西安交通大学动力工程多相流国家重点实验室,西安,710049
网络首发:2009-01-10,
纸质出版:2009
移动端阅览
吕友军, 金辉, 郭烈锦, 等. 生物质在超临界水流化床系统中部分氧化气化制氢[J]. 西安交通大学学报, 2009,43(1):5-9.
Hydrogen Production by Partial Oxidation Gasification of Biomass in Supercritical Water with Fluidization Bed Reactor[J]. 2009, 43(1): 5-9.
从理论的角度对超临界水部分氧化过程进行分析
利用已建立的热力学模型计算了反应过程的化学平衡.热力学研究表明:随着氧化剂当量的增加
H
2
、CH
4
、CO的平衡产量减少
CO
2
的平衡产量增加
而且H
2
的体积分数也随之减少.在实验室新研制的超临界水流化床系统中
研究了生物质模型化合物(葡萄糖)以及原生生物质(玉米芯)的部分氧化气化制氢.实验结果表明:氧化剂的加入大大提高了生物质的气化率
但降低了气体产物中H
2
的体积分数; 在质量分数为10%的葡萄糖部分氧化气化过程中
当氧化剂(H
2
O
2
)当量为0.2(质量分数为4.53%)时
H
2
的绝对产量达到了最大值.
Supercritical partial oxidation is a new technology which combines supercritical water gasification with supercritical water oxidation for high efficient hydrogen production from biomass. Supercritical partial oxidation process was analyzed theoretically
and chemical equilibrium was calculated using the thermodynamic model. It is found that the equilibrium yield of hydrogen
methane
carbon monoxide
and the molar fraction of hydrogen decrease
while the equilibrium yield of carbon dioxide increases with the increase of the oxidant equivalence ratio. Experiments on hydrogen production by partial oxidation of model compound(glucose)and real biomass(corn cob)with SCW fluidization bed were also conducted. The results show that the gasification efficiency increases sharply with the additi
on of oxidant which reduces the molar fraction of hydrogen. During partial oxidation gasification process of 10% glucose
the hydrogen yield reaches maximum when the oxidant(H
2
O
2
)equivalence ratio is 0.2(i.e.
mass fraction of 4.53%).
吕友军, 冀承猛, 郭烈锦. 农业生物质超临界水气化制氢实验研究[J]. 西安交通大学学报, 2005, 39(3):238-242.
LÜ Youjun, JI Chengmeng, GUO Liejin. Experimental investigation on hydrogen production by agricultural biomass gasification in supercritical water [J]. Journal of Xi'an Jiaotong University, 2005, 39(3):238-242.
YOSHIDA Y, DOWAKI K, MATSUMURA Y, et al. Comprehensive comparison of efficiency and CO2 emissions between biomass energy conversion technologies:position of supercritical water gasification in biomass technologies [J]. Biomass and Bioenergy, 2003, 25(3): 257-27.
郝小红.生物质超临界水气化制氢[D].西安:西安交通大学能源与动力工程学院, 2004.
LÜ Y J, GUO L J, JI C M, et al. Hydrogen production by biomass gasification in supercritical water: a parametric study [J]. Int J Hydrogen Energy, 2006, 31(7): 822-831.
HONG G T, SPRITZER M H. Supercritical water oxidation [EB/OL]. [2004-03-25]. http:∥www.doe.gov/.
WATANABE M, INOMATA H, OSADA M, et al. Catalytic effects of NaOH and ZrO2 for partial oxidative gasification of n-hexadecane and lignin in supercritical water [J]. Fuel, 2003, 82(5):545-552.
ARAI K, ADSCHIRI T, WATANABE M. Hydrogenation of hydrocarbons through partial oxidation in supercritical water [J]. Ind Eng Chem Res, 2000, 39(12): 4697-4701.
WATANABE M, MOCHIDUKI M, SAWAMOTO S, et al. Partial oxidation of n-hexadecane and polyethylene in supercritical water[J]. Journal of Supercritical Fluids, 2001, 20(3): 257-266.
ARMBRUSTER U, MARTIN A, KREPEL A. Partial oxidation of propane in sub- and supercritical water [J]. Journal of Supercritical Fluids, 2001, 21(3): 233-243.
JOHANSON N W, SPRITZER M H, HONG G T, et al. Supercritical water partial oxidation [EB/OL]. [2006-06-20]. http:∥www.doe.gov/.
ANTAL M J, MANARUNGSON S, MOK W S. Hydrogen production by steam reforming glucose in supercritical water [J]. Adv Thermochem Biomass Convers, 1994, 3(2): 1367-1377.
YAN Q H, GUO L J, LÜ Y J. Thermodynamic analysis of hydrogen production from biomass gasification in supercritical water [J]. Energy Conversion and Management, 2006, 47(11): 1515-1528.
吕友军.生物质超临界水流化床气化系统的研制与气化制氢特性研究[D].西安:西安交通大学能源与动力工程学院, 2007.
SINAG A, KRUSE A, SCHWARZKOPF V. Key compounds of the hydropyrolysis of glucose in supercritical water in the presence of K2CO3 [J]. Ind Eng Chem Res, 2003, 42(15): 3516-3521.
SAVAGE P E. Organic chemical reactions in supercritical water [J]. Chem Rev, 1999, 99(2):603-621.
0
浏览量
4
下载量
0
CSCD
关联资源
相关文章
相关作者
相关机构
京公网安备11010802024621