Heat, mass, and fluid flow in a solar reactor for fullerene synthesis

Citation
T. Guillard et al., Heat, mass, and fluid flow in a solar reactor for fullerene synthesis, J SOL ENERG, 123(2), 2001, pp. 153-159
Citations number
17
Categorie Soggetti
Environmental Engineering & Energy
Journal title
JOURNAL OF SOLAR ENERGY ENGINEERING-TRANSACTIONS OF THE ASME
ISSN journal
01996231 → ACNP
Volume
123
Issue
2
Year of publication
2001
Pages
153 - 159
Database
ISI
SICI code
0199-6231(200105)123:2<153:HMAFFI>2.0.ZU;2-L
Abstract
Experimental results with a 2 kW solar furnace, in a wide range of vaporiza tion rates (0.1-4 g/h), under variable pressure and flow rate of argon, are used with numerical simulation to define key parameters for large scale sy nthesis of fullerenes with solar energy. The vaporization process is contro lled by diffusion in the temperature and pressure ranges 3000-3700 K and 70 -250 hPa respectively. In the solar reactor; fullerene yield is governed by the dilution of carbon vapor in argon and the temperature gradient in the cooling zone. Criteria for both parameters are suggested. Consequently, the se data, combined with a validated numerical model of the reactor may be us ed for the design of large-scale solar process.