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    Accepted for publication inAluminum Transactions Journal, 2000

    Molten Aluminum Micro-Droplet Formation and Deposition for

    Advanced Manufacturing Applications

    Melissa Orme*, Qingbin Liu and Robert Smith

    Department of Mechanical and Aerospace Engineering, University of California - Irvine

    Irvine, CA 92697-3975, USA

    Abstract

    Molten aluminum droplets are generated from capillary stream break-up and are injected into

    an inert environment. The intrinsic fidelity of droplet formation from capillary stream break-upprovides the allure for use in advanced manufacturing applications such as net-form

    manufacturing and electronics packaging for the two following reasons: first, because the

    droplets are generated with extremely regular diameters and inter-droplet spacings, and second,

    because of the high rates at which they are generated. Additionally, droplet formation from

    capillary stream break-up allows the customization of droplet streams for a particular ap-

    plication. The current status of the technology under development is presented, and issues

    affecting the microstructure and the mechanical properties of the manufactured components are

    studied in an effort to establish a relationship between processing parameters and properties.

    Keywords: Net-Form Manufacturing, Solid Freeform Fabrication, Capillary Stream Break-Up,

    Droplet Deposition, Droplet Based Precision Manufacturing

    1. Introduction

    Use of precisely controlled molten aluminum droplets for advanced manufacturing applications

    is gaining considerable academic and industrial interest due to the promise of improved

    component quality resulting from rapid solidification processing and the economic benefits

    associated with fabricating a structural component in one integrated operation. The

    manufacturing industrial sector seeks to gain a competitive advantage by developing new

    methods of droplet-based net-form manufacturing that allow the flexible data driven manufacture

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    of complicated three-dimensional components in one integrated step with minimal post-

    treatment. Such a droplet based net-form manufacturing technique is under development at

    University of California-Irvine (UCI) that is termed precision droplet-based net-form

    manufacturing (PDM). The crux of the technique lies in the ability to generate highly uniform

    streams of molten metal droplets such as aluminum or aluminum alloys. Though virtually any

    Newtonian fluid that can be contained in a crucible is suitable for the technology, this work

    concentrates on the generation and deposition of molten aluminum alloy (AA2024) droplets that

    are generated and deposited in an inert environment.

    Shown in Figure 1 is a conceptual schematic of the PDM process. Droplets are generated from

    capillary stream break-up in an inert environment and are deposited onto a substrate whose

    motion is controlled by a programmable x-y table. In this way, tubes with circular, square and

    triangular cross sections have been fabricated such as those illustrated in Figure 2. Tubes have

    been fabricated with heights as great as 11.0 cm. The surface morphology of the component is

    governed by the thermal conditions at the substrate. If we denote the solidified component and

    the substrate the "effective substrate," then the newly arriving droplets must have sufficient

    thermal energy to locally remelt a thin layer (with dimensions on the order of 10 microns or less)

    of the effective substrate. Remelting action of the previously deposited and solidified material

    will insure the removal of individual splat boundaries and result in a more homogeneous

    component. The thermal requirements for remelting have been studied analytically in reference

    [1]. It was shown in that work that there exists a minimum substrate temperature for a given

    droplet impingement temperature that results in remelting. The "bumpiness" apparent in the

    circular cylinder shown in Figure 2 is because the initial substrate temperature was insufficient to

    initiate the onset of remelting. In particular to the circular tube, it can be seen that the surface

    morphology is not uniform. This is because the temperature of the substrate was not uniform,

    but was lower at the positions where the component is rougher. Deposition on a low temperature

    surface caused the incoming droplets to land on a previously solidified and curved top surface,

    with insufficient thermal energy for the action of remelting. Hence, the droplets tend to roll from

    the top of the curved surface and roll from one side or the other prior to solidification, as is

    evident in the photograph. Generally, as the component grows in height by successive droplet

    deliveries, the effective substrate temperature increases due to the fact that droplets are delivered

