes to the deposition head.


In an alternative embodiment, the atomizer is located directly adjacent to the virtual impactor. Positioning the virtual impactor near the pneumatic atomizer output results in the deposition of larger droplets, since the aerosol ultimately spends less time in transit from the atomizer to the target, and undergoes reduced evaporation. The deposition of larger droplets can produce a considerable effect on the characteristics of the deposited structure. In general, deposited structures formed from larger droplets show less particle overspray and improved edge definition when compared with structures deposited with small to moderate size droplets. The atomizer is optionally agitated to prevent material agglomeration.


Typically the carrier gas flowrate needed for pneumatic atomization must be reduced after the aerosol is generated, in order for the aerosol stream to be introduced into the deposition head. The required reduction in carrier gas flowrate—from as much as 2 L/min to as little as 10 ml/min—is preferably accomplished using a virtual impactor. However, the use of a virtual impactor may cause the system to be prone to clogging, decreasing the operating time of the apparatus to as little as several minutes, while undesirably decreasing the tolerance of the deposited structure. For example, the apparatus of FIG. 1b may deposit carbon-based resistors for as little as 15 minutes before failure, with a tolerance in the resistance values of as much as 30%. The apparatus of FIG. 1a, contrastingly, replaces the standard


M3D® virtual impactor with cross 30 that exhausts excess carrier gas from the system, while minimizing the loss of particles and buildup of particles with the system. Cross 30 acts as a virtual impactor with considerably larger jet and collector orifice diameters than those used with the standard impactor. The use of larger jet and collector orifice diameters may increase the amount of material that flows through the virtual impactor minor flow axis, while minimizing the accumulation of material on the interior of the device.


Leak/Clog Sensor


The present invention preferably uses a leak/clog sensor comprising pressure transducers to monitor the pressure developed at the atomizer gas inlet and at the sheath gas inlet. In normal operation, the pressure developed within the system is related to the total gas flow rate through the system, and can be calculated using a second-order polynomial equation. A plot of pressure versus total flow through the system is shown in FIG. 2. If the system pressure is higher than the pressure predicted by the curve of FIG. 2, a non-ideal flow may have developed within the system as a result of material accumulation. If the pressure is too low, a system leak is present, and material deposition may be inhibited or stopped entirely. The second order polynomial equation of the curve representing normal operation is of the form:

P=M0+M1Q+M2Q2

where P is the sheath gas pressure and Q is the total flow rate. The total flow rate through the system is given by:

Qultrasonic=Fsheath+Fultrasonic
Qpneumatic=Fsheath+F pneumatic−Fexhaust

where F is the device flow rate. The coefficients M0, M1, and M2 are constants for each deposition tip diameter, but are variable with respect to atmospheric pressure.


The leak/clog sensor provides a valuable system diagnostic that can allow for continuous manual or automated monitoring and control of the system. When operating in an unassisted mode, the system may be monitored for clogs, and automatically purged when an increase in pressure beyond a pre-determined value is detected.


Mist Sensing


Quantitative measurement of the amount of aerosol generated by the atomizer units is critical for extended manual or automated operation of the M3D® system. Maintenance of a constant mist density allows for precision deposition, since the mass flux of aerosolized material delivered to the target can be monitored and controlled.


The system of the present invention preferably utilizes a mist sensor, which preferably comprises a visible wavelength laser whose beam passed through the aerosol outlet tube of the atomizer unit. The beam is preferably oriented perpendicular to the axis of the tube, and silicon photodiodes are preferably positioned adjacent to the tube on an axis perpendicular to both the axes of the tube and the laser. As the laser interacts with the mist flowing through the tube, light is scattered through a wide angle. The energy detected by the photodiodes is proportional to the aerosol density of the mist flow. As the mist flow rate increases, the photodiode output increases until a state of saturation is reached, at which the photodiode output becomes constant. A saturated mist level condition is preferred for constant mist output, so that a constant photodiode output indicates an optimum operating condition.


In a feedback control loop, the output of the photodiodes is monitored and can be used to determine the input power to the ultrasonic atomizer transducer.


Processing


The aerosolized material compositions may be processed in-flight—during transport to the deposition head 22 (pre-processing)—or once deposited on the target 28 (post-processing). Pre-processing may include, but is not limited to, humidifying or drying the aerosol carrier gas or the sheath gas. The humidification process may be accomplished by introducing aerosolized droplets and/or vapor into the carrier gas flow. The evaporation process is preferably accomplished using a heating assembly to evaporate one or more of the solvent and additives.


