Effect of Porous and Nonporous Carbonaceous
Substrates on Polystyrene Thermal Degradation during
Fast CO
2
Laser Heating
Ashish Tripathi,
†
Chris L. Vaughn,
†
Waleed Maswadeh,
‡
and
Henk L. C. Meuzelaar*
,†
Center for Microanalysis and Reaction Chemistry, The University of Utah, Salt Lake City,
Utah 84112, and 2-Geo-Centers, E3220 Aberdeen Proving Grounds, Maryland 21010
Received November 17, 1998
To investigate the effect of porosity on elution of volatiles from a devolatilizing coal particle
under pulverized coal combustion (PCC) type heating rate conditions, polystyrene was doped
into porous model char (Spherocarb) particles and also coated on the surface of nonporous model
char (Glassy Carbon) particles. Particles of approximately 80 μm(( 10 μm) diameter were then
individually handpicked. These 80 μm diameter particles were heated to a temperature in the
range of 1200-2000 K in 32 ms by means of two converging CO
2
laser beams. The eluted products
were analyzed by combined gas chromatography/mass spectrometry (GC/MS). The evolved product
information was used to construct yield curves. These yield curves were compared to a simple
first-order rate law prediction. It was observed that while the styrene yield profile was predicted
satisfactorily in the case of nonporous Glassy Carbon, styrene evolution rates were approximately
four times slower than predicted in the case of porous Spherocarb. Also, the ratio of secondary
pyrolysis products of polystyrene (benzene, toluene, etc.) to a primary pyrolysis product (styrene)
was approximately four times higher in the case of Spherocarb than in the Glassy Carbon case.
Both findings strongly suggest the presence of transport limitations in porous Spherocarb under
PCC-type heating rate conditions.
Introduction
The focus of this study is to investigate the effect of
porosity on the release of products from small carbon-
aceous particles (40-100 μm diameter) at the very high
heating rates (approximately 10
5
K/s) characteristic of
PCC conditions.
1
To achieve these conditions, we con-
structed and tested the CO
2
laser pyrolysis system
(shown in Figure 1).
2-5
Porous (Spherocarb) and non-
porous (Glassy Carbon) spherical particles were selected
as the carbonaceous substrates, and polystyrene was
chosen as the model polymer for these studies. Not only
is polystyrene one of the most extensively studied and
characterized polymers,
6-22
but also it has some degree
of structural resemblance to coal in that alkylaromatic
“tar” components are produced upon pyrolysis.
23-28
Hence, studying the thermal degradation behavior of
polystyrene in the presence of porous and nonporous
carbonaceous substrates could help shed light on the
effect of porosity on the elution of similar products from
coal.
* Corresponding author.
†
The University of Utah.
‡
Aberdeen Proving Grounds.
(1) Smoot, L. D.; Smith, P. J. Coal Combustion and Gasification;
Plenum Press: New York, 1985.
(2) Maswadeh, W.; Arnold, N. S.; McClennen, W. S.; Tripathi, A.;
DuBow, J.; Meuzelaar, H. L. C. Energy Fuels 1993, 7, 1006.
(3) Maswadeh, W.; Tripathi, A.; Arnold, N. S.; DuBow, J.; Meuzelaar,
H. L. C. J. Anal. Appl. Pyrolysis 1994, 28, 55.
(4) Maswadeh, W., Ph.D. Thesis, 1995.
(5) Tripathi, A., Ph.D. Thesis, 1997.
(6) Tanaka, M.; Shimono, T.; Yabuki, Y.; Shono, T. J. Anal. Appl.
Pyrolysis 1980, 2, 207.
(7) Urbas, E.; Kaljurand, M.; Ku ¨ llik, E. J. Anal. Appl. Pyrolysis 1980,
3, 213.
(8) Bouster, C.; Vermande, P.; Vernon, J. J. Anal. Appl. Pyrolysis
297, 1980,
(9) Sousa Pessoa De Amorim, M. T.; Bouster, C.; Vermande, P.;
Vernon, J.; J. Anal. Appl. Pyrolysis 1981, 19.
(10) Trojer, L. J. Anal. Appl. Pyrolysis 1981, 2, 353.
(11) Toh, H. K.; Funt, B. L. J. Appl. Polym. Sci. 1982, 27, 4171.
(12) Brauman, S. K.; Chen, I. J.; Matzinger, D. P. J. Polym. Sci.,
Polym. Chem. Ed. 1983, 21, 1831.
(13) Ide, S.; Nanabu, H.; Kuroki, T.; Ikemura, T. J. Anal. Appl.
Pyrolysis 1984, 6, 69.
(14) Szekely, T.; Varhegyi, G.; Till, F.; Szabo, P.; Jakab, E. J. Anal.
Appl. Pyrolysis 1987, 11, 83.
(15) Dean, L.; Groves, S.; Hancox, R.; Lamb, G.; Lehrle, R. S. Polym.
Degrad. Stab. 1989, 25, 143.
(16) Bouster, C.; Vermande, P.; Vernon, J. J. Anal. Appl. Pyrolysis
1989, 15, 249.
(17) Atkinson, D. J.; Lehrle, R. S. J. Anal. Appl. Pyrolysis 1991, 19,
319.
(18) Gardener, P.; Lehrle, R. S. Eur. Polym. J. 1993, 29, 2/3, 425.
(19) Still, R. H.; Peters, O. A. J. Appl. Polym. Sci. 1993, 50, 989.
(20) Lehrle, R. S.; Atkinson, D.; Cook, S.; Gardner, P.; Groves, S.;
Hancox, R.; Lamb, G. Polym. Degrad. Stab. 1993, 42, 281.
(21) Page `s, P.; Carrasco, F. J. Appl. Polym. Sci. 1996, 61, 187.
(22) Hancox, R. N.; Lamb, G. D.; Lehrle, R. S. J. Anal. Appl.
Pyrolysis 1991, 19, 333.
(23) Solomon, P. R.; King, H. H. Fuel 1984, 63, 1302.
(24) Nip, M.; DeLeeuw, J. W.; Crelling, J. C. Energy Fuels 1992, 6,
125.
(25) Winans, R. E.; Meuzelaar, H. L. C. Advances in Coal Spectros-
copy; Plenum Press: New York, 1992.
(26) Greenwood, P. F.; Zhang, E.; Vastola, F. J.; Hatcher, P. G. Anal.
Chem. 1993, 65, 1937.
(27) Metcalf, G. S.; Windig, W.; Hill, G. R.; Meuzelaar, H. L. C. Int.
J. Coal Geol. 1987, 7, 245.
(28) Meuzelaar, H. L. C.; Harper, A. M.; Hill, G. R.; Given, P. R.
Fuel 1984, 63, 640.
984 Energy & Fuels 1999, 13, 984-991
10.1021/ef980254u CCC: $18.00 © 1999 American Chemical Society
Published on Web 07/01/1999