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無電鍍銅觸媒應用於一氧化碳氧化反應之研究

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CO Oxidation by Electroless Copper Catalyst

 : NSC88-2214-E011-006

 87/8/1 – 88/7/31

  

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Abstract (Keyword: Copper, Electroless catalyst, CO, Oxidation)

The purpose of this study is to investigate the effects of preparation method on the electroless copper catalyst for CO oxidation reaction. The impregnated copper catalysts are also prepared for comparison.

All prepared catalysts were characterized by XRD ƋBETƋTPRƋchemisorption and SEM.

The catalysts were further tested by CO oxidation reaction. Experimental results show that the catalysts prepared by the electroless method has better activities than those prepared by the impregnation method, and the electroless copper catalysts

prepared by EDTA chelating agent were better than those by TEA chelating agent.

Furthermore, the calcined electroless copper catalyst (at 500C) presents highest activities among all the catalysts.

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1. Barbier, J. Dumas, J.M. Geron, C. and Kribii, A., Appl. Catal., 47, L9 (1989).

2. Bond G.C Namijo S.N and Wakeman J.S, J. Mol.Catal, 64, 305 (1991).

3. Chang, H.F. and Yung, C.F., IECR., 36, 2080 (1997)ƌ

4. Fabio, B.Noronha and Martin Schmal, Appl.. Catal., 78, 125 (1991).

5. Huang, T.J and Yu, T.C, Appl. Catal., 71, 275 (1991).

6. Laine, J. and Severino, F., J. Catal., 129, 297 (1991).

7. Noronha, Fabio, Schmal and Martin, Appl. Catal., 78, 125 (1991).

8. Rossi, S.D., Ferraris, G. and Mancini, R., Appl. Catal., 38, 359 (1988).

BET 

 BET 

 (m 2 /g-cat)



(Å)

(4)

4 γ-Al 2 O 3 159.9 54.7 Cu 15%-Pd 0.12%

FE-t-f 116.7 60.7 FE-e-f 146.4 62.0 IE-t-f 112.5 66.7 IE-e-f 127.7 69.7 FE-t-c 114.1 64.6 FE-e-c 122.6 66.7 IE-t-c 108.4 70.4 IE-e-c 117.7 71.8

IWI 95.6 74.9

FE-e-c (Pd 0.12

%)

Cu 20 % 112.6 70.3 Cu 15 % 122.6 66.7 Cu 10 % 128.9 63.5 Cu 5 % 147.3 61.9 Cu 15%-Pd

0.012%

FE-t-c 116.8 64.0 FE-e-c 126.2 66.2

IWI 109.6 70.3

 



 

(m 2 /g)



(%)



(Å) FE-t series (Cu 15%)

Pd 0.24% 148.6 22.0 45.5 Pd 0.12% 143.7 21.2 47.1 Pd 0.012% 94.7 14.5 75.8

FE-e series (Cu 15%)

Pd 0.24% 274.6 40.6 24.6 Pd 0.12% 253.4 37.5 26.7 Pd 0.012% 171.7 25.4 39.4

FE-e series (Pd 0.12%) Cu 20% 290.7 42.7 23.9 Cu 15% 253.4 37.5 26.7 Cu 10% 201.7 29.8 33.5 Cu 5% 145.6 22.5 46.3

IWI series (Cu 15%)

Pd 0.12% 35.6 5.3 190.2 Pd 0.012% 43.5 6.4 155.7

0 10 0 20 0 30 0 40 0

Tem peratur e ( oC )

H ydrogen C o m sumpt ion

Pd 0.012 % calcin P d 0.12 % calci n Pd 0.24 % calcin

α

β

α β

α

Fig. 1

0 1 00 20 0 3 0 0 4 00 50 0

Tem peratur e ( oC )

Hydrogen C o ms u m ption

Pd 0.0 12 % P d 0.12 %

γ

γ δ

δ

Fig. 2

0 1 00 2 00 30 0 40 0

Temp er atur e (0C )

Hydro gen Coms umpt ion

Cu 5 % Cu 10 % Cu 15 % Cu 20 %

α β

α β

α

Fig. 3

(5)

5

0 .00 0 .02 0.0 4 0.0 6 0 .08 0. 10 0.1 2

Pd load in g (w t %)

0 .0 0 .1 0 .2 0 .3 0 .4 0 .5 0 .6

CO convers ion

FE -t- c FE -e-c IE -t- c IE -e-c IWI

Fig. 4

5 10 15 2 0 2 5

Cu lo ading (%)

0. 0 0. 1 0. 2 0. 3 0. 4 0. 5 0. 6

CO convers ion

I WI F E- t-c F E- e- c I E- t-c

Fig. 5

350 40 0 450 50 0 550 60 0 6 50 70 0 7 50 80 0

Temperature ( oC)

0.0 0.2 0.4 0.6 0.8 1.0

CO conve rsi on

Fig. 6

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