Post-processing may include, but is not limited to using one or a combination of the following processes: (1) thermally heating the deposited feature, (2) subjecting the deposited feature to a reduced pressure atmosphere, or (3) irradiating the feature with electromagnetic radiation. Post-processing of passive structures generally requires temperatures ranging from approximately 25 to 1000° C. Deposits requiring solvent evaporation or cross-linking are typically processed at temperatures of approximately 25 to 250° C. Precursor or nanoparticle-based deposits typically require processing temperatures of approximately 75 to 600° C., while commercial fireable pastes require more conventional firing temperatures of approximately 450 to 1000° C. Commercial polymer thick film pastes are typically processed at temperatures of approximately 25° to 250° C. Post-processing may optionally take place in an oxidizing environment or a reducing environment. Subjecting the deposit to a reduced pressure environment before or during the heating step, in order to aid in the removal of solvents and other volatile additives, may facilitate processing of passive structures on heat-sensitive targets.


Two preferred methods of reaching the required processing temperatures are by heating the deposit and target on a heated platen or in a furnace (thermal processing), or by irradiating the feature with laser radiation. Laser heating of the deposit allows for densification of traditional thick film pastes on heat-sensitive targets. Laser photochemical processing has also been used to decompose liquid precursors to form mid to high-range resistors, low to mid-range dielectric films, and highly conductive metal. Laser processing may optionally be performed simultaneously with deposition. Simultaneous deposition and processing can be used to deposit structures with thicknesses greater than several microns, or to build three-dimensional structures. More details on laser processing may be found in commonly-owned U.S. patent application Ser. No. 10/952,108, entitled “Laser Processing For Heat-Sensitive Mesoscale Deposition”, filed on Sep. 27, 2004, the specification and claims of which are incorporated herein by reference.


Thermally processed structures have linewidths that are partially determined by the deposition head and the deposition parameters, and have a minimum linewidth of approximately 5 microns. The maximum single pass linewidth is approximately 200 microns. Linewidths greater than 200 microns may be obtained using a rastered deposition technique. Laser-processed lines may have linewidths ranging from approximately 1 to 100 microns (for a structure deposited with a single pass). Linewidths greater than 100 microns may be obtained using a rastered processing technique. In general, laser processing is used to densify or to convert films deposited on heat-sensitive targets, such as those with low temperature thresholds of 400° C. or less, or when a linewidth of less than approximately 5 microns is desired. Deposition of the aerosol stream and processing may occur simultaneously.


Types of Structures: Material Compositions


The present invention provides a method for precision fabrication of passive structures, wherein the material composition includes, but is not limited to, liquid chemical precursors, inks, pastes, or any combination thereof. Specifically, the present invention can deposit electronic materials including but not limited to conductors, resistors, dielectrics, and ferromagnetic materials. Metal systems include, but are not limited to, silver, copper, gold, platinum, and palladium, which may be in commercially available paste form. Resistor compositions include, but are not limited to, systems composed of silver/glass, ruthenates, polymer thick films formulations, and carbon-based formulations. Formulations for deposition of capacitive structures include, but are not limited to, barium titanate, barium strontium titanate, aluminum oxide, and tantalum oxide. Inductive structures have been deposited using a manganese/zinc ferrite formulation blended with low-melting temperature glass particles. The present invention can also blend two uv-curable inks to produce a final composition with a targeted characteristic, such as a specific refractive index.


A precursor is a chemical formulation consisting of a solute or solutes dissolved in a suitable solvent. The system may also contain additives that alter the fluid, chemical, physical, or optical properties of the solution. Inks may be comprised of particles, including but not limited to metal nanoparticles or metal nanoparticles with glass inclusions, of an electronic material suspended in a fluid medium. Depositable pastes include, but are not limited to, commercially available paste formulations for conductive, resistive, dielectric, and inductive systems. The present invention can also deposit commercially available adhesive pastes.


