flame aerosol reactors

Keyword(s):  
1998 ◽  
Vol 520 ◽  
Author(s):  
H. Briesen ◽  
A. Fuhrmann ◽  
S. E. Pratsinis

ABSTRACTNanostructured materials have distinctly different properties than the bulk because the number of atoms or molecules on their surface is comparable to that inside the particles creating a number of new materials and applications. Despite this potential for nanoparticles, very few practical applications have been developed because of the current high cost of these materials ($100/lb). On the other hand, flame aerosol reactors are routinely used for inexpensive production (∼$1/lb) of submicron sized commodities such as carbon blacks, pigmentary titania, fumed silica and preforms for optical fibers in telecommunications. Flame technology can be used also for synthesis of nanoparticles with precisely controlled characteristics. In these reactors, gas mixing is used to widely control the primary particle size and crystallinity of product powders while electric fields can be used to narrowly control the primary, and aggregate particle size and crystallinity. Here the application of axial electrical fields on a silica producing flame using hexamethyldisiloxane (HMDS) as precursor is presented. Experiments varying the precursor delivery rate corresponding to total production rates of 10, 20 and 30 g/h are presented. Electric fields decreased the particle size by electrostatic dispersion and repulsion of charged particles and by the reduced particle residence time inside the flame.


1996 ◽  
Vol 88 (3) ◽  
pp. 261-266 ◽  
Author(s):  
M. Sadakata ◽  
Y.B. Xu ◽  
A. Harano

Langmuir ◽  
1991 ◽  
Vol 7 (8) ◽  
pp. 1807-1814 ◽  
Author(s):  
Hung V. Nguyen ◽  
Richard C. Flagan

AIChE Journal ◽  
1988 ◽  
Vol 34 (8) ◽  
pp. 1249-1256 ◽  
Author(s):  
Jin Jwang Wu ◽  
Hung V. Nguyen ◽  
Richard C. Flagan ◽  
Kikuo Okuyama ◽  
Yasuo Kousaka

1998 ◽  
Vol 4 (3) ◽  
pp. 233-246 ◽  
Author(s):  
B. D. Shaw

Nonlinear evolution equations based upon moments of the aerosol size distribution function are solved asymptotically for constant-rate aerosol reactors (i.e., where condensible monomer is added at a constant rate) operating in the free-molecular limit. The governing equations are nondimensionalized and a large parameter that controls nucleation behavior is identified. Asymptotic analyses are developed in terms of this parameter. Comparison of the asymptotic results with direct numerical integration of the governing equations is favorable. The asymptotic results provide a simplified analytical approach to estimating average particle sizes, particle number densities, and peak supersaturation values for constant-rate aerosol reactors.


AIChE Journal ◽  
1999 ◽  
Vol 45 (10) ◽  
pp. 2097-2107 ◽  
Author(s):  
Andreas Bensberg ◽  
Paul Roth ◽  
Reinhard Brink ◽  
Helmut Lange
Keyword(s):  

2001 ◽  
Vol 114 (1-3) ◽  
pp. 197-204 ◽  
Author(s):  
Zhong-Min Wang ◽  
Guixiang Yang ◽  
Pratim Biswas ◽  
Wayne Bresser ◽  
Punit Boolchand

Author(s):  
Julia F. Haltiwanger ◽  
Luke J. Venstrom ◽  
Jane H. Davidson

One approach proposed for the exothermic step of the solar Zn/ZnO thermochemical water-splitting cycle is synthesis and hydrolysis of Zn nanoparticles in an aerosol reactor. To date the most common method to quantify the extent of conversion from Zn to ZnO is ex-situ X-ray diffraction analysis of particles collected on a filter placed at the exit of the reactor. The assumption inherent in this approach is that captured particles do not react on the filter because of its relatively low temperature. In the present study, we assess this assumption using data collected on hydrolysis of Zn nanoparticles at temperatures between 360 and 465 K and discuss methods of quantitative analysis via X-ray diffraction (XRD). Zn nanoparticles synthesized via condensation in an argon carrier gas are captured on a filter. Once the particles are collected, steam is introduced to the reactor at controlled partial pressure and temperature. The extent of reaction at the filter is characterized via calibrated XRD. At and below 380 K the reaction is negligible. At 465 K, the rate of conversion is slow at 0.007 ± 0.001%/min. In most cases, quantifying the extent of conversion from Zn to ZnO in the aerosol by ex-situ X-ray diffraction analysis of particles collected on the filter is an acceptable approach, though care should be taken in both the application of this method and in the quantitative analysis of the XRD data.


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