IP Library Granted Patent US 12,594,728
Granted Patent B2
US 12,594,728 · App. 18/400,673 · Granted Apr 7, 2026

Three-dimensional printing of hydrophobic materials in fumed silica suspension

Inventors: Yong Huang (Gainesville, FL); Yifei Jin (Gainesville, FL); Nevada J. Gellermann (Gainesville, FL); Kaidong Song (Gainesville, FL)
Assignee: UNIVERSITY OF FLORIDA RESEARCH FOUNDATION, INCORPORATED
B29C64/40B33Y10/00B33Y70/00B29K2063/00B29K2083/00
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Quick Facts
Patent No.
US 12,594,728
App. No.
18/400,673
Granted
Apr 7, 2026
Kind
B2
Abstract

A three-dimensional (3D) printing methodology is disclosed for freeform fabrication of hydrophobic structures without the use of printed support structures. The build material is directly printed in and supported by a fumed silica-containing yield-stress support bath to form an intermediate article in the support bath material. The intermediate article may be liquid or only partially solidified after being printed into the support bath material. The intermediate article is then heated or irradiated with ultraviolet radiation to initiate cross-linking to solidify the printed intermediate article, forming a finished article.

Claims (43)

1 . A method comprising:

disposing a mass of hydrophobic fumed silica nanoparticles in a volume of a mineral oil to achieve a concentration of the hydrophobic fumed silica nanoparticles in the mineral oil of between about 2% (w/v) and about 8% (w/v) to form a heterogenous mixture;

mixing the heterogenous mixture to form a homogenous mixture comprising the mass of hydrophobic fumed silica nanoparticles dispersed throughout the volume of the mineral oil;

centrifuging the homogenous mixture comprising the mass of hydrophobic fumed silica nanoparticles dispersed throughout the volume of the mineral oil to form a hydrophobic yield-stress support material; and

disposing a volume of a hydrophobic printing material into the hydrophobic yield-stress support material to form an intermediate article having particular dimensions and a particular form factor.

2 . The method of claim 1 , wherein the mixing the heterogenous mixture to form the homogenous mixture is carried out for between about 10 minutes and about 120 minutes.

3 . The method of claim 1 , wherein the centrifuging the homogenous mixture is carried out for between about one minute and about 30 minutes.

4 . The method of claim 1 , wherein a plurality of microbubbles trapped are initially trapped in the homogeneous mixture of hydrophobic fumed silica nanoparticles in the mineral oil, and wherein the centrifuging the homogenous mixture removes at least a portion of the microbubbles trapped in the homogenous mixture.

5 . The method of claim 1 , wherein the hydrophobic fumed silica nanoparticles have an average diameter of between about 5 nm and about 500 nm.

6 . The method of claim 1 , wherein a concentration of the hydrophobic fumed silica nanoparticles in the mineral oil is about 6% (w/v).

7 . The method of claim 1 , further comprising:

allowing the homogenous mixture to age for greater than a day to form a stable colloidal suspension therein of the mass of hydrophobic fumed silica nanoparticles in the volume of the mineral oil.

8 . The method of claim 7 , wherein the centrifuging the homogenous mixture forms a plurality of fumed silica aggregates from the hydrophobic fumed silica nanoparticles dispersed in the mineral oil.

9 . The method of claim 8 , wherein the fumed silica aggregates have an average aggregate size of between about 100 nm and about 500 nm.

10 . The method of claim 7 , wherein the allowing the homogenous mixture to age for greater than a day comprises maintaining a temperature of the homogeneous mixture between about 25 degrees Celsius and about 100 degrees Celsius, and wherein, after the allowing the homogenous mixture to age, the plurality of fumed silica aggregates are structurally resistant to perturbations of the hydrophobic yield-stress support material.

11 . The method of claim 1 , wherein the centrifuging the homogenous mixture is carried out at a centrifugal speed of between about 1,000 rotations per minute (RPM) and about 5,000 RPM.

12 . A method comprising:

forming a heterogenous mixture of hydrophobic fumed silica nanoparticles and mineral oil, the heterogenous mixture having a concentration of the hydrophobic fumed silica nanoparticles in the mineral oil of between about 2% (w/v) and about 8% (w/v);

mixing the heterogeneous mixture of hydrophobic fumed silica nanoparticles and mineral oil to form a homogenous mixture in which the hydrophobic fumed silica nanoparticles are at least partially dispersed within the mineral oil;

centrifuging the homogenous mixture to form a colloidal suspension of the hydrophobic fumed silica nanoparticles within the mineral oil;

allowing the colloidal suspension of the hydrophobic fumed silica nanoparticles within the mineral oil to rest for greater than a minimum rest duration to stabilize the colloidal suspension and form a hydrophobic yield-stress support material; and

disposing one or more volumes of a hydrophobic printing material into the hydrophobic yield-stress support material to form an intermediate article having particular dimensions and a particular form factor,

wherein, during a time period following the disposing of the one or more volumes of the hydrophobic printing material into the hydrophobic yield-stress support material to form the intermediate article, the one or more volumes of the hydrophobic printing material are substantially immobilized in order to maintain the particular dimensions and the particular form factor of the intermediate article.