Resistors


A silver/glass resistor formulation may be composed of a liquid molecular precursor for silver, along with a suspension of glass particles, or silver and glass particles, or silver particles in a liquid precursor for glass. A ruthenate system may be comprised of conductive ruthenium oxide particles and insulating glass particles, ruthenium oxide particles in a precursor for glass, or a combination of a ruthenium oxide precursor and a precursor for glass or an insulating medium. Precursor compositions and some precursor/particle compositions may have viscosities of approximately 10 to 100 cP, and may be aerosolized ultrasonically. Resistor pastes may be comprised of either or both of ruthenates, polymer thick film formulations, or carbon-based formulations. Commercially available ruthenate pastes, typically consisting of ruthenium oxide and glass particles, having viscosities of 1000 cP or greater, may be diluted with a suitable solvent such as terpineol to a viscosity of 1000 cP or less. Polymer thick film pastes may also be diluted in a suitable solvent to a similar viscosity, so that pneumatic aerosolization and flow-guidance is enabled. Similarly, carbon-based pastes can be diluted with a solvent such as butyl carbitol to a viscosity of approximately 1000 cP or less. Therefore, many commercial paste compositions with viscosities greater than 1000 cP may be modified and deposited using the M3D® process.


Resistors: Range of Resistance, Repeatability, and Temperature Coefficient of Resistance


The resistive structures deposited using the M3D® process may comprise a resistance spanning approximately six orders of magnitude, from 1 ohm to 1 Mohm. This range of resistance values may be obtained by depositing the appropriate material with the appropriate geometrical cross-sectional area. The tolerance or variance of the resistance values—defined as the ratio of the difference in the resistance value of the highest and lowest passive structure and the average resistance value, for a set of deposits—may be as low as 2 percent. The temperature coefficient of resistance (TCR) for Ag/glass and ruthenate structures may range from approximately ±50 to ±100 ppm.


Geometry


The present method is capable of producing a specific electronic, optical, physical, or chemical value of a structure by controlling the geometry of the deposit. For example, properties of a structure can be altered by controlling the cross-sectional area of the structure, as shown in FIGS. 3a and 3b. Resistance values may be altered by adding material to an existing trace, thereby increasing the cross sectional area of the total trace, thus decreasing the resistance value as material is added to the existing trace. This method is analogous to commonly used laser trimming methods, however material is added rather than removed. The additively trimmed passive trace 38 is deposited onto the existing passive trace 40. As a further example, a specific value may be obtained by controlling the length of a deposited structure; as shown in FIG. 4, the rightmost resistor has a greater resistance than the middle structure, by virtue of the greater length of resistor material between the contact pads. The method of the present invention may also be used to add material to a set of traces or between one or more sets of contact pads 42 connected to a pre-existing electronic circuit, as shown in FIGS. 5a and 5b. Ladder passive traces 44a-b are added to existing passive trace 40. This method enables tuning of the circuit to a specific response or characteristic value. The method is also capable of creating passive structures between layers of circuitry by making passive connections in vias, or by wrapping resistor material 46 around the edge of circuit layers, as shown in FIG. 6.


The passive structures deposited using the M3D® process of the present invention typically have linear geometries, such as the linear passive trace 48 shown in FIG. 7a. Other geometries include, but are not limited to, serpentine 50 (as shown in FIG. 7b), spiral, and helical patterns. Linewidths of deposited resistor material typically range from approximately 10 to 200 microns, but could be greater or lower. Linewidths greater than 200 microns may be obtained by depositing material in a rastered fashion. The thickness of the deposited film may range from a few hundred nanometers to several microns.


Via Filling


The M3D® process can be used to fill vias, providing electrical interconnectivity between adjacent layers of an electronic circuit. The present invention allows for the precise, uniform deposition of an aerosolized material over an extended period of time, for example into via holes.



FIG. 8 shows a resistive connection between different layers of circuitry. Conductive layers in a PCB (printed circuit board) are typically connected by metal vias, however, the M3D® process also allows for deposition of resistive structures into vias. The resistive via configuration is advantageous since, by moving the layer resistors into vias, additional space is provided on the surface of the circuit board layers.



FIG. 9 depicts a method for depositing a coating on the walls and bottom of a via. In FIG. 9a, via 60 is completely filled with ink 62 using the process of the present invention. As ink 62 dries, the solids 64 will adhere onto the walls and the bottom of the via, leaving the middle of the via hollow, as shown in FIG. 9b. Coating the wall with highly conductive material results in a very useful structure, because most of the current in a via flows along the wall and not through the middle.


