JOURNAL OF SHANDONG UNIVERSITY (ENGINEERING SCIENCE) ›› 2014, Vol. 44 ›› Issue (5): 78-82.doi: 10.6040/j.issn.1672-3961.0.2013.318

Previous Articles     Next Articles

Influence of pressure on active-air biomass gasification

SUN Hongyu1, ZHANG Zhaoling2, DONG Yuping3   

  1. 1. School of Mechanical Engineering, Liaoning Shihua University, Fushun 113001, Liaoning, China;
    2. Shandong Baichuan Tongchuang Co. Ltd., Jinan 250101, Shandong, China;
    3. Key Laboratory of High Efficiency and Clean Mechanical Manufacture, Ministry of Education, Shandong University, Jinan 250061, Shandong, China
  • Received:2013-11-06 Revised:2014-05-21 Published:2013-11-06

PDF (PC)

540

Abstract: The influence of bed pressure was investigate by the method of experiment. Air was used as gasifying agent during the biomass gasification experiment. Analysised the inner relationship of pressure, temperature and calorific value. The study results showed that optimum pressure range was 1.6-2.9 kPa in the experimental condition. In this pressure environment, the temperature of oxide layer reached 1 000-1 300 ℃, calorific value reached 4 900-5 700 kJ/m3, tar content decreased with the increasing temperature. However the oxide layer temperature decreased when pressure drop exceed 2.9 kPa, therefore, the influence of pressure on gas quality appeared fluctuating trend, research results could provide a reference for the study on kinetics of reaction of biomass gasification.

Key words: active-air gasification, pressure drop, production gas, kinetics of reaction, calorific value

CLC Number: 

  • TK6
[1] 肖波,周英彪.生物质能源循环经济技术[M].北京: 化学工业出版社,2006.
[2] 董玉平,邓波,景元琢,等.中国生物质气化技术的研究和发展现状[J].山东大学学报:工学版, 2007, 37(2):1-7.DONG Yuping, DENG Bo, JING Yuanzhuo, et al.A review of the research and development of gasification technology in China[J].Journal of Shandong University: Engineering Science, 2007, 37(2):1-7.
[3] MOHAMED G, ESBJOM P, RAINER B, et al.Evaluation of cyclone gasifier performance for gasification of sugar cane residue-Part 1: gasification of biomass[J].Biomass and Bioenergy, 2001, 21(5):351-369.
[4] KNIGHT R.A Experience with raw gas analysis from pressurized gasification of biomass[J].Biomass and Bioenergy, 2000, 18(1):67-77.
[5] MCLENDON T R, LUI A P, PINEAULT R L, et al.High-pressure co-gasification of coal and biomass in a fluidized bed[J].Biomass and Bioenergy, 2004, 26(4):377-388.
[6] YANG Weihong, ANNA P, CARLOS L, et al.Performance analysis of a fixed-bed biomass gasifier using high-temperature air[J].Fuel Processing Technology, 2006, 87(1):235-245.
[7] 黄亚继,金保升,仲兆平,等.气化压力对煤气化过程中痕量元素迁移规律的影响[J].东南大学学报,2008, 38(1):93-96.HUANG Yaji, JIN Baosheng, ZHONG Zhaoping, et al.Effect of gasification pressure on the occurred nce of trace elements[J].Journal of Southeast University, 2008, 38(1):93-96.
[8] AHMED Y M Z, EWAIS E M, ZAKI Z I.Production of porous silica by the combustion of rice husk ash for tundish lining[J].Journal of University of Science and Technology Beijing, 2008, 15(3):307-313.
[9] 傅旭峰,仲兆平,肖刚,等.几种生物质热解特性及动力学的对比[J].农业工程学报,2009,25(1):199-202.FU Xufeng, ZHONG Zhaoping, Xiao Gang, et al.Comparative study on pyrolysis characteristics and dynamics of grass biomass[J].Transactions of the CSAE, 2009, 25(1):199-202.
[10] SOSTROM G, CHEN Q, YU C, et al.Catalytic effects observed during the co-gasification of coal and switchgrass[J].Biomass and Bioenergy, 2000, 18(6):499-506.
[11] LEUNG D Y C, YIN X L, WU C Z.A review on the development and commercialization of biomass gasification technologies in China[J].Renewable and Sustainable Energy Reviews, 2004, 8(6):565-580.
[12] HAYKIRI-ACMA H, YAMAN S.Thermal reactivity of rapeseed(brassicanapus L) under different gas atmosphere[J].Bioresource Technology, 2008, 99(2):237-242.
[13] WILLIAMS P T,BESLER A.The influence of temperature and heating rate on the slow pyrolysis of biomass[J].Renewable Energy, 1996, 7(3):233-250.
[14] XIONG Yuanquan.Experiment and research of coal pressurized thermogravimetric analysis[D].Nanjing: Southeast University, 1995.
[15] 赖艳华,吕明新,马春元,等.缩口结构对降低生物质两段气化中焦油生成量的影响研究[J].太阳能学报, 2004, 25(4):547-551.LAI Yanhua, L Mingxin, MA Chunyuan, et al.Study on the influence of throat structure on reducing tar content of two-stage biomass gasification reactor[J].ACTA ENERGIAE SOLARIS SINICA, 2004, 25(4):547-551.
[16] 杨猛.计算流体力学两相流流动的模拟及两相流模型的研究[D].天津:天津大学,2005.
[17] KUMABE K, HANAOKA T, FUJIMOTO S.Co-gasification of woody biomass and coal with air and steam[J].Fuel, 2007, 86(5):684-689.
[18] FRANCO C, PINTO F, GULYURTLU L, et al.The study of reactions influencing the biomass steam gasification process[J].Fuel, 2003, 62(1):835-842.
[19] HANAOKA T, INOUE S, UNO S.Effect of woody biomass components on air-steam gasification[J].Biomass and bioenergy, 2005, 28(1):69-76.
[20] ZHOU Hongcang.Air and steam coal partial gasification in an atmospheric fluidized bed[J].Energy ＆ Fuels, 2005, 19(4):1619-1623.
[21] MERMOUD F, SALVADOR S, van de STEENE L, et al.Influence of the pyrolysis heating rate on the steam gasification rate of large wood char particles[J].Fuel, 2006, 85(11):1473-1482.
[22] HAYKIRI-ACMA H, YAMAN S, KUCUKBAYRAK S.Gasification of biomass chars in steam-nitrogen mixture[J].Energy Conversion and Management, 2006, 47(8):1004-1013.
[23] SENNECA O.Kinetics of pyrolysis, combustion and gasification of three biomass fuels[J].Fuel Processing Technology, 2007, 88(1):87-97.
[1] DONG Yu-ping,WANG Li-peng,DENG Bo,LU Ping,SHEN Shu-yun . A review of the research and development of biomass energy technology [J]. JOURNAL OF SHANDONG UNIVERSITY (ENGINEERING SCIENCE), 2007, 37(3): 64-69 .
[2] DONG Yu-ping,DENG Bo,JING Yuan-zhuo,QIANG Ning,SHEN Shu-yun . A review of the research and development of biomass gasification technology in China [J]. JOURNAL OF SHANDONG UNIVERSITY (ENGINEERING SCIENCE), 2007, 37(2): 1-7 .
Viewed
Full text


Abstract

Cited
  Shared   
  Discussed   
No Suggested Reading articles found!
Copyright 2018 © Editorial office of Journal of Shandong University (Engineering Science)
Supported by Beijing Magtech Co.Ltd