13 . The method of claim 12 , wherein the mixing the heterogenous mixture to form the homogenous mixture is carried out for between about 10 minutes and about 120 minutes.

14 . The method of claim 12 , wherein the centrifuging the homogenous mixture is carried out for between about 1 minute and about 30 minutes.

15 . The method of claim 12 , wherein the homogeneous mixture comprises a plurality of microbubbles trapped in the homogenous mixture of hydrophobic fumed silica nanoparticles in the mineral oil, and wherein the centrifuging the homogenous mixture removes at least a portion of the plurality of microbubbles trapped in the homogenous mixture.

16 . The method of claim 12 , wherein the hydrophobic fumed silica nanoparticles have an average diameter of between about 5 nm and about 500 nm.

17 . The method of claim 12 , wherein the concentration of the hydrophobic fumed silica nanoparticles in the mineral oil is about 6% (w/v).

18 . The method of claim 12 , wherein the forming the heterogenous mixture of hydrophobic fumed silica nanoparticles and mineral oil comprises disposing a mass of the hydrophobic fumed silica nanoparticles into a volume of the mineral oil to achieve the concentration of the hydrophobic fumed silica nanoparticles in the mineral oil of between about 2% (w/v) and about 8% (w/v).

19 . The method of claim 12 , wherein, the centrifuging the homogenous mixture causes formation of a plurality of fumed silica aggregates from the hydrophobic fumed silica nanoparticles dispersed in the mineral oil.

20 . The method of claim 19 , wherein the fumed silica aggregates have an average aggregate size of between about 100 nm and about 500 nm.

21 . The method of claim 12 , wherein the allowing the colloidal suspension of the hydrophobic fumed silica nanoparticles within the mineral oil to rest for greater than the minimum rest duration to stabilize the colloidal suspension and form the hydrophobic yield-stress support material is performed for greater than about one hour while the colloidal suspension is maintained a temperature between about 25 degrees Celsius to about 100 degrees Celsius.

22 . The method of claim 12 , wherein the centrifuging the homogenous mixture is carried out at a centrifugal speed of between about 1,000 rotations per minute (RPM) and about 5,000 RPM.

23 . A method, comprising:

mixing a mass of hydrophobic fumed silica nanoparticles having an average diameter of between about 5 nm and about 500 nm into a volume of mineral oil to form a homogeneous mixture, the homogeneous mixture having a hydrophobic fumed silica nanoparticle concentration in the mineral oil of between about 2% (w/v) and about 8% (w/v), wherein the mixing causes the hydrophobic fumed silica nanoparticles to become dispersed throughout the mineral oil, and wherein the mixing also causes a plurality of microbubbles to become trapped in the homogeneous mixture;

centrifuging the homogenous mixture at between about 1,000 rotations per minute and about 5,000 rotations per minute for between about one minute and about 30 minutes to remove at least a portion of the plurality of microbubbles trapped in the homogeneous mixture, thereby forming a colloidal suspension of the hydrophobic fumed silica nanoparticles within the mineral oil;

maintaining a temperature of the colloidal suspension at a temperature of between about 25 degrees Celsius to about 100 degrees Celsius for greater than a minimum rest duration to form a plurality of hydrophobic fumed silica aggregates having an average aggregate size of between about 100 nm and about 500 nm, the plurality of hydrophobic fumed silica aggregates being formed through aggregation of the hydrophobic fumed silica nanoparticles dispersed within the mineral oil in the colloidal suspension, thereby structurally stabilizing the colloidal suspension and forming a hydrophobic yield-stress support material; and

disposing one or more volumes of a hydrophobic printing material into the hydrophobic yield-stress support material to form an intermediate article having particular dimensions and a particular form factor,

wherein, during a time period following the disposing the one or more volumes of the hydrophobic printing material into the hydrophobic yield-stress support material to form the intermediate article, the particular dimensions and the particular form factor of the intermediate article are substantially maintained.

24 . The method of claim 1 , wherein, during a time period following the disposing the volume of the hydrophobic printing material into the hydrophobic yield-stress support material to form the intermediate article, the particular dimensions and the particular form factor of the intermediate article are substantially maintained.

25 . The method of claim 1 , wherein the disposing the one or more volumes of the hydrophobic printing material into the hydrophobic yield-stress support material is carried out using one or more nozzles moving along a predefined pathway through the hydrophobic yield-stress support material.

26 . The method of claim 12 , wherein the disposing the one or more volumes of the hydrophobic printing material into the hydrophobic yield-stress support material is carried out using one or more nozzles moving along a predefined pathway through the hydrophobic yield-stress support material.

