J. Am. Ceram. Soc., 87 [3] 523–25 (2004)
journal
Dynamics of Hollow and Solid Alumina Particle Formation in
Spray Flames
Takao Tani and Kazumasa Takatori†
Toyota Central Research and Development Laboratories, Inc., Nagakute, Aichi 480-1192, Japan
Sotiris E. Pratsinis
Particle Technology Laboratory, Department of Mechanical and Process Engineering,
Swiss Federal Institute of Technology (ETH) Zurich, CH-8092 Zurich, Switzerland
Thermophoretic sampling (TS) of the aerosol was conducted to
manifest the formation of hollow and solid alumina particles in
spray flames. The collected particles were investigated by
transmission electron microscopy. Hollow particles with a thin
shell (e.g., 10 nm) were formed from the aluminum nitrate
precursor emulsion at less than 4-cm flame height. Hollow
particles maintained their shapes in the flame using air as
dispersion/oxidant gas, whereas hollow-to-solid restructuring
of the particles took place in the flame using oxygen. With
oxygen, nanoparticles were formed in the gas phase from the
aluminum butoxide/2-propanol precursor solution only,
whereas gas-phase reaction was hindered, forming large par-
ticles from the aluminum nitrate/2-propanol precursor solu-
tion.
(AB)-derived alumina particles by the solution-fed FSP using
2-propanol as solvent.
II. Experimental Procedure
The AN nonahydrate (Wako, S grade) was dissolved in deion-
ized water, which was mixed with kerosene (Wako) and a
surfactant (hexa(2-hydroxy-1,3-propylene glycol) diricinoleate
(Taiyo Kagaku, Sunsoft 818H) at a volume ratio of 65 (AN
aqueous solution)/33 (kerosene)/2 (surfactant). The mixture was
stirred at 10 000 rpm for 10 min, forming the w/o emulsion of 1
mol/L precursor concentration, where aqueous microspheres of
1–2-m size were dispersed in the oil phase. The AN was
dissolved also in a mixture of 90 vol% 2-propanol (Wako, S grade)
and 10 vol% methanol (Wako, S grade) to obtain a 1 mol/L
solution. A 75 wt% AB/butanol solution (Gelest) was diluted with
2-propanol to 1 mol/L.
The detailed configuration of the FSP reactor was reported
elsewhere.10 The total methane and oxygen flow rates of the
supporting flames were 3 L/min each, while 12 mL/min precursor
solution was dispersed by air or oxygen of 11 L/min. Air of 45
L/min or oxygen of 15 L/min was supplied to the main flame
through a porous metal plate surrounding the nozzle for excess
oxidant when using air or oxygen, respectively, as dispersion gas.
Air was not used as dispersion/oxidant gas when dispersing the
2-propanol solutions because of an insufficient amount of oxidant.
A schematic of the equipment for TS is shown in Fig. 1. A copper
(Cu) mesh (3-mm diameter) covered with carbon film was set on
the edge of the sampling rod, which was driven by air of 2 atm at
1 m/s average velocity and held below the nozzle for 50 ms to
collect particles in the spray flame. The sampling time was
controlled by a timer setting. The TS was conducted at positions of
4, 6, and 8 cm below the nozzle along the central flame axis. It was
difficult to obtain particles at only 2 cm below the nozzle because
of melting of the Cu mesh. Even at sampling positions further
away, the carbon film was burned out, and therefore particles
attached with the Cu mesh were observed for some cases. The
particle morphology was observed by transmission electron mi-
croscopy (TEM: Nihon Denshi, JEM2000EX, 200 kV). The
particles are labeled by precursor (AN ϭ N or AB ϭ B)–process
(emulsion-fed FSP ϭ E or solution-fed FSP ϭ F)–dispersion/
oxidant gas (air ϭ A or oxygen ϭ O), so the nitrate-derived
alumina particles made by the emulsion-fed FSP using air as
dispersion/oxidant gas is labeled N-E-A.
I. Introduction
N
EMULSION-FED flame spray pyrolysis (FSP), the so-called
A
emulsion combustion method,1 is an elegant process to make
oxide particles by spraying and combusting a water-in-oil (w/o)
emulsion. It differs from the standard organic solution-fed FSP,2–4
because a high-content aqueous phase (e.g., 65 vol%) in the
precursor emulsion decreases the flame temperature, favoring
precipitation of the precursor in the liquid phase5 as in spray
pyrolysis (SP)6 rather than precursor evaporation and oxidation as
in the gas-phase route for particle formation.4
The emulsion-fed FSP of aluminum nitrate (AN) or aluminum
chloride using air as dispersion/oxidant gas made unique hollow
alumina particles which can be attractive for insulating and
lightweight filler materials as well as catalyst carriers because of
their small size (submicrometer), very thin shell (ϳ10 nm), and
high specific surface area (ϳ50 m2/g).5 Enhanced surface precip-
itation by combustion of the oil phase is considered to form the
hollow particles in both cases using the nitrate and chloride as
precursor. On the other hand, oxygen as dispersion/oxidant gas
increased the flame temperature, enhancing restructuring of the
hollow particles in the hot zone,7 resulting in solid particles from
the same AN precursor emulsion.5 In this study, thermophoretic
sampling (TS)8,9 of the aerosol in the spray flame was conducted
to demonstrate the evolution of hollow and solid alumina particle
formation in the emulsion spray flames. In addition, the results
were compared with those of the AN- or aluminum butoxide
A. Krell—contributing editor
III. Results and Discussion
Figure 2 shows the evolution of the alumina particle growth in
the emulsion spray flames (emulsion-fed FSP) using (a) air
Manuscript No. 10530. Received September 15, 2003; approved October 28, 2003.
†Author to whom correspondence should be addressed.
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