Preparation of porous carbons from phenol-formaldehyde resins with chemical and physical activation

被引:149
作者
Teng, HS [1 ]
Wang, SC [1 ]
机构
[1] Natl Cheng Kung Univ, Dept Chem Engn, Tainan 70101, Taiwan
关键词
activated carbon; activation; chemical treatment; surface areas; porosity;
D O I
10.1016/S0008-6223(99)00160-8
中图分类号
O64 [物理化学(理论化学)、化学物理学];
学科分类号
070304 ; 081704 ;
摘要
Porous carbons with high porosities were prepared from phenol-formaldehyde resins using chemical and physical activation methods. The resin precursor employed was synthesized with an initial formaldehyde-to-phenol ratio of 1.33 by mole. The chemical activation process consisted of KOH impregnation followed by carbonization in nitrogen at 500-900 degrees C for 0-3 h, whereas the physical activation was performed by carbonizing the resins at 900 degrees C followed by gasifying the char in CO2 to different degrees of burn-off. Both activation methods can produce carbons with surface areas and pore volumes greater than 2000 m(2)/g and 1.0 cm(3)/g, respectively. The influence of different parameters during chemical activation. such as carbonization temperature and time. KOH/resin ratio and heating rate, on the carbon yield and the surface characteristics was explored. and the optimum preparation conditions were determined. With physical activation the resulting carbons are mainly microporous and their porosity is an increasing function of the degree of burn-off. At similar porosity levels the carbon yield during physical activation was found to be lower than that with chemical activation. An SEM study showed that carbons produced from CO2 activation have a more compact surface than those produced from KOH activation. (C) 2000 Elsevier Science Ltd. All rights reserved.
引用
收藏
页码:817 / 824
页数:8
相关论文
共 26 条
[1]   The preparation of active carbons from coal by chemical and physical activation [J].
Ahmadpour, A ;
Do, DD .
CARBON, 1996, 34 (04) :471-479
[2]   The preparation of activated carbon from macadamia nutshell by chemical activation [J].
Ahmadpour, A ;
Do, DD .
CARBON, 1997, 35 (12) :1723-1732
[3]  
GREENBANK M, 1993, WATER TECHNOLOGY, V16, P56
[4]   CHEMICAL ACTIVATION OF ELUTRILITHE PRODUCING CARBON-ALUMINOSILICATE COMPOSITE ADSORBENT [J].
HU, ZH ;
VANSANT, EF .
CARBON, 1995, 33 (09) :1293-1300
[5]   CATALYTIC EFFECTS OF ZINC-CHLORIDE IN THE PYROLYSIS OF SPANISH HIGH SULFUR COALS [J].
IBARRA, JV ;
MOLINER, R ;
PALACIOS, JM .
FUEL, 1991, 70 (06) :727-732
[6]   Activated carbons from Spanish coals .2. Chemical activation [J].
IllanGomez, MJ ;
GarciaGarcia, A ;
deLecea, CSM ;
LinaresSolano, A .
ENERGY & FUELS, 1996, 10 (05) :1108-1114
[7]   ADSORBENT CARBON SYNTHESIS FROM COALS BY PHOSPHORIC-ACID ACTIVATION [J].
JAGTOYEN, M ;
THWAITES, M ;
STENCEL, J ;
MCENANEY, B ;
DERBYSHIRE, F .
CARBON, 1992, 30 (07) :1089-1096
[8]   EFFECT OF THE PREPARATION METHOD ON THE PORE-SIZE DISTRIBUTION OF ACTIVATED CARBON FROM COCONUT SHELL [J].
LAINE, J ;
YUNES, S .
CARBON, 1992, 30 (04) :601-604
[9]   Effect of calcium catalyst loading procedure on the porous structure of active carbon from plum stones modified in the steam gasification process [J].
Leboda, R ;
Skubiszewska-Zieba, J ;
Grzegorczyk, W .
CARBON, 1998, 36 (04) :417-425
[10]   All-solid-state electric double-layer capacitor with isotropic high-density graphite electrode and polyethylene oxide/LiClO4 polymer electrolyte [J].
Liu, XJ ;
Osaka, T .
JOURNAL OF THE ELECTROCHEMICAL SOCIETY, 1996, 143 (12) :3982-3986