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    at high rates so that the cooling time between successive droplet deliveries is insufficient to

    allow cooling before the arrival of the next layer of droplets. Therefore, within the constraints of

    the current embodiment of the technology, there exists a certain height of the component for

    which remelting will occur. This height is demarcated at the location where the "bumpiness" is

    eliminated and relative "smoothness" prevails, as can be seen in the circular cylinder. As the

    component grows beyond this height, the remelting depth will continue to increase due to

    increased heating to the effective substrate. Hence, the component walls will thicken due to

    slower solidification rates. There is an ongoing work at UCI to identify the heat flux required for

    the minimum remelting of the effective substrate and to develop processing conditions for which

    this heat flux seen by the substrate remains constant for each geometry desired. In this manner,

    the fidelity of the microstructure, mechanical properties and geometry will remain intact.

    At this stage in the development of the PDM technology, electrostatic charging and deflection is

    not employed. However, in the final realization of the technology, charging and deflection will

    be utilized in order to control the droplet density as a function of the component geometry, and to

    print fine details at high speed and at high precision. The charging and deflection of droplets

    bears many similarities to the technology of ink-jet printing, except that in the current application

    of PDM, large lateral areas are printed, thereby requiring significantly higher droplet charges

    than in ink-jet printing. The high charges on the closely spaced droplets result in mutual inter-

    droplet interactions that are not apparent in the application of ink-jet printing. Recent

    experimental and numerical results on the subject of droplet interactions due the application of

    high electrostatic charges are presented elsewhere [2]. Droplet charging and deflection has been

    successfully applied to the "printing" of electronic components such as ball grid arrays (BGA's)

    [3] with a high degree of success. Hence, we aim in future work to bridge the technology of fine

    pitch printing of electronic components with that of net-form manufacturing.

    A vast body of research on controlled droplet formation from capillary stream break-up over the

    past decade forms the basis of the PDM technology and has enabled ultra-precise charged droplet

    formation, deflection and deposition that makes feasible many emerging applications in net-form

    manufacturing and electronic component fabrication [4-9]. Unlike the Drop-on-Demand mode

    of droplet formation, droplets can be generated at rates typically on the order of 10,000 to 20,000

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    droplets per second, from capillary stream break-up and can be electrostatically charged and

    deflected onto a substrate with a measured accuracy of 12.5 m.

    The technologies of 3D printing (3DP) [10-12] and shape deposition manufacturing (SDM) [13-

    15]bear similarities to PDM in as much as they rely on the deposition of precisely controlled

    molten droplets. In 3DP, parts are manufactured by generating droplets of a binder material with

    the Drop-on-Demand mode of generation and depositing them onto selected areas of a layer of

    metal or ceramic powder. After the binder dries, the print bed is lowered and another layer of

    powder is spread in order to repeat the process. The process is repeated until the 3-D component

    is fabricated.

    Similarly, the process of SDM relies on uniform generation of molten metal droplets. However,

    the droplet generation technique is markedly different than droplet generation from capillary

    stream formation, which is the method employed in this work. In SDM, the tip of a feedstock

    wire is melted with the aid of a plasma-welding torch to form droplets that are typically on the

    order of 1-10 mm in diameter. The droplets impinge upon a substrate where they fuse with

    previously deposited and solidified material. With SDM, high quality metallic, ceramic and

    polymer components have manufactured.

    2. Experimental Procedures

    Figure 3 illustrates a conceptual schematic of the molten aluminum droplet generation and

    deflection apparatus. The main component is a graphite lined titanium cartridge that contains the

    molten aluminum or aluminum alloy. The alumina orifice is contained at the lower end of the

    cartridge and a vibrating plunger rod is inserted through an adapting plate at the upper end and is

    extended through the entire length of the cartridge. An active cooling flange shields the

    piezoelectric crystal from extreme temperatures. The molten aluminum is pressurized with a

    driving pressure that is typically on the order of 20 psi. The pressure perturbation established by

    the vibrating rod is on the order of 5% of the driving pressure. The pressure perturbation

    translates to a radial perturbation on the capillary stream, which will grow until droplets are

    pinched off from the stream. The droplets are injected into an inert environment with an oxygen

    content of less than 25 ppm.