Dielectrics


In the case of fabrication of dielectric structures, an ink can be comprised of a precursor for an insulator, such as polyimide, while a paste may be a formulation containing dielectric particles and low melting temperature glass inclusions. The precision deposition offered by the present invention is critical to fabrication of high tolerance capacitors, since the thickness and uniformity of a capacitive film determines the capacitance and the performance of the capacitor. Low-k dielectric materials such as glass and polyimide have been deposited for dielectric layers in capacitor applications, and as insulation or passivation layers deposited to isolate electronic components. Mid-k and high-k dielectrics such as barium titanate can be deposited for capacitor applications.


Etch Resist


The present embodiment of the M3D® process may be used in a hybrid additive/subtractive technique to fabricate precision metal structures using an etch resist. Etch resist 70 is preferably atomized and deposited through the deposition head onto metal layer 72, as shown in FIG. 10a. A subtractive technique, for example etching, is then used to remove the exposed metal, FIG. 10b. In the last step, the etch resist is removed, leaving metal structure 74 on the underlying substrate, FIG. 10c. The additive/subtractive etch resist process can be used to deposit reactive metals such as copper.


Targets


Targets suitable for direct write of passive structures using the M3D® process include, but are not limited to, polyimide, FR4, alumina, glass, zirconia, and silicon. Processing of resistor formulations on polyimide, FR4, and other targets with low temperature damage thresholds, i.e. damage thresholds of approximately 400° C. or less, generally requires laser heating to obtain suitable densification. Laser photochemical processing may be used to direct write mid to high range resistor materials such as strontium ruthenate on polyimide.


Applications


Applications enabled by fabrication of passive structures using the M3D® process include, but are not limited to, direct write resistors for electronic circuits, heating elements, thermistors, and strain gauges. The structures may be printed on the more conventional high-temperature targets such as alumina and zirconia, but may also be printed on heat-sensitive targets such as polyimide and FR4. The M3D® process may also be used to print embedded passive structures onto pre-existing circuit boards, onto planar or non-planar surfaces, and into vias connecting several layers of a three-dimensional electronic circuit. Other applications include, but are not limited to, blending passive element formulations to produce a deposited structure with a specific physical, optical, electrical, or chemical property; repair of passive structures on pre-populated circuit boards; and deposition of passive structures onto pre-populated targets for the purpose of altering the physical, optical, electrical, or chemical performance of a system. The present invention enables the above applications with tolerances in physical or electrical properties of 5% or less.


Although the present invention has been described in detail with reference to particular preferred and alternative embodiments, persons possessing ordinary skill in the art to which this invention pertains will appreciate that various modifications and enhancements may be made without departing from the spirit and scope of the claims that follow, and that other embodiments can achieve the same results. The various configurations that have been disclosed above are intended to educate the reader about preferred and alternative embodiments, and are not intended to constrain the limits of the invention or the scope of the claims. Variations and modifications of the present invention will be obvious to those skilled in the art and it is intended to cover all such modifications and equivalents. The entire disclosures of all patents and publications cited above are hereby incorporated by reference.

Claims
  • 1. A method for depositing blended materials, the method comprising the steps of: separately aerosolizing a plurality of materials comprising different values of a property;blending the aerosolized materials;focusing the aerosolized materials into at least one stream directed at a target;transporting the at least one stream to the target;depositing the blended materials in a desired pattern on the target; andcontinuously varying the relative amounts of the aerosolized materials during the depositing step, thereby varying a value of the property of the deposited blended materials such that the materials form a deposited structure comprising a plurality of values of the property.
  • 2. The method of claim 1 wherein the property is selected from the group consisting of electrical resistance, resistivity, conductivity, electrical conductance, inductance, capacitance, refractive index, etch resistance, a physical property, a thermal property, an optical property, an electrical property, and a chemical property.
  • 3. The method of claim 1 wherein a material is selected from the group consisting of paste, inks, fluid, chemical precursor solution, particle suspension, adhesive, etch resist, UV-curable ink, electronic material, optical material, biological material, bio-compatible material, and combinations thereof.
  • 4. The method of claim 1 wherein the aerosolizing step comprises using a plurality of atomizers.
  • 5. The method of claim 1 wherein the propelling step comprises passing the materials through a single deposition head.
CROSS-REFERENCE TO RELATED APPLICATIONS

This application is a continuation application of U.S. patent application Ser. No. 11/302,481, entitled “Aerodynamic Jetting of Aerosolized Fluids for Fabrication of Passive Structures”, filed on Dec. 12, 2005, issuing as U.S. Pat. No. 7,674,671, which application claims the benefit of the filing of U.S. Provisional Patent Application Ser. No. 60/635,848, entitled “Solution-Based Aerosol Jetting of Passive Electronic Structures” filed on Dec. 13, 2004. The specification and claims of these applications are incorporated herein by reference.

