23 2 Vol. 23, No JOURNAL OF MOLECULAR CATALYSIS(CH INA) Ap r ZnO. ZnO Pd /m 2ZnO ZnO Pd

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1 23 2 Vol. 23, No JOURNAL OF MOLECULAR CATALYSIS(CH INA) Ap r : (2009) ZnO Pd /m 2ZnO, 3, (, ) : F2127 ZnO (m2zno ),, Pd /m2zno, XRD FT2IR H 2 2TPR TEM BET., m2zno ( m 2 /g), ZnO, ( m 2 /g). Pd /ZnO, Pd /m2zno Pd m2zno, CO , Pd /m2zno CO 2 Pd /ZnO 38. 4% 44. 4% 30. 0%, h, Pd /m2zno 95%, 4. 9%. : ; ; Pd ; : TQ ; O : A,,.,. Cu [ 126 ] Pd [ 7 ]. Cu, CO Pt,. Pd [ 8 ]. ZnO B ronsted,, ZnO, Pd, ZnO,. Yan [ 9 ] Cambelli P Daniel M L [ 10, 11 ] ZnO (m 2ZnO ), F2127 m2 ZnO. m2zno Pd, FT2IR XRD BET H 2 2TPR m2zno Pd /m2zno, ZnO Pd ZnO (m2zno ) : 1. 10g Zn ( CH 3 COO) 2 2H 2 O g CO (NH 2 ) 2 100mL, 0. 12g F2127, 10 m in CH 3 COOH ph = 4 5, 2 h h., 3 5, 100, h. ZnO ( ZnO ) F2127,. Pd /m 2ZnO Pd /ZnO : Pd. m 2ZnO ZnO mol/l H 2 PdCl 6, mol/l NaCO 3 ph 9 10, 2 h,, 5,, h. Pd /m2zno Pd /ZnO, Pd 2% ( ). : ; : : ( ) ; ( GJJ08021) : ( ),,. 3, Tel: , E - mail: Luolaitao@163. com.

2 , 0. 1 g U, h (30 ml /m in)., ml /h g CH 3 OH H 2 O = 1 (mol ). ( GC102), TCD, Porapak Q H 2 O CH 3 OH CH 4 CO 2, 5 A H 2 CO.,, CO 2 P CO2 / ( P CO2 CO 2 CO P CO ), P CO2 P CO X (XRD ) B ruker2axs D8 Advnce, 40 kv, 40 ma, CuK, N i, 1 o / m in, Scherrer. M icromeritics ASAP 22020, 18 Pa 403 K 1. 6 h, N 2, BET BJH. ( TPR) M icromeritics Chem isorb ( g) He ( 50 ml /m in) 10 /m in 300,,, 5 Vol% H 2 /A r (50 ml /m in), 800,. ( TG) R igaku TAS2 100, ( 100 ml /m in) 10 /m in 600. ( TEM ) H2600, 200 V m 2ZnO Pd /m 2ZnO 1 m2zno N 2,, m 2ZnO 2.,,, m2 ZnO P /P 0 = 0. 45, m 2ZnO nm ( P /P 0 = ), 2 nm. P /P 0 = 0. 9,, [ 12 ]., m2zno nm, nm, > 50nm, F2127. m2 ZnO BET, m 2 /g cm 3 /g nm. Pd,,,. m 2ZnO BET ZnO (9. 0 m 2 /g), ( m 2 /g) [ 13 ]. Pd m2zno, ( m 2 /g), m2zno PdO x. 1 m2zno N 2 2 Fig. 1 N itrogen adsorp tion2desorp tion isotherm and the pore size distribution for m2zno m 2ZnO TEM 2., m2 ZnO < 10 nm,, m2zno 20 nm. 3, m2zno 2 = 1. 0, m2zno. 4 m2zno TG.,. 200 (1. 59% ), F2127 ( 22. 5% ), (2. 38% ),