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    3. Droplet Generation and Manipulation

    This paper focuses on the generation and deposition of highly uniform molten aluminum droplets

    generated from capillary stream break-up and their application to net-form manufacturing. For

    purposes of brevity, the basic physics of conventional droplet generation from capillary stream

    break-up is omitted and the reader is referred to the informative review papers [16, 17], or other

    numerous references on the subject in the literature base.

    Our experiments have revealed the critical importance of maintaining an environment virtually

    devoid of oxygen. It was found that the aluminum capillary stream is very efficient in capturing

    oxygen. Small trace amounts of oxygen in the jetting environment cause the droplet stream to

    lose its angular stability. Larger amounts of oxygen prohibit entirely the capillary disturbance to

    grow on the stream, eliminating the possibility of generating droplets.

    Additionally, it has been found in this and in previous work [9] that oxides within the melt are

    the leading cause of angular instabilities of the droplet stream. Hence, meticulous attention must

    be paid to filtering the molten aluminum and insuring that it is maintained in an inert

    environment at all times.

    With the above precautions, we have been successful in generating uniform and angularly stable

    streams of droplets from capillary stream break-up. Care must also be taken with respect to the

    selection of the characteristics of the forcing disturbance in order to achieve a stream of drops

    with highly uniform diameters and inter-droplet spacings. The nondimensional wavenumber

    ( *ok ) is defined as the ratio of the stream circumference to the wavelength of the applied

    disturbance and is likely the most important parameter in capillary stream break-up. It is well

    known that the capillary wave growth on an inviscid jet subject to conventional forcing grows

    the fastest for *ok = 0.697. It has also been shown previously [5] that droplet generation at the

    wavenumber corresponding to fastest wave growth results in the most uniform droplet stream

    and generation at wavenumbers far from that of maximum growth lead to droplet streams with

    highly irregular characteristics. Therefore, droplet generation with conventional forcing

    (sinusoidal disturbance resulting in a droplet stream such as that shown in Figure 3) is restricted

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    to a small range of wavenumbers that will result in uniform droplets.

    Use of amplitude-modulated (a-m) disturbances, however, will bypass the limitation imposed by

    conventional forcing. Figure 4 illustrates the ability to manipulate and control the droplet stream

    characteristics through variations in the applied force. The images were obtained by

    backlighting the droplet stream and capturing the droplet configuration on videotape. Individual

    frames were processed and reproduced as shown in Figure 4. In Figure 4a the droplets were

    generated with an a-m disturbance with a frequency ratio of N = fc / fm = 3, where the carrier

    frequency (fc) is selected to be in the region of Rayleigh growth, and is 12,000 Hz. Figure 4b

    illustrates the a-m disturbance that is applied to the piezoelectric crystal that initiated the stream's

    radial instability. Examination of Figure 4 and other similar experimental realizations reveal that

    when an a-m disturbance with an integer frequency ratio (N) is employed for droplet generation,

    groups of N droplets systematically merge in flight to form the final stream of droplets. The

    droplet configurations and the time required to achieve the droplet configurations are predictable

    with knowledge of the forcing disturbance characteristics. Excellent comparison between

    experiment and simulation are provided elsewhere [4, 6]. The final droplet configuration

    consists of droplets that are separated by a distance of Nand have diameters equal to N1/3 times

    the diameter of the original carrier droplet, where 2 is the wavelength of the applied carrier

    disturbance, i.e., the wavelength of the disturbance employed in conventional Rayleigh modedroplet formation. The droplets shown form a highly-regularly spaced and sized droplet stream.

    In fact, the speed dispersion, which is a measure of the uniformity of the droplet stream,

    decreases as 1/N, so that the a-m droplet stream is more uniform than the conventionally

    generated stream. Additionally, the effective wavenumber of the a-m generated stream is *ok /N,

    so that the droplet streams shown in Figure 4 has an effective wavenumber of 0.232. Generation

    of these droplet streams with a conventional disturbance would be impossible due to the severe

    degradation in uniformity that occurs at generation at such low wavenumbers.

