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Frontiers in Energy

ISSN 2095-1701

ISSN 2095-1698(Online)

CN 11-6017/TK

Postal Subscription Code 80-972

2018 Impact Factor: 1.701

Front. Energy    2009, Vol. 3 Issue (1) : 117-122    https://doi.org/10.1007/s11708-008-0078-2
Research articles
Process analysis of syngas production by non-catalytic POX of oven gas
Fuchen WANG , Xinwen ZHOU , Wenyuan GUO , Zhenghua DAI , Xin GONG , Haifeng LIU , Zunhong YU ,
Institute of Clean Coal Technology, East China University of Science and Technology;
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Abstract A non-catalytic POX of oven gas is proposed to solve the problem of secondary pollution due to solid wastes produced from the great amount of organic sulfur contained in oven gas in the traditional catalytic partial oxidation (POX) process. A study of the measurement of flow field and a thermodynamic analysis of the process characteristics were conducted. Results show that there exist a jet-flow region, a recirculation-flow region, a tube-flow region, and three corresponding reaction zones in the non-catalytic POX reformer. The combustion of oven gas occurs mainly in the jet-flow region, while the reformation of oven gas occurs mainly in the other two regions. Soot would not be formed by CH4 cracking at above 1200°C. Since there are very little C2+ hydrocarbons in oven gas, the soot produced would be very tiny, even if they underwent cracking reaction. The integrated model for entrained bed gasification process was applied to simulate a non-catalytic POX reformer. It indicated that the proper oxygen-to-oven gas ratio is 0.22–0.28 at different pressures in the oven gas reformation process.
Keywords oven gas      non-catalytic POX process      syngas      
Issue Date: 05 March 2009
 Cite this article:   
Fuchen WANG,Wenyuan GUO,Xinwen ZHOU, et al. Process analysis of syngas production by non-catalytic POX of oven gas[J]. Front. Energy, 2009, 3(1): 117-122.
 URL:  
https://academic.hep.com.cn/fie/EN/10.1007/s11708-008-0078-2
https://academic.hep.com.cn/fie/EN/Y2009/V3/I1/117
Fan Weitang, Du Minghua. Present situation and prospectof coal chemical industry in China. International Hi-Tech Symposiumon Coal Chemical Industry and Coal Conversion. Shanghai, 2004, 4–8
hen Weiguo. Developing foreground of alcohol-ether fuel in China and methanolmanufacture technology process by oven-gas. International Hi-TechSymposium on Coal Chemical Industry and Coal Conversion. Shanghai, 2004, 208–219
Johansen T, Raghuraman K S, Hackett L A. Trends in hydrogen plant design. Hydrocarbon Process, 1992, 71(8): 119–127
Dybkjœr I. Tubularreforming and autothermal reforming of natural gas-an overview ofavailable processes. Fuel Processing Technology, 1995, 42(2, 3): 85–107

doi: 10.1016/0378-3820(94)00099-F
Miyasagi T, Tasaka S, Kawai T, Suzuki A. A heat-exchangertype steam reformer for ammonia production. Ammonia Plant Sar, 1984, 25: 64–68
Zhu J, Zhang D, King K D. Reforming of CH4 by partial oxidationthermodynamic and kinetic analyses. Fuel, 2001, 80(7): 899–905

doi: 10.1016/S0016-2361(00)00165-4
Thomas S, Andrew P E Y, Ahmad H, et al. Potential utilization of Indonesia's Natunanatural gas field via methane dry reforming to synthesis gas. Catalysis Letters, 2001, 71(1): 49–54

doi: 10.1023/A:1016600223749
Hou Kaihu, Ronald H. The kinetics of methane steamreforming over a Ni/α-Al2O3 catalyst. Chemical EngineeringJournal, 2001, 82(3): 311–328

doi: 10.1016/S1385-8947(00)00367-3
Vaso A T, Xenophon E V. Kinetic study of catalyticreforming of methane with carbon dioxide to synthesis gas over Ni/La2O3 catalyst. Catalysis Today, 2001, 64(1,2): 83–90
Yu Zunhong, Yu Jianguo, Wang Fuchen, et al. Research on residual-oil gasification with twin-fluidatomizer (II) zone model of gasification reaction. Journal of Chemical Industry and Engineering, 1994, 45(2): 135–139 (in Chinese)
Wang Fuchen. Investigation on jet-entrained gasification technology process. Dissertation for the Doctoral Degree. Shanghai: East China University of Science and Technology, 1995, 60–80 (in Chinese)
Wang Fuchen, Wu Tao, Yu Jianguo, et al. Macro-mixing process investigation for jet-entrainedgasifier (III): Process analysis and simulation. Journal of Chemical Industry and Engineering, 1997, 48(3): 337–346 (in Chinese)
Wang Fuchen, Li Weifeng, Dai Zhenghua, et al. Investigation for manufactory synthesis gasby natural-gas non-catalyst partial oxidization process. Petrochemical Technology, 2006, 45(1): 47–51(in Chinese)
Rostrup-Nielsen J R. Sulfur-passivated nickel catalysts for carbon-free steam reformingof methane. Journal of Catalysis, 1984, 85(1): 31–43

doi: 10.1016/0021-9517(84)90107-6
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