Experimental Evaluation of Indirect Heating Tubular Reactors for Solar Methane Pyrolysis

被引:20
作者
Rodat, Sylvain [1 ]
Abanades, Stephane [1 ]
Flamant, Gilles [1 ]
机构
[1] CNRS, PROMES, F-75700 Paris, France
关键词
hydrogen production; concentrated solar energy; methane pyrolysis; solar reactor; plasma reactor; natural gas; carbon black; NATURAL-GAS PYROLYSIS; AEROSOL FLOW REACTOR; THERMAL-DECOMPOSITION; HYDROGEN-PRODUCTION; CARBON-BLACK; DISSOCIATION; PLASMA;
D O I
10.2202/1542-6580.2084
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Solar thermal pyrolysis of natural gas is studied for the co-production of hydrogen, a promising energy carrier, and Carbon Black, a high-value nano-material, with the bonus of zero CO2 emissions. A 10 kW multi-tubular solar reactor (SR10) based on the indirect heating concept was designed, constructed and tested. It is composed of an insulated cubic cavity receiver (20 cm side) that absorbs concentrated solar irradiation through a quartz window by a 9 cm-diameter aperture. The solar concentrating system is the 1 MW solar furnace of CNRS-PROMES laboratory. An argon-methane mixture flows inside four graphite tubular reaction zones each composed of two concentric tubes that are settled vertically inside the cavity. Experimental runs mainly showed the key influence of the residence time and temperature on the reaction extent. Since SR10 design presented a weak recovery of carbon black in the filter, a single tube configuration was tested with an external plasma heating source. Complete methane conversion and hydrogen yield beyond 80% were achieved at 2073K. Hydrogen and carbon mass balances showed that C(2)H(2) intermediates affect drastically the carbon black production yield: about half of the initial carbon content in the CH(4) was found as C(2)H(2) in the outlet gas. Nevertheless, the carbon black recovery in the filtering device was improved with this new configuration. Data are extrapolated to predict the possible hydrogen and carbon production for a future 50 kW solar reactor. The expected production was estimated to be about 2.47 Nm(3)/h H(2) and 386 g/h carbon black for 1.47 Nm(3)/h of CH(4) injected.
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页数:21
相关论文
共 27 条
[1]   Hydrogen production from solar thermal dissociation of methane in a high-temperature fluid-wall chemical reactor [J].
Abanades, Stephane ;
Flamant, Gilles .
CHEMICAL ENGINEERING AND PROCESSING-PROCESS INTENSIFICATION, 2008, 47 (03) :490-498
[2]   Natural gas pyrolysis in double-walled reactor tubes using thermal plasma or concentrated solar radiation as external heating source [J].
Abanades, Stephane ;
Tescari, Stefania ;
Rodat, Sylvain ;
Flamant, Gilles .
JOURNAL OF NATURAL GAS CHEMISTRY, 2009, 18 (01) :1-8
[3]  
BACK MH, 1983, PYROLYSIS THEORY IND, P1
[4]   THERMAL-DECOMPOSITION OF PURE METHANE AT 1263-K - EXPERIMENTS AND MECHANISTIC MODELING [J].
BILLAUD, F ;
GUERET, C ;
WEILL, J .
THERMOCHIMICA ACTA, 1992, 211 :303-322
[5]   Nonoxidative activation of methane [J].
Choudhary, TV ;
Aksoylu, E ;
Goodman, DW .
CATALYSIS REVIEWS-SCIENCE AND ENGINEERING, 2003, 45 (01) :151-203
[6]   Rapid solar-thermal dissociation of natural gas in an aerosol flow reactor [J].
Dahl, JK ;
Buechler, KJ ;
Finley, R ;
Stanislaus, T ;
Weimer, AW ;
Lewandowski, A ;
Bingham, C ;
Smeets, A ;
Schneider, A .
ENERGY, 2004, 29 (5-6) :715-725
[7]   Solar-thermal dissociation of methane in a fluid-wall aerosol flow reactor [J].
Dahl, JK ;
Buechler, KJ ;
Weimer, AW ;
Lewandowski, A ;
Bingham, C .
INTERNATIONAL JOURNAL OF HYDROGEN ENERGY, 2004, 29 (07) :725-736
[8]  
Donnet J.B., 1993, CARBON BLACK, V2nd
[9]   Plasma pyrolysis of methane to hydrogen and carbon black [J].
Fincke, JR ;
Anderson, RP ;
Hyde, TA ;
Detering, BA .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2002, 41 (06) :1425-1435
[10]   Comparison between new carbon nanostructures produced by plasma with industrial carbon black grades [J].
Fulcheri, L ;
Schwob, Y ;
Flamant, G .
JOURNAL DE PHYSIQUE III, 1997, 7 (03) :491-503