27 . The method of claim 23 , wherein the disposing the one or more volumes of the hydrophobic printing material into the hydrophobic yield-stress support material is carried out using one or more nozzles moving along a predefined pathway through the hydrophobic yield-stress support material.

Assignments (1)
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Dec 29, 2023
From: HUANG, YONG; JIN, YIFEI; GELLERMANN, NEVADA J.; SONG, KAIDONG
To: UNIVERSITY OF FLORIDA RESEARCH FOUNDATION, INCORPORATED
Reel/Frame 065983/0856 →
Continuity (4)
Continuation 17870424 · Jul 21, 2022
Division 16707087 · Dec 9, 2019
Provisional Application 62783267 · Dec 21, 2018
Related Publication 20240269934A1 · Aug 15, 2024
References Cited (40)
US 10974441B2 · Huang et al. · 2021 [cited by applicant]
US 11426945B2 · Huang · 2022 [cited by examiner]
US 11759999B2 · Huang et al. · 2023 [cited by applicant]
US 12017414B2 · Huang · 2024 [cited by examiner]
US 20100059704A1 · Davis · 2010 [cited by examiner]
US 20100297213A1 · Dupont et al. · 2010 [cited by applicant]
US 20160067918A1 · Millar · 2016 [cited by applicant]
US 20160250808A1 · Barnwell, III et al. · 2016 [cited by applicant]
US 20180021140A1 · Angelini et al. · 2018 [cited by applicant]
US 20180281295A1 · Tibbits et al. · 2018 [cited by applicant]
US 20180282923A1 · Carlyle et al. · 2018 [cited by applicant]
US 20180370116A1 · Huang et al. · 2018 [cited by applicant]
US 20190092951A1 · Wang et al. · 2019 [cited by applicant]
US 20190375149A1 · Limem et al. · 2019 [cited by applicant]
US 20200198251A1 · Huang et al. · 2020 [cited by applicant]
US 20200307068A1 · Huang et al. · 2020 [cited by applicant]
US 20210237340A1 · Huang et al. · 2021 [cited by applicant]
US 20230226772A1 · Huang et al. · 2023 [cited by applicant]
US 20240208137A1 · Huang et al. · 2024 [cited by applicant]
WO WO2015017421A2 · 2015 [cited by applicant]
Hauschild SpeedMixer. “Product—Hauschild Speedmixer 150-250 Series”. Retrieved from https://hauschild-speedmixer.com/products/speedmixer/laboratory-mixers/dac-overview/model-series-150-200/ on Apr. 24, 2025. [cited by examiner]
Hinton, Thomas J. et al. [cited by applicant]
Jin, Yifei et al. [cited by applicant]
Jin, Yifei et al. [cited by applicant]
Jin, Yifei et al. [cited by applicant]
O'Bryan, Christopher S. et al. [cited by applicant]
Hinton, Thomas J. et al. [cited by applicant]
O'Bryan, Christopher S. et al. (2017). [cited by applicant]
Bhattacharjee, Tapomoy et al. [cited by applicant]
Notice of Allowance and Fee(s) Due for U.S. Appl. No. 16/703,686, Jan. 28, 2021, (11 pages), United States Patent and Trademark Office, USA. [cited by applicant]
Final Office Action for U.S. Appl. No. 16/707,087, dated Dec. 29, 2021, (17 pages), United States Patent and Trademark Office. [cited by applicant]
Grosskopf, Abigail K. et al. [cited by applicant]
Advisory Action for U.S. Appl. No. 16/707,087, dated Mar. 22, 2022, (4 pages), United States Patent and Trademark Office, USA. [cited by applicant]
NonFinal Office Action for U.S. Appl. No. 16/707,087, dated Aug. 3, 2021, (18 pages), United States Patent and Trademark Office, USA. [cited by applicant]
NonFinal Office Action for U.S. Appl. No. 16/781,336, dated Feb. 22, 2022, (18 pages), United States Patent and Trademark Office, USA. [cited by applicant]
Whitby, Catherine P. et al. “Understanding The Role of Hydrogen Bonding in the Aggretation of Fumed Silica Particles in Triglyceride Solvents,” Journal of Colloid and Interface Science, vol. 527, May 12, 2018, pp. 1-9. [cited by applicant]
Notice of Allowance and Fee(s) Due for U.S. Appl. No. 16/707,087, dated Apr. 25, 2022, (23 pages), United States Patent and Trademark Office, US. [cited by applicant]
NonFinal Office Action for U.S. Appl. No. 16/781,336, dated Aug. 3, 2022, (12 pages), United States patent and Trademark Office, US. [cited by applicant]
U.S. Appl. No. 17/870,424, filed Jul. 21, 2022, 2023-02267772. [cited by applicant]
U.S. Appl. No. 16/707,087, filed Dec. 9, 2019, U.S. Pat. No. 11,426,945. [cited by applicant]