    In addition to generating highly uniform streams of droplets at extended wavenumbers, droplet

    streams can be customized for a given application, where the droplet sizes and separations can be

    selected a priori. Figure 5 illustrates one example of the evolution of a droplet pattern that

    consists of repeated sequences of large-small-large droplets. This droplet stream was generated

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    with a frequency ratioN = 3.5.

    The microstructural characteristics of several tubes similar to those shown in Figure 2 that were

    fabricated with AA2024 aluminum alloy droplets were examined. The processing parameters

    are included below in Table I. In the table, To is the initial capillary stream temperature, Ts is the

    initial substrate temperature and m/l is the mass delivered per unit length to the substrate, which

    is directly related to the droplet speed and substrate speed. We chose not to characterize the

    results in terms of the mass flow rate ( )m& since it contains no information regarding the amount

    of material overlap on the substrate (a function of substrate speed), which is of critical

    importance for the geometric and mechanical quality of the component. The cylinders were

    sectioned, and the sections were polished and subsequently photographed with an optical

    microscope. The samples were etched with a modified version of Keller's Reagent, which

    consists of 31% H2O, 31% HCl, 31% HNO3 and 7% HF.

    Table I. Processing properties of cylindrical components.

    Microphotographs shown in Figure number 8 9 10

    To (oC) 787 787 830

    Ts(oC) 176 176 149

    m/l(kg/m) 1.02 1.02 1.19

    Micro-hardness tests were conducted on the above samples directly after fabrication (with no

    post-working) at OCM Test Laboratory in Anaheim California. The results were provided as

    Rockwell "B" Hardness values, which were converted to BNH values (500 kg load and a 10 mm

    diameter ball) in order to compare to the unworked AA2024 reference stock that has a Rockwell

    "B" Hardness value of less than zero and a BNH value of 47. The measurements were conducted

    by averaging five readings over a vertical distance of 1.0 cm in the sample. The procedure is

    identified as ASTM-E-384. The specific gravity was also measured by OCM Test Laboratories

    for the specimens.

    4. Results

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    Alum inum Bal l Fabr icat ion

    By selecting processing parameters that allow the droplets to solidify in flight, uniform

    aluminum balls can be fabricated with capillary stream break-up. Shown in Figure 6 are

    solidified aluminum (AA2024) balls that are 190 m in diameter and were generated at a rate of

    17,000 balls per second, this corresponds to 1.85 kg/hour. The droplet size can be estimated

    from conservation of mass by assuming that mass in one wavelength () of the capillary stream

    of initial radius (ro)forms a carrier droplet of radius rd:

    31

    2

    3

    4

    = od rr

    And relating the wavelength of the applied disturbance to the nondimensional wavenumber )*ok ,

    which is held constant in experiment, the above equation for rdcan be rewritten as:

    31

    *3

    8

    =

    o

    odk

    rr

    The size of the droplets generated with a-m disturbances with integer frequency ratios is just

    rdN1/3. The droplet production rate can be written as:

    o

    o

    cr

    Vkf

    2

    *

    =

    or fc/N for droplets generated with integer frequency ratios. In the above, the stream speed (V) is

    estimated experimentally from conservation of mass measurements obtained by photographing

    the image of the droplet stream. The disturbance wavelength () was measured by averaging up

    to 20 inter-droplet spacings off of several video images. Knowledge of the driving frequency (fc)

    and wavelength () enables the estimate of stream speed V = fc. Measurements reveal that the

    balls are uniform to within 10.60% of the mean diameter without any sorting or sieving. Hence,

    droplet generation from capillary stream break-up provides a natural mechanism for highly

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    uniform ball formation.

    Figure 7 illustrates the microstructure in an individual solidified aluminum ball. The scale

    shown is 10 microns and hence, the small dimension of the grain size is on the order of 10

    microns. The use of such spheres is beneficial for a host of emerging applications and the

    production rate can be scaled-up by using arrays of orifices.