US Referenced Citations (241)
Number Name Date Kind
3474971 Goodrich Oct 1969 A
3590477 Cheroff et al. Jul 1971 A
3642202 Angelo Feb 1972 A
3715785 Brown et al. Feb 1973 A
3777983 Hibbins Dec 1973 A
3808432 Ashkin Apr 1974 A
3808550 Ashkin Apr 1974 A
3846661 Brown et al. Nov 1974 A
3854321 Dahneke Dec 1974 A
3901798 Peterson Aug 1975 A
3959798 Hochberg et al. May 1976 A
3974769 Hochberg et al. Aug 1976 A
3982251 Hochberg Sep 1976 A
4004733 Law Jan 1977 A
4016417 Benton Apr 1977 A
4019188 Hochberg Apr 1977 A
4034025 Martner Jul 1977 A
4036434 Anderson et al. Jul 1977 A
4046073 Mitchell et al. Sep 1977 A
4046074 Hochberg et al. Sep 1977 A
4073436 Behr Feb 1978 A
4092535 Ashkin et al. May 1978 A
4112437 Mir et al. Sep 1978 A
4132894 Yule Jan 1979 A
4171096 Welsh et al. Oct 1979 A
4200669 Schaefer et al. Apr 1980 A
4228440 Horike et al. Oct 1980 A
4269868 Livsey May 1981 A
4323756 Brown et al. Apr 1982 A
4453803 Hidaka et al. Jun 1984 A
4485387 Drumheller Nov 1984 A
4497692 Gelchinski et al. Feb 1985 A
4601921 Lee Jul 1986 A
4605574 Yonehara et al. Aug 1986 A
4670135 Marple et al. Jun 1987 A
4685563 Cohen et al. Aug 1987 A
4689052 Ogren et al. Aug 1987 A
4694136 Kasner et al. Sep 1987 A
4724299 Hammeke Feb 1988 A
4825299 Okada et al. Apr 1989 A
4826583 Biernaux et al. May 1989 A
4893886 Ashkin et al. Jan 1990 A
4904621 Loewenstein et al. Feb 1990 A
4911365 Thiel et al. Mar 1990 A
4920254 DeCamp et al. Apr 1990 A
4947463 Matsuda et al. Aug 1990 A
4971251 Dobrick et al. Nov 1990 A
4997809 Gupta Mar 1991 A
5032850 Andeen et al. Jul 1991 A
5043548 Whitney et al. Aug 1991 A
5064685 Kestenbaum et al. Nov 1991 A
5164535 Leasure Nov 1992 A
5170890 Wilson et al. Dec 1992 A
5176744 Muller Jan 1993 A
5182430 Lagain Jan 1993 A
5194297 Scheer et al. Mar 1993 A
5208431 Uchiyama et al. May 1993 A
5245404 Jannson et al. Sep 1993 A
5250383 Naruse Oct 1993 A
5254832 Gartner et al. Oct 1993 A
5270542 McMurry et al. Dec 1993 A
5292418 Morita et al. Mar 1994 A
5322221 Anderson Jun 1994 A
5335000 Stevens Aug 1994 A
5343434 Noguchi Aug 1994 A
5344676 Kim et al. Sep 1994 A
5359172 Kozak et al. Oct 1994 A
5366559 Periasamy Nov 1994 A
5378505 Kubota et al. Jan 1995 A
5378508 Castro et al. Jan 1995 A
5403617 Haaland Apr 1995 A
5425802 Burton et al. Jun 1995 A
5449536 Funkhouser Sep 1995 A
5486676 Aleshin Jan 1996 A
5491317 Pirl Feb 1996 A
5495105 Nishimura et al. Feb 1996 A
5512745 Finer et al. Apr 1996 A
5529634 Miyata et al. Jun 1996 A
5607730 Ranalli Mar 1997 A
5609921 Gitzhofer et al. Mar 1997 A
5612099 Thaler Mar 1997 A
5614252 McMillan et al. Mar 1997 A
5648127 Turchan et al. Jul 1997 A
5676719 Stavropoulos et al. Oct 1997 A
5732885 Huffman Mar 1998 A
5733609 Wang Mar 1998 A
5736195 Haaland Apr 1998 A
5742050 Amirav et al. Apr 1998 A
5770272 Biemann et al. Jun 1998 A
5772106 Ayers et al. Jun 1998 A
5772964 Prevost et al. Jun 1998 A
5814152 Thaler Sep 1998 A
5844192 Wright et al. Dec 1998 A
