期刊文献+

生物质费托合成制取液体燃料的仿真及分析 被引量:1

SIMULATION AND ENERGY ANALYSIS OF LIQUID FUEL PRODUCED BY FISCHER-TROPSCH SYNTHESIS OF BIOMASS
下载PDF
导出
摘要 以生物质费托合成制取液体燃料工艺为基础,利用Aspen Plus软件建立其流程的仿真模型,研究各单元操作参数变化对航空煤油产量的影响,并在最优工况下对系统进行能量分析。结果表明:生物质气化单元对航油产量的影响主要来自产物合成气中H_(2)与CO物质的量之比(H_(2)/CO),最优操作条件为T=750℃,P=0.1 MPa,进口水蒸气与生物质质量比(S/B)为0.5;加大FT合成温度和压力可增大航油产量和提高能量利用效率,最优费托合成温度为230℃,压力为2.5 MPa;在最优工况下,当收益[火用]仅为航煤[火用]时,系统总[火用]效率为49.67%,若将全部副产品算入收益[火用]中,总[火用]效率为59.48%。 Based on the route of biomass gasification with Fischer-Tropsch synthesis to produce liquid fuel,and using Aspen Plus software to establish the simulation model of the process,the influence of operation parameters of each unit on aviation kerosene output was studied.The energy usage ratio of the whole system under optimal conditions was analyzed.The results reveal that the impact of biomass gasification unit on jet fuel production mainly come from the material ratio of H_(2)to CO(H_(2)/CO),the optimal gasification temperature is 750℃,pressure is 0.1 MPa,mass ratio of steam to biomass(S/B)is about 0.5.The fuel production and energy efficiency is improved with increasing FT synthesis temperature and pressure,the unit’s optimal Fischer-Tropsch synthesis temperature is 230℃,pressure is 2.5 MPa.Under the optimal condition,when the revenue exergy only contains jet fuel exergy,the total exergy efficiency is49.67%.When whole by-products exergy are included,the total exergy efficiency is 59.48%.
作者 邓玥 仲兆平 Deng Yue;Zhong Zhaoping(MOE Key Laboratory of Energy Thermal Conversion&Control,Southeast University,Nanjing 210018,China)
出处 《太阳能学报》 EI CAS CSCD 北大核心 2022年第4期468-473,共6页 Acta Energiae Solaris Sinica
基金 国家重点研发计划(2018YFB1501405)。
关键词 生物质气化 费托合成 航空燃料 [火用] Aspen Plus biomass gasification Fischer-Tropsch synthesis aircraft fuel exergy Aspen Plus
  • 相关文献

参考文献3

二级参考文献35

  • 1Vladimir I,Rachadaporn K, Songpol C. Effects of op- erating conditions and fuel properties on emission per- formance and combustion efficiency of a swirling fluid- ized-bed combustor fired with a biomass fuel [ J ]. Ener- gy, 2011, 36 (4): 2034-2048.
  • 2Meng K, Fei J H, Wang S, Lu W, Zheng X M. Influ- ence of supports on catalytic behavior of nickel catalysts in carbon dioxide reforming of toluene as a model com- pound of tar from biomass gasification [ J]. Bioresource Technology, 2011, 102 (2): 2004-2008.
  • 3Mazur V. Fuzzy thermoeconomic optimization of energy- transforming systems [ J]. Applied Energy, 2007, 84 (7 -8): 749 -762.
  • 4Luis R S J, Richard A G. Second-law efficiency analy- sis of a coal gasification process [ J ]. The Canadian Journal of Chemical Engineering, 1980, 58 (3) : 376 -381.
  • 5Ibrahim D. Technical, environmental and exergetic as- pects of hydrogen energy systems [ J ]. International Journal of Hydrogen Energy, 2002, 27 (3): 265- 285.
  • 6Yunus A C, Michael A B neering approach [ M ]. 1994. Thermodynamics: an engi- New York: McGraw-Hill.
  • 7Michael J M, Howard N S. Fundamentals of engineer- ing thermodynamics [ M ]. New York: John Wiley & Sons, 2000.
  • 8蒋光羲.燃料燃烧过程的炯分析.四川冶金,1985,(4):76-80.
  • 9朱玉琢 李炬.炯与节能(二).节能,1986,(7):20-24.
  • 10Selcuk B,Kamil K, Ahmet S. Second law analysis of various types of coal and woody biomass in Turkey [ Jl. Energy Sources, 2004, 26 (12) : 1083 - 1094.

共引文献10

同被引文献9

引证文献1

二级引证文献1

相关作者

内容加载中请稍等...

相关机构

内容加载中请稍等...

相关主题

内容加载中请稍等...

浏览历史

内容加载中请稍等...
;
使用帮助 返回顶部