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Mesostructured Hollow Spheres of Graphitic N-Doped

Carbon Nanocast from Spherical Mesoporous Silica

J. Phys. Chem. B 2004 , 108, 19293- 19298

Introduction

 Porous carbon - high chemical stability, large surface area and tailorable structure property.

 High SA and meso str. – more dispersion of metal ions on their surface

 it is difficult to achieve highly dispersed metal catalyst due to the inert surface of the carbon materials

 Generation functional groups on the carbon surface – by harsh conditions

 Functional groups by in situ generation – N-carbon source

 Varying carbonization temperature – change in N/C ratio

 by adopting CVD method N- OMC were prepared

(SBA-15 hard template, acetonitrile carbon source)

SBA-15

4g P123 + 0.5 g CTAB + 25 ml EtOH + 30 ml H

2

O + 60 ml HCl (2M)

Stirred at RT

10 g TEOS

Stirred at RT for 1 h

Autoclave at 80 0 C for 6 h

Autoclave at 110 0 C for 12 h

Washed EtOH and dried Cal at 550 0 C

SBA-15

NOMCs (CNx)

0.5 g SBA-15

N

2

& sat. with acetonitrile

Carbonized at 900-1000 0 C for 3 h under N

2 atm.

Washed with 20 % HF at RT and with EtOH

NOMCs

N

2sorption isotherm & SEM of SBA-15

BET

PD = 6.0 nm

P vol

SA

=1087 m 2 /g

= 1.13 cc/g

SEM & TEM images OMC

(f)

SEM images of OMCs compaction at 1.0 Gpa for 1 h.

1000 0 C 1000 0 C

900 0 C 900 0 C

XRD of OMC

2θ = 2.11 ° - d

200 basal d

100

= 8.4 nm & a

0

= 9.7 nm

2θ = 26.2 ° - d

002

= 0.339 nm

N

2sorption isotherm & TEM of OMC

BET

PD = 4.7 nm

P vol

SA

=779 m 2 /g

= 0.66 cc/g

Mechanism for the Formation of Mesoporous Carbon Hollow Spheres

Textural properties

XPS of OMC

N1s C1s

N1s

400.8eV – quaternary N atoms

398.9 eV – pyridine - like N atoms

C1s

284.6 eV – sp 2 gC species

Raman spectra of OMC

Conclusion hollow spheres of structurally wellordered – NOMC may be nanocast using SBA-15 template via a CVD route

The CVD temperature is an important consideration and should be higher than 900 ° C and preferably 1000 ° C for successful formation of carbon hollow spheres.

The use of acetonitrile as a carbon precursor results in N-doped (CNx) materials with a nitrogen content of ca. 6.5 wt %.

The CNx hollow spheres exhibit a high level of graphitization especially for materials prepared at a CVD temperature of 1000 ° C

Preparation of

Pt/CMK-3

Anode Catalyst for Methanol

Fuel Cells Using Paraformaldehyde as Reducing Agent

Chinese J Catal, 2007, 28(1): 17-21

Introduction

In recent years, DMFC have attracted significant attention because of their high energy transfer efficiency and low pollution causing potential.

The disadvantages of the existing catalyst low catalytic activity

The highest electro catalytic activity of two component system is Ru-Pt/C

In this study Pt/CMK-3 anode catalyst for DMFC was prepared by a novel liquid reduction method using paraformaldehyde has reducing agent.

SBA-15

4g P123 + 22 ml H

2

O +38 ml HCl (2M)

Stirred at 35 0 C

7 g TEOS

Stirred at 35 0 C for

24 h

Aged at 100 0 C for 48 h

Washed EtOH and dried Cal at 550 0 C

SBA-15

Msoporus Carbon

1 g SBA-15 + 1.25 g sucrose + 0.14 g H

2

SO

4

+ 5 g H

2

O

Dried at 100 0 C for 6 h and 160 0 C for 6 h

Black powder

0.8 g sucrose + 0.09 g H

2

SO

4

+ 5 g H

2

O

Dried at 100 0 C for 6 h and 160 0 C for 6 h

Carbonized at 900 0 C for 6 h under N

2 atm.

Washed with 5% HF at RT and with EtOH

CMK-3

Preparation of Pt/CMK-3

60 mg CMK-3 + 20 ml H

2

O +0.039 M H

2

PtCl

6

Ultrasonication 30 min

Heated at 343 K / N

2

10 ml Na

2

CO

3

+ Paraformaldehyde

Stirred 2.5 h

Filt. Washed & dried

Pt/CMK-3, Pt/C-M

XRD patterns of the Pt/CMK-3, Pt/C-M and Pt/XC-72

Pt/C-M

Pt/XC-72

Pt/CMK-3

Average diameter and relative crystallinity of Pt particles

TEM images of SBA-15 and CMK-3

TEM images of Pt/CMK-3 and Pt/XC-72

Particle size distribution

Pt/CMK-3 Pt/XC-72

The average size of the Pt particles in the Pt/CMK-3 catalyst is 2.8 nm

The average particle size Pt/XC-72 is 3.5 nm

Particles aggregation is observed in Pt/XC-72 more then 10 nm

Electrocatalytic activity of the catalysts for methanol oxidation

8 mg Pt/CMK-3 + 0.6 ml EtOH +2.4 ml H

2

0.2 ml Nafion (5 %)

O +

Sonication 30 min

4 µl slurry on GC electrode

Dried at 308 K

0.5 M H

2

SO

4

+ 0.5 M MeOH

N

2 bubbled to remove O

2

50 mV/s at 309 K

Cyclic voltammograms of Pt/CMK-3, Pt/C-M and Pt/XC-72

1.Pt/C-M

2. Pt/XC-72

3.Pt/CMK-3

Positive scan, the potential of oxidation peaks of CH

0.64 V

3

OH for all 3 catalyst at

Negative scan the potential located at 0.43 V

Methanol is dissociatively adsorbed on the Pt surface

Increasing potential platinum oxides are formed and reaction rate is enhanced

Current density is increased

The electrocatalytic activity is related to the size of Pt particles. Smaller the particle size the activity is relatively higher

Catalyst

Pt/CMK-3

Pt/XC-72

Pt/C-M

Peak current

(mA cm -2 )

22.06

19.72

14.9

Chronoamperometric Curves

1.Pt/C-M

2. Pt/XC-72

3.Pt/CMK-3

Pt/CMK-3 high catalytic activity

The relative crystalinity and average Pt particle size in

Pt/CMK-3 are lower and smaller.

Catalyst preparation and reduction rate is important factor for the structure of metal deposition.

Creation of metal atoms from chemical reaction

Formation of crystal cells from atoms

Aggregation of cells to from particles

Coalescence of particles

The primary role of carbon support is to disperse metal nanoparticles and provide electrical connection among them.

Conclusion

 The nucleation and growth of Pt particles on CMK-3 are influenced by the experimental conditions such as surface states of carbon, temperature, time, and concentration of reactants and products.

 Small and uniformly distributed Pt particles can be obtained by controlling the experimental conditions

 This preparation method is very simple and the electro catalytic activity of the prepared Pt/CMK-3 catalyst for the methanol oxidation is high, this method is promising for practical applications.

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