5854311 Richart Dec 1998 A
5861136 Glicksman et al. Jan 1999 A
5882722 Kydd Mar 1999 A
5894403 Shah et al. Apr 1999 A
5940099 Karlinski Aug 1999 A
5958268 Engelsberg et al. Sep 1999 A
5965212 Dobson et al. Oct 1999 A
5980998 Sharma et al. Nov 1999 A
5993549 Kindler et al. Nov 1999 A
5993554 Keicher et al. Nov 1999 A
5997956 Hunt et al. Dec 1999 A
6007631 Prentice et al. Dec 1999 A
6015083 Hayes et al. Jan 2000 A
6025037 Wadman et al. Feb 2000 A
6036889 Kydd Mar 2000 A
6040016 Mitani et al. Mar 2000 A
6056994 Paz de Araujo et al. May 2000 A
6110144 Choh et al. Aug 2000 A
6116718 Peeters et al. Sep 2000 A
6136442 Wong Oct 2000 A
6143116 Hayashi et al. Nov 2000 A
6151435 Pilloff Nov 2000 A
6159749 Liu Dec 2000 A
6182688 Fabre Feb 2001 B1
6197366 Takamatsu Mar 2001 B1
6251488 Miller et al. Jun 2001 B1
6258733 Solayappan et al. Jul 2001 B1
6265050 Wong et al. Jul 2001 B1
6267301 Haruch Jul 2001 B1
6290342 Vo et al. Sep 2001 B1
6291088 Wong Sep 2001 B1
6293659 Floyd et al. Sep 2001 B1
6318642 Goenka et al. Nov 2001 B1
6328026 Wang et al. Dec 2001 B1
6340216 Peeters et al. Jan 2002 B1
6348687 Brockmann et al. Feb 2002 B1
6349668 Sun et al. Feb 2002 B1
6355533 Lee Mar 2002 B2
6379745 Kydd et al. Apr 2002 B1
6384365 Seth et al. May 2002 B1
6390115 Rohwer et al. May 2002 B1
6391494 Reitz et al. May 2002 B2
6406137 Okazaki et al. Jun 2002 B1
6416156 Noolandi et al. Jul 2002 B1
6416157 Peeters et al. Jul 2002 B1
6416158 Floyd et al. Jul 2002 B1
6416159 Floyd et al. Jul 2002 B1
6416389 Perry et al. Jul 2002 B1
6454384 Peeters et al. Sep 2002 B1
6467862 Peeters et al. Oct 2002 B1
6471327 Jagannathan et al. Oct 2002 B2
6481074 Karlinski Nov 2002 B1
6486432 Colby et al. Nov 2002 B1
6503831 Speakman Jan 2003 B2
6513736 Skeath et al. Feb 2003 B1
6521297 McDougall et al. Feb 2003 B2
6537501 Holl et al. Mar 2003 B1
6544599 Brown et al. Apr 2003 B1
6548122 Sharma et al. Apr 2003 B1
6564038 Bethea et al. May 2003 B1
6572033 Pullagura et al. Jun 2003 B1
6573491 Marchitto et al. Jun 2003 B1
6607597 Sun et al. Aug 2003 B2
6636676 Renn Oct 2003 B1
6646253 Rohwer et al. Nov 2003 B1
6656409 Keicher et al. Dec 2003 B1
6772649 Zimmermann et al. Aug 2004 B2
6774338 Baker et al. Aug 2004 B2
6780377 Hall et al. Aug 2004 B2
6811744 Keicher et al. Nov 2004 B2
6823124 Renn et al. Nov 2004 B1
6855631 Kirby Feb 2005 B2
6890624 Kambe et al. May 2005 B1
6921626 Ray et al. Jul 2005 B2
6998345 Kirby Feb 2006 B2
6998785 Silfvast et al. Feb 2006 B1
7009137 Guo et al. Mar 2006 B2
7045015 Renn et al. May 2006 B2
7108894 Renn Sep 2006 B2
7270844 Renn Sep 2007 B2
7294366 Renn et al. Nov 2007 B2
7485345 Renn et al. Feb 2009 B2
7658163 Renn et al. Feb 2010 B2
7674671 Renn et al. Mar 2010 B2
20010046551 Falck et al. Nov 2001 A1
20020012743 Sampath et al. Jan 2002 A1
20020071934 Marutsuka Jun 2002 A1
20020096647 Moors et al. Jul 2002 A1
20020100416 Sun et al. Aug 2002 A1
20020132051 Choy Sep 2002 A1
20020162974 Orsini et al. Nov 2002 A1