    M icrostr uctu ral Characterist i cs of N et-Form ed Component s

    Components were analyzed for their chemical composition and compared to the corresponding

    pre-jetted characteristics. It was found in all cases that the composition of the droplet-deposited

    components was consistent with AA2024 aluminum alloy, and therefore the process of droplet

    deposition does not significantly alter the alloy composition.

    Figure 8 illustrates the microstructure of a tube component fabricated in a manner as illustrated

    in Figure 1. The microstructure is sampled from a location at 5.0 mm from the substrate. It can

    be seen that the grain size is on the order of 50 m.

    Figure 9 shows the microstructure of a sample that was taken from a distance of 1l0 mm from the

    substrate fabricated with the same processing conditions. It can be seen that the grain size issignificantly larger than that of the corresponding sample closer to the substrate. The reason for

    the larger grain size is that the component temperature increases with increasing component

    height. This is because the droplets are delivered at a rate that is too high to allow for cooling

    prior to the arrival of the subsequent droplets. Hence, as the component grows, the depth of

    molten aluminum increases, thereby increasing the solidification time. It is well known that an

    increase in solidification time can be correlated to an increase in grain size. As mentioned

    earlier, current work is focused on modeling the heat flux required to locally remelt a thin layer

    of the previously solidified material in efforts to maintain a constant heat flux for any fabrication

    geometry.

    Figure 10 is a microphotograph of a component illustrating coarse precipitation zones. The

    reason for the coarse precipitation zones is that both the droplet temperature and the mass

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    delivered per unit length of substrate was higher than those for the components fabricated in

    Figures 8 and 9, thereby transferring more heat from the molten droplet stream to the component.

    Hardness

    It was found that the samples without the coarse precipitation zones had a hardness of over twice

    that of the raw stock, with typical BNH values in the range of 95-101. No significant difference

    in hardness was measured between samples obtained near the substrate or far from the substrate.

    The value of BNH hardness for sample shown in Figure 10 is 77, which is significantly lower

    than that of the other samples and it is concluded to be a result of the coarse precipitates that are

    observable in the micrograph and are due to elevated heating.

    Specifi c Gravi ty

    The specific gravity of specimens was found to vary from 2.62 to 2.71 g/cc, where the raw stock

    value of 2.70 g/cc is used as a reference. Hence, cylinders have been fabricated that are fully

    dense and devoid of measurable porosity. Even the specimen shown in Figure 10 is only 1.5%

    less dense than our reference value, yet the hardness is significantly lower than the other samples

    in this work. Hence, the generation of widespread coarse precipitates appears to be the

    influencing factor for the generation of softer components, and not the presence of porosity.

    5. Conclusions

    This paper describes the generation and deposition of molten aluminum alloy droplets for

    advanced manufacturing applications. Several important findings have been reported in this

    paper, which chronicles the development of the PDM process. The most important findings are

    summarized below.

    We have found that molten aluminum alloy droplets can be consistently generated from capillary

    stream break-up, provided that great care has been taken to remove traces of oxygen from the

    jetting environment, and to filter residual oxides from the melt, which both have the tendency to

    cause angular jitter in the droplet stream. Large concentrations of oxygen in the jetting

    environment will eliminate the possibility of generating droplets altogether. Measurements have

    revealed that aluminum alloy AA2024 droplets can be generated from capillary stream break-up

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    and deposited in an inert environment without deviation from specified alloy composition limits.

    Capillary stream break-up provides an attractive method for generating highly uniform metallic

    spheres at relatively high rates. Aluminum alloy AA2024 spheres have been fabricated at a rate

    of 18,000 spheres per second, which corresponds to 1.85 kg/hour for one orifice. Typical sample

    measurements reveal that the uniformity in sphere diameter is 0.60% of the average diameter.

    Molten aluminum-droplet deposition has been utilized for the fabrication of net-shape structures.

