Volume 43 Issue 05
May  2015
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YANG Tian-hua, SUN Hai-peng, SUN Yang, KAI Xing-ping, LI Jie, LI Run-dong. Influence of deashing pretreatments on physicochemical properties and steam gasification reaction characteristics of rice straw[J]. Journal of Fuel Chemistry and Technology, 2015, 43(05): 598-606.
Citation: YANG Tian-hua, SUN Hai-peng, SUN Yang, KAI Xing-ping, LI Jie, LI Run-dong. Influence of deashing pretreatments on physicochemical properties and steam gasification reaction characteristics of rice straw[J]. Journal of Fuel Chemistry and Technology, 2015, 43(05): 598-606.

Influence of deashing pretreatments on physicochemical properties and steam gasification reaction characteristics of rice straw

  • Received Date: 2014-10-22
  • Publish Date: 2015-05-30
  • The influences of water-leaching and different concentration acid-leaching pretreatments on physicochemical properties and steam gasification reaction characteristics of rice straw (RS) were investigated in a laboratory fixed-bed reactor. The results show that after water-leaching, the potassium and sodium in RS are removed by 90.5% and 82.1%, respectively, and after acid-leaching, the removal of potassium from RS reaches to 99.2%, and the removal efficiency of sodium with acids is between 84.6% and 92.3%. Acid leaching does not change the main component content of RS, but destroys the microscopic structures of RS. The order of different concentration acid-treated RSs with respect to the three indexes including pore volume, pore diameter distribution and specific surface area is: all water-leached RS > 3% sulfuric acid-treated RS > raw RS > 7% sulfuric acid-treated RS > 10% sulfuric acid-treated RS. As the concentration of various pretreatment acids is 3%, the sulfuric acid-treated RS has the largest values of the three indexes and the phosphoric acid-treated RS has the smallest values of the three indexes. The steam gasification results show that potassium, sodium and abundant pore structure all can promote hydrogen generation, and the effects of potassium and sodium on gasification process are significantly stronger than pore structure. The H2 and CO2 instantaneous release concentration for water-leached RS is higher than that for acid-treated RS during gasification; however, it is contrary to CO and CH4. When the four acids concentration is 3%, there is a positive correlation between H2 and CO2 instantaneous release concentration and the pore diameter distribution; and there is a negative correlation between CO and CH4 instantaneous release concentration and the pore diameter distribution. The more abundant the pore, the faster the gasification rate. Though deashing pretreatment decreases the H2 production, it increases the calorific value of gasification gas.
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  • HANS W S. WEC energy policy scenarios to 2050[J]. Energy Policy, 2008, 36(7): 2464-2470.
    World Energy Counil. World energy resources: 2013 Survey[EB]. http://www.worldenergy.org/-publications/2013/world-energy-resources-2013-survey, 2013-10.
    蒋剑春. 生物质能源应用研究现状与发展前景[J]. 林产化学与工业, 2002, 22(2): 75-80.(JIANG Jian-chun. Prospect on research and development ofbiomass energy utilization[J].Chem Ind Forest Prod, 2002, 22(2): 75-80.)
    REZAIYAN J, CHEREMISINOFF N P. Gasification technologies: A primer for engineersand scientists[M]. Boca Raton: Taylor & Francis, 2005.
    王艳, 陈文义, 孙姣, 石海波, 陈晓东. 国内外生物质气化设备研究进展[J]. 化工进展, 2012, 31(8): 1656-1664.(WANG Yan, CHEN Wen-yi, SUN Jiao, SHI Hai-bo, CHEN Xiao-dong. Research progress in biomass gasification equipment[J].Chem Ind Eng Prog, 2012, 31(8): 1656-1664.)
    常轩, 齐永锋, 张冬冬, 徐亮. 生物质气化技术研究现状及其发展[J]. 现代化工, 2013, 33(6): 36-39.(CHANG Xuan, QI Yong-feng, ZHANG Dong-dong, XU Liang. Current status and development of biomass gasification technology[J]. Modern Chem Ind, 2013, 33(6): 36-39.)
    田原宇, 乔英云. 生物质气化技术面临的挑战及技术选择[J]. 中外能源, 2013, 8(22): 27-32.(TIAN Yuan-yu, QIAO Ying-yun. Biomass gasification technology challenges and technical options[J]. Sino Global Energy, 2013, 8(22): 27-32.)
