journal article·2001-08

Nanoparticle Microreactor: Application to Synthesis Of Titania by Thermal Decomposition of Titanium Tetraisopropoxide

K.Y. Park, M. Ullmann, Y.J. Suh, S.K. Friedlander

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Abstract

The nanoparticle microreactor (NPMR) is a new concept that we have introduced to describe a very small-scale system capable of converting an aerosol precursor to solid particles. The liquid precursor of about 1 µl is injected by a syringe through a septum into a tubular evaporator of 1.0 cm3 in volume with stopcocks at both ends. The evaporator has been preheated by a heating tape to a temperature sufficiently high for vaporization to occur in half a minute. By opening the stopcocks, the vaporized precursor is transported by a carrier gas stream into a quartz tube which is mounted along the axis of a tubular furnace. The nanoparticle aggregates produced in the reactor are sampled by deposition on an electron micrograph grid at the reactor exit. The NPMR was applied first to the synthesis of TiO2 particles by thermal decomposition of titanium tetraisopropoxide (TTIP) in a nitrogen carrier gas, with TTIP concentrations varying from 1.0 to 7.0 mol% or 2.35×10−6 to 1.65×10−5 in TiO2 volume loading, and decomposition temperatures from 300°C to 1000°C. Studies were made with a 2 mm reaction tube and a 4 mm tube with sheath gas. With the 2 mm tube, a considerable fraction of the TTIP precursor was consumed at the wall by surface reaction, resulting in very small particles. With the 4 mm tube, the primary particle size was comparable to that reported in the literature for steady flow experiments using a 22.2 mm tube. Primary particle sizes ranged from 200 to 400 nm. Depending on TTIP concentration and reactor temperature, the particles exhibited a bimodal size distribution, probably due to a two-stage nucleation. A fourfold increase in the gas flow rate had little effect on particle size, indicating that particle growth ended early, within one-fourth the tube length. Residence time in the reactor was between 0.35 and 1.4 s, and total run time about 1 min. The NPMR has potential for rapid assembly of large databases and is adaptable to combinatorial discovery of nanoparticles with novel properties. Design requirements for an ‘ideal’ aerosol microreactor are discussed briefly.
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OpenAlex topics: Catalytic Processes in Materials Science · Industrial Gas Emission Control

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References (17)

Show source-provided references
1. Akhtar K.M., Y. Xiong & S.E. Pratsinis, 1991. Vapor synthesis of titania powder by titanium tetrachloride oxidation. AIChE J. 37, 1561–1570.10.1002/aic.690371013 ↗
2. Alam M.K. & R.C. Flagan, 1986. Controlled nucleation aerosol reactors: Production of bulk silicon. Aerosol Sci. Technol. 5, 237–248.10.1080/02786828608959090 ↗
3. Carrizosa I. & G. Munuera, 1977. Study of the interaction of aliphatic alcohols with TiO2. I. Decomposition of ethanol, 2-propanol, and tert-butanol on anatase. J. Catal. 49, 174–188.10.1016/0021-9517(77)90253-6 ↗
4. Dagani R., 1999. A faster route to new materials. Chem. Eng. News, 8 March, 1999, 51–60.10.1021/cen-v077n010.p051 ↗
5. Fictorie C.P., J.F. Evans & W.L. Gladfelter, 1994. Kinetic and mechanistic study of the chemical vapor deposition of titanium dioxide thin films using tetrakis-(isopropoxo)-titanium(IV). J. Vac. Sci. Technol. A 12, 1108–1113.10.1116/1.579173 ↗
6. Formenti M., F. Juillet, P. Meriaudeau, S.J. Teichner & P. Vergnon, 1972. Preparation in a hydrogen-oxygen flame of ultrafine metal oxide particles. In: Hidy G.M. ed. Aerosols and Atmospheric Chemistry. Academic Press, New York, pp. 45–54.10.1016/B978-0-12-347250-2.50007-0 ↗
7. Jang H.D. & J. Jeong, 1995. The effects of temperature on particle size in the gas-phase production of TiO2. Aerosol Sci. Technol. 23, 553–560.10.1080/02786829508965337 ↗
8. Jang H.D. & S.K. Friedlander, 1998. Restructuring of chain aggregates of titania nanoparticles in the gas phase. Aerosol Sci. Technol. 29, 81–91.10.1080/02786829808965553 ↗
9. Kirkbir F. & H. Komiyama, 1987. Formation and growth mechanism of porous, amorphous, and fine particles prepared by chemical vapor deposition. Titania from titanium tetraisopropoxide. Can. J. Chem. Eng. 65, 759–766.10.1002/cjce.5450650508 ↗
10. Komiyama H., T. Kanai & H. Inoue, 1984. Preparation of porous, amorphous, and ultrafine TiO2 particles by chemical vapor deposition. Chem. Lett. 1984, 1283–1286.10.1246/cl.1984.1283 ↗
11. Okuyama K., Y. Kousaka, N. Tohge, S. Yamamoto, J.J. Wu, R.C. Flagan & J.H. Seinfeld, 1986. Production of ultrafine metal oxide aerosol particles by thermal decomposition of metal alkoxide vapors. AIChE J. 32, 2010–2019.10.1002/aic.690321211 ↗
12. Park K.Y., H.D. Jang & C.S. Choi, 1991. Generation of ultrafine iron powders by gas-phase reduction of ferrous chloride with hydrogen. J. Aerosol Sci. 22, S113–S116.10.1016/S0021-8502(05)80047-3 ↗
13. Pratsinis S.E. & T.T. Kodas, 1993. Manufacturing of materials by aerosol processes. In: Willeke K. & Baron P.A. eds. Aerosol Measurement. John Wiley, USA, pp. 721–746.
14. Satake T., T. Sorita & H. Adachi, 1996. Kinetic and theoretical study of the thermal decomposition of tetraethoxysilane in the gas phase. In: Besmann T.M., Allendorf M.D., Robinson Mc D. & Ulrich R.K. eds. Proceedings of the Thirteenth International Conference on Chemical Vapor Deposition, Los Angeles, CA, USA, 5-10 May, pp. 23–28.
15. Suyama Y. & A. Kato, 1976. TiO2 produced by a vapor-phase oxygenolysis of TiCl4. J. Am. Ceram. Soc. 59, 146–149.10.1111/j.1151-2916.1976.tb09453.x ↗
16. Ulrich G.D., 1971. Theory of particle formation and growth in oxide synthesis flames. Combust. Sci. Technol. 4, 47–57.10.1080/00102207108952471 ↗
17. Windeler R.S., Kari E.J. Lehtinen & S.K. Friedlander, 1997. Production of nanometer-sized metal oxide particles by gas phase reaction in a free Jet. II: Particle size with neck formation - comparison with theory. Aerosol Sci. Technol. 27, 191–205.10.1080/02786829708965466 ↗