    Though the process is still immature, several important findings can be reported. 1) It has been

    found that structures as high as 11.0 cm can be formed (11.0 cm is the greatest height that our

    current apparatus will permit) with little measurable changes in component characteristics; 2)

    BNH of as-deposited material is roughly twice that of (annealed) raw stock; 3) an increase in

    hardness of 100% over the raw stock can be achieved under certain processing conditions and 4)

    fully dense components can be fabricated with this process.

    With respect to microstructural and mechanical properties of the manufactured components, it

    was found that the processing parameters that govern the geometric, mechanical and

    microstructural integrity of the net-formed component are coupled with each other. It was found

    that the most important factor is the heat flux received by the cylinder during droplet deposition.The heat flux can be affected by varying the mass delivered per unit length, the droplet

    temperature or the substrate temperature. Extreme heating of the cylinder through any of the

    mechanisms discussed above results in coarsely precipitated microstructure, which can reduce

    the hardness of the component. Additionally, extreme heat fluxes also thickened cylinder walls

    due to slow solidification times. It is also important, however, that the droplets not be too cool

    prior to impingement, else the droplet boundaries will remain intact thereby reducing the

    structural integrity of the component. Hence, there is a trade-off between high heat fluxes to

    reduce porosity and increase hardness and low heat fluxes for higher control over component

    geometry and finer microstructures.

    It is believed that the results presented here are an underestimate of the microstructural

    refinement and mechanical quality enhancements of the final realization of PDM technology.

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    This is because the droplets did not solidify as rapidly as they will in the final PDM technology

    since electrostatic charging and deflection was not employed in the present work. In the final

    realization of PDM, the droplets will be deflected to different locations on the substrate, allowing

    the splats to cool prior to the next splats arrival. In this manner, the temperature of the

    previously deposited and solidified material will not increase with time, allowing the droplets to

    rapidly solidify which leads to refined microstructures and enhanced mechanical properties.

    Acknowledgment: This work has received the generous support from Boeing Commercial

    Airplane Company (BCA-23483), Lawrence Livermore National Laboratories (B345710) and

    the National Science Foundation (DMI-9622400).

    References

    1. M. Orme and C. Huang, "Phase Change Manipulation for Droplet-Based Solid Freeform

    Fabrication of Aluminum Components,"ASME J. Heat Transfer, vol. 119, 1997, pp 818 832

    2. Q. Liu, C. Huang and M. Orme, "Mutual Electrostatic Interactions Between Closely Spaced

    Charged Solder Droplets"Journal of Atomization and Sprays, (in print, September 2000)

    3. E. P. Muntz, M. Orme, G. Pham-Van-Diep and R. Godin, "An Analysis of Precision, Fly-

    Through Solder Jet Printing for DCA Components" presented at the 30th International

    Symposium on Microelectronics, Pennsylvania, published by IMAPS -Int. Microelectronics

    Packaging Soc., Reston, VA, USA 1997, pp. 671-680

    4. M. Orme and E. P. Muntz, "The Manipulation of Capillary Stream Breakup Using Amplitude

    Modulated Disturbances: A Pictorial and Quantitative Representation," Phys. of Fluids, vol. 2,

    no. 7, 1990, pp. 1124 - 1140

    5. M. Orme, "On the Genesis of Droplet Stream Microspeed Dispersions," Physics of Fluids,

    vol. 3, no. 12, 1991, pp 2936 - 2947

    6. M. Orme, K. Willis and V. Nguyen, "Droplet Patterns from Capillary Streams," Physics of

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    Fluids, vol. 5, 1993, pp 80 - 90

    7. M. Orme, "A Novel Technique of Rapid Solidification Net-Form Materials Synthesis,"

    Journal of Materials Engineering and Performance, vol. 2, no. 3, 1993, pp 399 - 405

    8. M Orme, C. Huang and J. Courter, "Precision Droplet Based Manufacturing and Material

    Synthesis: Fluid Dynamic and Thermal Control Issues", ILASS Journal of Atomization and

