In order to prove the scalability of the preparation method,
magnetic carbons were also synthesized on a larger scale in a pilot
plant-size rotary kiln (see ESI{). For this preparation, 125 g
3
21
of activated carbon (P-43 171, Adsor-Tech, 0.598 cm
2
g ,
21
1
3 3
207 m g ) was impregnated with 59.8 mL of 2 M Fe(NO )
solution and fed into the continuously operated rotary kiln. The
impregnated 0.3–0.5 mm activated carbon beads are successively
transferred through a drying zone, a decomposition zone, a
calcination zone and a cooling zone. In order to prevent working
Fig. 5 Interaction of the magnetic carbon with a permanent magnet.
with larger amounts of benzene, a nitrogen–toluene stream (N
2
21
flow 50 L h ) was passed at 700 uC in concurrent flow over the
carbon material in the kiln. In this way, a magnetic carbon
containing about 5 wt% of iron was obtained. The toluene acts in
the same way as benzene. Using this pilot scale kiln, a productivity
It should be noted that the iron–carbon composites also
contain a small fraction of iron carbide as evidenced by XPS
spectroscopy. This minor by-phase is probably formed on the
surface of the iron particles during the calcination under protective
atmosphere.
21
of about 25 g h of magnetic carbon could be achieved. However,
if working with higher loading as in the experiment described, the
fraction of ferromagnetic domains increases.
Fig. 5 shows the magnetic carbon sedimented in a solution (left)
and attracted by a permanent magnet. After removing the
permanent magnet, the carbon is easily redispersed in the solution
because of the superparamagnetic properties of the iron particles.
Their size in the range of a few nanometres prevents ferromagnet-
ism because the size of the magnetic domains (,10 nm) falls below
its critical value. At this size, the thermal energy at room
temperature is sufficient to change the direction of magnetization
of the entire crystallite at room temperature. In presence of a field,
the magnetic momentum of the complete crystallite is aligned with
the external field. After removal of the external magnetic field, the
alignment of the magnetic momentum is lost, allowing redispersion
of the particles. It should be noted that a small residual
ferromagnetism at room temperature was observed which can be
attributed to the small fraction of larger iron particles in the
material. This, however, did not negatively affect the redispersi-
bility of the materials.
The materials obtained via the pathway described in this
manuscript are essentially superparamagnetic, have high surface
areas and high porosities, they are bio-compatible, and stable
under alkaline as well as under acidic conditions. Last but not
least, upscaling of the preparation process is easily possible. This
makes these magnetic carbons very promising candidates for larger
scale applications in catalysis (e.g. magnetically separable catalyst
supports) and/or separation technology (e.g. magnetically separ-
able adsorber).
Notes and references
1
T. L. Makarova, Semiconductors, 2004, 38, 615–638; H. Pardo, R. Faccio,
F. M. Ara u´ jo-Moreira, O. F. de Lima and A. W. Mombr u´ , Carbon,
2006, 44, 565–569; P. Esquinazi, K. H. Han, R. H o¨ hne, D. Spemann,
A. Setzer and T. Butz, Phase Transitions, 2005, 78, 155–168.
L. C. A. Oliveira, R. V. R. A. Rios, J. D. Fabris, V. Garg, K. Sapag and
R. M. Lago, Carbon, 2002, 40, 2177–2183; Z. Sun, Z. Liu, Y. Wang,
B. Han, J. Du and J. Zhang, J. Mater. Chem., 2005, 15, 4497–4501;
C. Gao, W. Li, H. Morimoto, Y. Nagaoka and T. Maekawa, J. Phys.
Chem. B, 2006, 110, 7213–7220.
2
The preparation of magnetic carbon as described above thus
results in a material with excellent magnetic properties for various
applications. The particles only aggregate in a magnetic field and
redispersion occurs if the external magnetic field is switched off. In
contrast to materials from other reports where the magnetic
properties are due to metal oxide particles, here metallic iron
nanoparticles are causing the magnetism. Also in contrast to most
reports, a protective carbon shell prevents dissolution and/or
leaching of the metal nanoparticles.
3
4
A. B. Fuertes and P. Tartaj, Chem. Mater., 2006, 18, 1675–1679.
A.-H. Lu, W. Schmidt, N. Matoussevitch, H. B o¨ nnemann, B. Spliethoff,
B. Tesche, E. Bill, W. Kiefer and F. Sch u¨ th, Angew. Chem., Int. Ed., 2004,
43, 4303–4306.
5
6
A.-H. Lu, W.-C. Li, N. Matoussevitch, B. Spliethoff, H. Boennemann
and F. Sch u¨ th, Chem. Commun., 2005, 98–99.
J. Jang and H. Yoon, Small, 2005, 1, 1195–1199; J. Jang and H. Yoon,
Adv. Mater., 2003, 15, 2088–2091.
This journal is ß The Royal Society of Chemistry 2006
Chem. Commun., 2006, 3987–3989 | 3989