20030003241 Suzuki et al. Jan 2003 A1
20030020768 Renn Jan 2003 A1
20030048314 Renn Mar 2003 A1
20030108511 Sawhney Jun 2003 A1
20030108664 Kodas et al. Jun 2003 A1
20030117691 Bi et al. Jun 2003 A1
20030138967 Hall et al. Jul 2003 A1
20030175411 Kodas et al. Sep 2003 A1
20030180451 Kodas et al. Sep 2003 A1
20030202032 Moffat et al. Oct 2003 A1
20030219923 Nathan et al. Nov 2003 A1
20030228124 Renn et al. Dec 2003 A1
20040004209 Matsuba et al. Jan 2004 A1
20040029706 Barrera et al. Feb 2004 A1
20040038808 Hampden-Smith et al. Feb 2004 A1
20040080917 Steddom et al. Apr 2004 A1
20040151978 Huang Aug 2004 A1
20040179808 Renn Sep 2004 A1
20040185388 Hirai Sep 2004 A1
20040191695 Ray et al. Sep 2004 A1
20040197493 Renn et al. Oct 2004 A1
20040247782 Hampden-Smith et al. Dec 2004 A1
20050002818 Ichikawa Jan 2005 A1
20050101129 Lirby May 2005 A1
20050110064 Duan et al. May 2005 A1
20050129383 Renn et al. Jun 2005 A1
20050133527 Dullea et al. Jun 2005 A1
20050145968 Goela et al. Jul 2005 A1
20050147749 Liu et al. Jul 2005 A1
20050156991 Renn Jul 2005 A1
20050163917 Renn Jul 2005 A1
20050184328 Uchiyama et al. Aug 2005 A1
20050205415 Belousov et al. Sep 2005 A1
20050205696 Saito et al. Sep 2005 A1
20050214480 Garbar et al. Sep 2005 A1
20050215689 Garbar et al. Sep 2005 A1
20050238804 Garbar et al. Oct 2005 A1
20060008590 King et al. Jan 2006 A1
20060046461 Benson et al. Mar 2006 A1
20060057014 Oda et al. Mar 2006 A1
20060163570 Renn et al. Jul 2006 A1
20060172073 Groza et al. Aug 2006 A1
20060175431 Renn et al. Aug 2006 A1
20060233953 Renn et al. Oct 2006 A1
20060280866 Marquez et al. Dec 2006 A1
20070019028 Renn Jan 2007 A1
20070128905 Speakman Jun 2007 A1
20070154634 Renn Jul 2007 A1
20070181060 Renn et al. Aug 2007 A1
20080013299 Renn Jan 2008 A1
20090061077 King et al. Mar 2009 A1
20090061089 King et al. Mar 2009 A1
20090090298 King et al. Apr 2009 A1
20090114151 Renn et al. May 2009 A1
20100173088 King Jul 2010 A1
20100192847 Renn et al. Aug 2010 A1
20130260056 Renn et al. Oct 2013 A1
Foreign Referenced Citations (14)
Number Date Country
198 41 401 Apr 2000 DE
0 331 022 Sep 1989 EP
0 444 550 Sep 1991 EP
0470911 Jul 1994 EP
1 258 293 Nov 2002 EP
2001-507449 Jun 2001 JP
2007-507114 Mar 2007 JP
10-2007-0008614 Jan 2007 KR
10-2007-0008621 Jan 2007 KR
WO 0023825 Apr 2000 WO
WO 0069235 Nov 2000 WO
WO 0183101 Nov 2001 WO
WO 2006041657 Apr 2006 WO
WO 2006065978 Jun 2006 WO
Non-Patent Literature Citations (23)
Entry
Webster's Ninth New Collegiate Dictionary Merriam-Webster, Inc., Springifled, MA. USA 1990 , 744.
Ashkin, A , “Acceleration and Trapping of Particles by Radiation Pressure”, Physical Review Letters Jan. 26, 1970 , 156-159.
Ashkin, A. , “Optical trapping and manipulation of single cells using infrared laser beams”, Nature Dec. 1987 , 769-771.
Dykhuizen, R. C. , “Impact of High Velocity Cold Spray Particles”, May 13, 2000 , 1-18.