    Sprays vol. 6, 1996, pp 305 - 329

    9. M. Orme and R. Smith, "Enhanced Aluminum Properties with Precise Droplet Deposition"

    ASME Journal of Manufacturing Science and Engineering, 2000 (in print, expected v. 122)

    10. E. M. Sachs, M. J. Cima, P. Williams, D. Brancazio and J. Cornie, "Three Dimensional

    Printing: Rapid Tooling and Prototypes Directly from a CAD Model" J. Eng. Ind., vol. 114, 481-

    488, 1992,

    11. E. Sachs, M. Cima, J. Bredt and A. Curodeau, "CAD-Casting: The Direct Fabrication of

    Ceramic Shells and Cores by Three Dimensional Printing, "Man. Rev., vol. 5, no. 2, pp 118-126

    1992

    12. T. Jackson, N. Patrikalakis, E. Sachs, and M. Cima, "Modeling and Designing Components

    with Locally Controlled Composition," Solid Freeform Fabrication Symposium, Austin, Texas,

    1998, pp. 259 - 266.

    13. F. B. Prinz, L. E. Weiss, C. H. Amon and J. L. Beuth, "Processing, Thermal and Mechanical

    Issues in Shape Deposition Manufacturing," Solid Freeform Fabrication Symposium, Austin,

    Texas, 1995, pp. 118-129.

    14. C. H. Amon, J. L. Beuth, R. Merz, F. B. Prinz, and L. E. Weiss, "Shape Deposition

    Manufacturing with Microcasting: Processing, Thermal and Mechanical Issues, ASME J.

    Manufacturing Science and Engineering,vol. 120, 1998, pp. 656-667.

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    15. J. Fessler, A. Nickel, G. Link, and F. Prinz, "Functional Gradient Metallic Prototypes

    through Shape Deposition Manufacturing" Solid Freeform Fabrication Symposium, Austin,

    Texas, USA, 1997, pp. 521 - 528.

    16. D. B. Bogy, "Drop Formation in a Circular Liquid Jet" Ann. Rev. Fluid Mech., vol. 11, 1979,

    pp. 207-228.

    17. M. J. McCarthy and N.A. Molloy, "Review of Stability of Liquid Jets and the Influence of

    Nozzle Design" Chem. Engineering, vol. 7, 1974, pp. 1-20.

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    Figure 1: Conceptual schematic of cylinder fabrication on a flat-plate substrate with controlled

    droplet deposition.

    Molten

    droplet

    stream

    Substrate motion

    Fabricate

    d

    Inert

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    Figure 2: Examples of preliminary components fabricated with PDM. The tall square tubeshown horizontally is 11.0 cm.

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    Figure 3: Schematic of experimental apparatus

    Droplet formation withan average inter-droplet

    spacing equal to

    Molten aluminum

    Cartridge

    orifice

    Stagnation pressure

    regulation

    Active coolingflange

    Periodic signal of

    wavelength topiezoelectric crystal

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    Figure 4: (a) evolution of droplets into modulation drops with an amplitude modulation ratioN=3, (b) amplitude modulated disturbance to the piezoelectric crystal

    (a)

    (b)

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    Figure 5: (a) evolution of droplets into a stable configuration of large-small-large with anamplitude modulation ratio N=3.5, (b) amplitude modulated disturbance to the piezoelectric

    crystal

    (a)

    (b)

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    Figure 6: SEM photograph of 2024 aluminum balls fabricated with capillary stream break-up

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    Accepted for publication inAluminum Transactions Journal, 2000

    Figure 7: Optical micrograph of cross-sections of several droplets illustrating grain structure(top view of a cut)

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    Accepted for publication inAluminum Transactions Journal, 2000

    Figure 8: Microstructure of aluminum cylinder sampled at 5.0mm from substrate

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    Accepted for publication inAluminum Transactions Journal, 2000

    Figure 9: Microstructure of cylinder sampled at 65mm from the substrate

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    Accepted for publication inAluminum Transactions Journal, 2000

    Figure 10: microstructure of a component that illustrates coarse precipitates