3 2 : ZnO Pd /m2zno m2zno TEM Fig. 2 TEM image of m2zno 4 m2zno TG Fig. 4 TG curve of m2zno ZnO (100) ( 002 ) ( 101 ) ( 102 ) ( 110 ) ( 103 ) (200) (112) (201), m2zno ZnO XRD Pd /m 2ZnO Pd /ZnO XRD ( ), Pd m2zno ZnO. Pd /m2 ZnO Pd /ZnO XRD Pd PdO x, PdO x. Sherrer D = K / B 1 /2 cos, Pd /m 2ZnO Pd /ZnO nm nm (002 ),, Pd /m2 ZnO. 3 m2zno XRD Fig. 3 Small XRD pattern of m2zno 27. 8%., > 400 ( < 1% ), 400 F2127., 500, 450, F2127.,,, m2zno Pd /m2zno Pd /ZnO XRD, XRD 2 = Pd /m2zno ( a) Pd /ZnO ( b) XRD Fig. 5 XRD patterns of Pd /m2zno (a) and Pd /ZnO (b) catalysts Pd /m2zno Pd /ZnO TPR., Pd /ZnO ( ), Pd /m 2ZnO (48 )., ZnO ( 62c), PdO x. Pd / ZnO,

4 Pd /m2zno,, Pd /m2zno PdO x H 2 Pd [ 14 ] ;, m 2ZnO Pd PdZn x, Pd, PdZn x [ 15 ]., PdO x m2zno m2zno, Pd m2zno Pd ZnO [ 16 ]. Pd /ZnO ZnO PdO x [ 17, 18 ], Pd /m2zno, PdO x m2zno, ZnO. Pd. 7, CO 2, Pd /m2zno CO % 98. 5%, Pd /ZnO 76. 7% 68. 2%., CH 3 OH + H 2 O CO 2 + 3H 2 CH 3 OH CO + 2H 2, CO 2, S CO2 + S CO = 1, CO 2 CO, CO, Pt. 7 Pd /m2zno ( a, b) Pd /ZnO ( c, d) CO 2 Fig. 7 Conversion and CO 2 selectivity for methanol steam 6 Pd / m2zno ( a) Pd / ZnO ( b) m2zno ( c) TPR Fig. 6 TPR p rofiles of Pd / m2zno ( a), Pd / ZnO ( b) and m2zno ( c) 2. 4 CO 2,,, Pd CO 2, , Pd /m2zno Pd /ZnO, Pd /m2 ZnO, 170 Pd /m2zno, 99. 9%, Pd /ZnO 90. 1%, 190 Pd /ZnO, %, %, Pd /m2zno,. ZnO, ZnO Pd, m2 ZnO ZnO, Pd, Pd /m2zno reform ing over Pd /m2zno ( a, b) and Pd / ZnO ( c, d) catalysts 8, Pd /m2zno mol h 21 g 21 cat, Pd /ZnO mol h 21 g 21 cat, Pd /m2zno Pd / ZnO., m2zno Pd /m 2ZnO CO 2. Pd /m2zno %,, h, Pd /m2zno, 95%, 4. 9%, Pd /ZnO 14. 0%, Pd /m2zno CO 2, Pd /m2 ZnO. 3 N 2 TEM XRD, F2127

