Nickel-catalyzed conversion of activated carbon extrudates into high surface area silicon carbide by reactive chemical vapour deposition

被引:21
作者
Moene, R [1 ]
Tazelaar, FW [1 ]
Makkee, M [1 ]
Moulijn, JA [1 ]
机构
[1] DELFT UNIV TECHNOL,DEPT CHEM ENGN,SECT IND CATALYSIS,NL-2628 BL DELFT,NETHERLANDS
关键词
D O I
10.1006/jcat.1997.1782
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
A novel method for the synthesis of high surface area silicon carbide extrudates has been developed which consists of applying nickel onto activated carbon extrudates followed by reaction with silicon tetrachloride and hydrogen, Utilization of nickel is shown to be essential in order to obtain a considerable conversion, Selective SiC formation has been obtained at 1380 K and 10 kPa. Thus, methane is formed at the interior of the carbon via gasification: C(s) + 2H(2)(g) reversible arrow CH4(g), which subsequently reacts with silicon tetrachloride to silicon carbide: SiCl4(g) + CH4(g) reversible arrow SiC(s) + 4HCl(g). The total carbon conversion ranges from 20 to 55% for nickel contents of 2 and 8 wt%, respectively. Si-codeposition will occur when the gasification reaction diminishes in time, due to deactivation of the nickel gasification sites, Extensive whisker formation of SiC is encountered owing to the operative vapour-liquid-solid mechanism. Mass transport calculations show that methane is formed throughout the extrudate, whereas the front of SiC formation moves from the outside to the internal part due to diffusion limitations of SiCl4 and nickel deactivation. The residual carbon can be removed after conversion by oxidation, resulting in high surface area SiC extrudates, The BET-surface areas after conversion vary from 359 to 154 m(2)/g; BET-surface areas after removal of the residual carbon are in the range of 57 to 32 m(2)/g. Pore size distributions of the SiC supports show that the pore volume is evenly distributed over the meso- and macro-pore region (diameter: 2 to 100 nm) which allows the following areas of application: (1) reactions at high temperatures and (2) liquid-phase reactions at demanding pH conditions. (C) 1997 Academic Press.
引用
收藏
页码:311 / 324
页数:14
相关论文
共 36 条
[1]  
[Anonymous], PERRYS CHEM ENG HDB
[2]   GROWTH OF SIC WHISKERS IN SYSTEM SIO2-C-H2 NUCLEATED BY IRON [J].
BOOTSMA, GA ;
VERSPUI, G ;
KNIPPENB.WF .
JOURNAL OF CRYSTAL GROWTH, 1971, 11 (03) :297-&
[3]  
BOUBLIK T, 1973, VAPOUR PRESSURES PUR, P32
[4]   Adsorption of gases in multimolecular layers [J].
Brunauer, S ;
Emmett, PH ;
Teller, E .
JOURNAL OF THE AMERICAN CHEMICAL SOCIETY, 1938, 60 :309-319
[5]  
Byung Jin Choi, 1992, Journal of the European Ceramic Society, V9, P357, DOI 10.1016/0955-2219(92)90094-T
[6]   STRUCTURE OF CHEMICAL VAPOR-DEPOSITED SILICON-CARBIDE [J].
CHIN, J ;
GANTZEL, PK ;
HUDSON, RG .
THIN SOLID FILMS, 1977, 40 (JAN) :57-72
[7]   SYNTHETIC ROUTES TO HIGH SURFACE-AREA NONOXIDE MATERIALS [J].
CHORLEY, RW ;
LEDNOR, PW .
ADVANCED MATERIALS, 1991, 3 (10) :474-485
[8]   STUDIES ON PORE SYSTEMS IN CATALYSTS .6. UNIVERSAL T CURVE [J].
DEBOER, JH ;
LINSEN, BG ;
OSINGA, TJ .
JOURNAL OF CATALYSIS, 1965, 4 (06) :643-&
[9]   CARBON-SUPPORTED SULFIDE CATALYSTS [J].
DUCHET, JC ;
VANOERS, EM ;
DEBEER, VHJ ;
PRINS, R .
JOURNAL OF CATALYSIS, 1983, 80 (02) :386-402
[10]  
Givargizov E.I., 1978, CURRENT TOPICS MATER, V1, P79