    HIGMAN C, VANDER B M. Gasification[M]. 2nd ed. Burlington: Gulf Professional Publishing, 2008.
    HENRICH E, WEIRICH F. Pressurized entrained flow gasifiers for biomass[J]. Environ Eng Sci, 2004, 21(1): 53-64.
    FIORENZO A, ANDREA A, PAOLA B, FRANCESCO S M, FABIO M. Entrained-flow gasification of coal under slagging conditions: Relevance of fuel-wall interaction and char segregation to the properties of solidwastes[J]. Fuel, 2013, 114: 44-55.
    KONG L X, BAI J, BAI Z Q, GUO Z X, LI W. Improvement of ash flow properties of low-rank coal for entrained flow gasifier[J]. Fuel, 2014, 120: 122-129.
    BARROSO J, BALLESTER J, FERRER L M, JIMÉNEZ S. Study of coal ash deposition in an entrained flow reactor: Influenceof coal type, blend composition and operating conditions[J]. Fuel Process Technol, 2006, 87(8): 737-752.
    GUO Q H, GONG Y, XU J L, YU G S, WANG F C. Particulate matter properties in a bench-scale entrained-flow coal waterslurry gasifier[J]. Powder Technol, 2014, 254: 125-130.
    FLETCHER D F, HAYNES B S, CHRISTO F C, JOSEPH S D. A CFD based combustion model of an entrained flow biomassgasifier[J]. Appl Math Model, 2000, 24(3): 165-182.
    张巍巍, 陈雪莉, 王辅臣, 代正华, 于遵宏. 基于ASPEN PLUS模拟生物质气流床气化工艺过程[J]. 太阳能学报, 2007, 28(12): 1360-1364.(ZHANG Wei-wei, CHEN Xue-li, WANG Fu-chen, DAI Zheng-hua, YU Zun-hong. Process simulation of biomass entrained flow gasification based on Aspen plus[J]. Act Energy Solar Sinica, 2007, 28(12): 1360-1364.)
    KAREL S, MICHAEL P, MILOSLAV H, JIRÍ M. Pretreatment and feeding of biomass for pressurized entrained flow gasification[J]. Fuel Process Technol, 2009, 90(5): 629-635.
    XIAO R R, CHEN X L, WANG F C, YU G S. Pyrolysis pretreatment of biomass for entrained-flow gasification[J]. Appl Energy, 2010, 87(1): 149-155.
    陈青. 生物质高温气流床气化合成气制备及优化研究[D]. 浙江: 浙江大学, 2012.(CHEN Qing. Study and optimization of biomass gasification in a high temperature entrained flow gasifer for syngas[D]. Zhejiang University, 2007.)
    赵辉. 生物质高温气流床气化制取合成气的机理试验研究[D].浙江: 浙江大学, 2007.(ZHAO Hui.Experimental and mechanism research on entrained flow gasification of biomass for syngas[D]. Zhejiang: Zhejiang University, 2007.)
    QIN K, LIN WG, JENSEN P A, JENSEN A D. High-temperature entrained flow gasification of biomass[J]. Fuel, 2012, 93: 589-600.
    苏德仁, 周肇秋, 谢建军, 朗林, 阴秀丽, 吴创之. 生物质流化床富氧-水蒸气气化制备合成气研究[J]. 农业机械学报, 2011, 42(3): 100-104.(SU De-ren, ZHOU Zhao-qiu, XIE Jian-jun, LANG Lin, YIN Xiu-li, WU Chuang-zhi. Bioma machinery ss oxygen entrained enrich-steam gasification in an atmospheric fluidized bed for syngas production[J]. Trans Chin Soc Agric Mach, 2011, 42(3): 100-104.)
    SALAH H A, KATSUYA K. Bench-scale gasification of cedar wood-Part II: Effect of operational conditions on contaminant release[J]. Chemosphere, 2013, 90: 1501-1507.
    HERNANDEZA J J, ARANDA G, BARBA J, MENDOZA J M. Effect of steam content in the air-steam flow on biomass entrained flow gasification[J]. Fuel Process Technol, 2012, 99: 43-55.
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