5 2 : ZnO Pd /m2zno Pd /m2zno ( a) Pd /ZnO ( b) Fig. 8 Hydrogen yield over Pd /m2zno ( a) and Pd / ZnO ( b) catalysts 9 Pd /m2zno (a) Pd /ZnO (b) Fig. 9 Effection of reaction time on Pd /m2zno ( a) and Pd / ZnO ( b) catalysts ZnO, BET,. Pd /ZnO, Pd /m2zno,, CO 2, 170 CO % mol h 21 g 21 cat 94. 4%. : [ 1 ] Agrell. J, Hasselbo. K, Jansson. K, Sven. G, et al. A ppl. Catal. A [ J ], 2001, 211 (2) : [ 2 ] W ang Zhi2fei ( ), Xi J ing2yu ( ), W ang W ei2p ing( ), et al. J. M ol. Catal. (China) ( ) [ J ], 2001, 15 (5) : [ 3 ] W ang Zhi2fei ( ), W ang W ei2p ing ( ), Lv Gong2xuan ( ). J. M ol. Catal. (China) ( ) [ J ], 2003, 17 (1) : [ 4 ] Mao L i2p ing ( ), Lu Gong2xuan ( ). J. M ol. Catal. (China) ( ) [ J ], 2007, 21 ( 4) : [ 5 ] Mao L i2p ing( ), Hu Xun ( ), Lu Gong2xu2 an ( ). J. M ol. Catal. ( China) ( ) [ J ], 2007, 21 (5) : [ 6 ] Ma Chong2hua ( ), Hu Xun ( ), Lu Gong2 xuan ( ). J. M ol. Catal. (China) ( ) [ J ], 2008, 22 (4) : [ 7 ] Agrell. J, Germani. G, Jaras. S. G, et al. A ppl. Catal. A [ J ], 2003, 242 (2) : [ 8 ] W ang Yan2hua ( ), Xu Heng2yong ( ), Zhang J ing2chang( ). J Chem ical Industry & En2 gineering ( China) ( ) [ J ], 2006, 57 ( 4 ) : [ 9 ] Yan H X, L iang L, Yan L, et al. J. N anotecnology, 2005, 16 (6) : [ 10 ] Cambelli P, Gorbo P, M igliardini F. J. Catal. Today, 2000, 59 (324) : [ 11 ] Daniel M L, Kevin M R, M ichael A M. J. M ater. Chem. 2002, 12 (23) : [ 12 ] W ang Ying( ), W ang Zheng( ), Ma J ian2 xin ( ), et al. Chem J Chinese U (China) ( ) [ J ], 2002, 23 (6) : [ 13 ] Yan C M, Chen Z, Zhao X P. J. Solid. S tate. Comm u2 nications, 2006, 140 ( 1) : [ 14 ] Enrique R C, Josefa M R, Lourdes D. J. A ppl. Catal. A, 2004, 260 (4) : 9 18 [ 15 ] W ang Yan2hua ( ), Zhang J ing2chang ( ), Xu Heng2yong( ), et al. Chin J Catal ( China) ( ) [ J ], 2007, 28 (3) : [ 16 ] Agrell J, Boutonnet M, Fierro J L G. J. A ppl. Catal. A: General, 2003, 253 (1) : [ 17 ] Shimokawabe M, A sakawa H, Takezawa N. J. A ppl. Catal, 1990, 59 (11) : [ 18 ] Gunter M M, Ressler T, Jentoftre, et al. J. Catal, 2001, 203 (1) :

6 The Synthesis of M esoporous ZnO by Hydrothermal and Performance of Pd /m2zno Catalyst for Steam Reform ing of M ethanol X IONG Guang2wei, LUO Lai2tao 3, L I Chang2quan ( Institu te of Applied Chem istry, N anchang U niversity, N anchang, , China) Abstract: M esoporous ZnO (m 2ZnO ) had been synthesized using hydrotherm al method and triblock copolym er Plu2 ronic F2127 ( F2127) as temp late reagent. The catalytic activities of Pd /m 2ZnO catalyst were studied w ith steam re2 form ing of methanol as p robe reaction. These samp les were characterized by m eans of BET, FT2IR, XRD, TEM and H 2 2TPR methods. The results showed that the p repared m2zno exhibited much higher BET surface area (124. 7m 2 /g) than those of nonmesoporous ZnO and literature value ( m 2 /g). A s compared with Pd /ZnO catalyst, Pd /m 2ZnO catalyst has higher dispersion and stronger interaction between Pd and ZnO, thus Pd /m 2ZnO catalyst exhibited much higher catalytic activity, H 2 yield, CO 2 selectivity and stability for steam reform ing of metha2 nol. The activity, H 2 yield and CO 2 selectivity of Pd /m2zno catalyst enhanced 38. 4% 44. 4% and 30. 0% than that of Pd /ZnO catalyst at 250, respectively. After continuum reaction 100 h, the activity of Pd /m2zno catalyst was 95% and only droped 4. 9%. Key words: M esoporous zinc oxide; Steam reform ing of methanol; Pd2based catalyst; Temp late reagent

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