Fernandez De La Mora, J. et al., “Aerodynamic focusing of particles in a carrier gas”, J. Fluid Mech. vol. 195, printed in Great Britain 1988 , 1-21.
King, Bruce et al., “M3D TM Technology: Maskless Mesoscale TM Materials Deposition”, Optomec pamphlet 2001.
Lewandowski, H. J. et al., “Laser Guiding of Microscopic Particles in Hollow Optical Fibers”, Announcer 27, Summer Meeting—Invited and Contributed Abstracts Jul. 1997 , 89.
Marple, V. A. et al., “Inertial, Gravitational, Centrifugal, and Thermal Collection Techniques”, Aerosol Measurement: Principles, Techniques and Applications 2001 , 229-260.
Miller, Doyle et al., “Maskless Mesoscale Materials Deposition”, HDI vol. 4, No. 9 Sep. 2001 , 1-3.
Odde, D. J. et al., “Laser-Based Guidance of Cells Through Hollow Optical Fibers”, The American Society for Cell Biology Thirty-Seventh Annual Meeting Dec. 17, 1997.
Odde, D. J. et al., “Laser-guided direct writing for applications in biotechnology”, Trends in Biotechnology Oct. 1999 , 385-389.
Rao, N. P. et al., “Aerodynamic Focusing of Particles in Viscous Jets”, J. Aerosol Sci. vol. 24, No. 7, Pergamon Press, Ltd., Great Britain 1993 , 879-892.
Renn, M. J. et al., “Evanescent-wave guiding of atoms in hollow optical fibers”, Physical Review A Feb. 1996 , R648-R651.
Renn, Michael J. et al., “Flow- and Laser-Guided Direct Write of Electronic and Biological Components”, Direct-Write Technologies for Rapid Prototyping Applications Academic Press 2002 , 475-492.
Renn, M. J. et al., “Laser-Guidance and Trapping of Mesoscale Particles in Hollow-Core Optical Fibers”, Physical Review Letters Feb. 15, 1999 , 1574-1577.
Renn, M. J. et al., “Laser-Guided Atoms in Hollow-Core Optical Fibers”, Physical Review Letters Oct. 30, 1995 , 3253-3256.
Renn, M. J. et al., “Optical-dipole-force fiber guiding and heating of atoms”, Physical Review A May 1997 , 3684-3696.
Renn, M. J. et al., “Particle Manipulation and Surface Patterning by Laser Guidance”, Submitted to EIPBN '98, Session AM4 1998.
Renn, M. J. et al., “Particle manipulation and surface patterning by laser guidance”, Journal of Vacuum Science & Technology B Nov./Dec. 1998 , 3859-3863.
Sobeck, et al., “Technical Digest: 1994 Solid-State Sensor and Actuator Workshop”, 1994 , 647.
TSI Incorporated, , “How a Virtual Impactor Works”, www.tsi.com Sep. 21, 2001.
Vanheusden, K. et al., “Direct Printing of Interconnect Materials for Organic Electronics”, IMAPS ATW, Printing an Intelligent Future Mar. 8-10, 2002 , 1-5.
Zhang, Xuefeng et al., “A Numerical Characterization of Particle Beam Collimation by an Aerodynamic Lens-Nozzle System: Part I. An Individual Lens or Nozzle”, Aerosol Science and Technology vol. 36, Taylor and Francis 2002 , 617-631.
Related Publications (1)
Number Date Country
20100255209 A1 Oct 2010 US
Provisional Applications (1)
Number Date Country
60635848 Dec 2004 US
Continuations (1)
Number Date Country
Parent 11302481 Dec 2005 US
Child 12720573 US