Methane thermal decomposition in regenerative heat exchanger reactor: Experimental and modeling study

被引:40
作者
Keipi, Tiina [1 ]
Li, Tian [2 ]
Lovas, Terese [2 ]
Tolvanen, Henrik [1 ]
Konttinen, Jukka [1 ]
机构
[1] Tampere Univ Technol, Lab Chem & Bioengn, POB 541, FIN-33101 Tampere, Finland
[2] Norwegian Univ Sci & Technol, Dept Energy & Proc Engn, Kolbjorn Hejes Vei 1B, NO-7491 Trondheim, Norway
关键词
CCS; Hydrogen production; Kinetics; Methane cracking; Methane decomposition; AEROSOL FLOW REACTOR; HYDROGEN-PRODUCTION; NATURAL-GAS; SOOT FORMATION; SOLAR REACTOR; CARBON; CRACKING; PYROLYSIS; DISSOCIATION; CATALYSTS;
D O I
10.1016/j.energy.2017.06.176
中图分类号
O414.1 [热力学];
学科分类号
摘要
In this work, thermal decomposition of methane (TDM) was experimentally studied at nominal gas temperatures of 1070 K-1450 K in a non-catalytic laboratory test reactor. The purpose was to use a simple kinetic mechanism to describe the TDM reaction, which could be applied in industrial reactor design. The experimental data was utilized to optimize global kinetic parameters describing the TDM reaction in the test reactor. For comparison, a 37-step reaction mechanism for TDM was adopted from the literature. When analyzing experimental datasets from the literature, the optimized global kinetics provided better agreement with the experimental data than the 37-step mechanism when the reactor temperature profiles were defined in detail. Since the 37-step mechanism was not able to predict the solid carbon formation well enough, the mechanism was slightly adjusted according to a reaction flow and sensitivity analysis. Additionally, it was suggested that the 37-step mechanism can be improved by optimizing the reaction mechanism by using a detailed experimental data of hydrocarbon formation in TDM achieved in an environment where the temperature profiles are fully defined. (C) 2017 Elsevier Ltd. All rights reserved.
引用
收藏
页码:823 / 832
页数:10
相关论文
共 40 条
[1]   Technological challenges for industrial development of hydrogen production based on methane cracking [J].
Abanades, A. ;
Rubbia, C. ;
Salmieri, D. .
ENERGY, 2012, 46 (01) :359-363
[2]   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
[3]   Kinetic investigation of carbon-catalyzed methane decomposition in a thermogravimetric solar reactor [J].
Abanades, Stephane ;
Kimura, Hiroyuki ;
Otsuka, Hiroyuki .
INTERNATIONAL JOURNAL OF HYDROGEN ENERGY, 2015, 40 (34) :10744-10755
[4]   Detailed kinetic modeling of soot formation in shock tube pyrolysis and oxidation of toluene and n-heptane [J].
Agafonov, G. L. ;
Naydenova, I. ;
Vlasov, P. A. ;
Warnatz, J. .
PROCEEDINGS OF THE COMBUSTION INSTITUTE, 2007, 31 (575-583) :575-583
[5]  
[Anonymous], 2015, PROJ COSTS GEN EL
[6]   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
[7]   Hydrogen production from natural gas, sequestration of recovered CO2 in depleted gas wells and enhanced natural gas recovery [J].
Blok, K ;
Williams, RH ;
Katofsky, RE ;
Hendriks, CA .
ENERGY, 1997, 22 (2-3) :161-168
[8]   PAH formation in acetylene-benzene pyrolysis [J].
Böhm, H ;
Jander, H .
PHYSICAL CHEMISTRY CHEMICAL PHYSICS, 1999, 1 (16) :3775-3781
[9]  
Böhm H, 1998, TWENTY-SEVENTH SYMPOSIUM (INTERNATIONAL) ON COMBUSTION, VOLS 1 AND 2, P1605
[10]   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