期刊文献+

生物质及其与惰性颗粒双组分体系的流化特性 被引量:2

Fluidization Characteristics of Bi-component System with Biomass and Inert Particles
在线阅读 下载PDF
导出
摘要 采用MDMDY-300型全自动密度仪和体积法测量了生物质和3种惰性颗粒的颗粒密度和堆密度,在有机玻璃流化床内考察了生物质单组分及其与3种惰性颗粒双组分体系的最小流化空隙率和流化速度。结果表明,单组分颗粒密度随粒径的变化可以忽略,而堆密度却随粒径的增大有所减小;双组分体系的最小流化空隙率随细颗粒组分增加而出现先减小后增大的趋势,最小值出现在细颗粒组分体积分数为30%左右,且颗粒粒径差异越大变化趋势越明显;双组分体系的起始流化速度、最小流化速度和完全流化速度均随细颗粒组分含量增加呈现减小的趋势,当细颗粒体积分数达到30%左右后起始流化速度的下降趋势趋于平缓。 The particle density and bulk density of biomass and three kinds of inert particles were measured using MDMDY-300 Automatic Density Meter and traditional volume method,respectively.The minimum voidage and minimum fluidization velocity of biomass monocomponent and three inert particles were observed in the plexiglas bed.The results indicate that the monocomponent particle density is almost independent from particle size,while the bulk density reduces with increment of particle size.The minimum voidage decreases when fine particles are introduced and reaches a minimum value at the fine particles of about 30 %(v/v).The minimum voidage of bi-component system starts to increase with fine particles increasing.Moreover,the greater the difference in particle size,the more obvious this trend.The initial,minimum and full fluidization velocities of bi-component system decrease with increment of the volume fraction of fine particle.It is similar to the minimum voidage,the minimum fluidization velocity decreases slowly when the volume fraction of fine particles is more than 30 % or so.
出处 《生物质化学工程》 CAS 2011年第1期15-20,共6页 Biomass Chemical Engineering
基金 国家自然科学基金资助(20976191) "十一五"国家科技支撑计划资助(2006BAD07A03) 教育部新世纪人才支持计划资助(09-0342)
关键词 生物质 惰性颗粒 双组分体系 流化特性 biomass inert particles bicomponent system fluidization characteristics
  • 相关文献

参考文献13

  • 1AUSILIO B,GORAN B,MARTIN J,et al.Bioenergy-a sustainable and reliable energy source,a review of status and prospects[R].IEA Bioenergy:Ex Co:2009:06.
  • 2CZERNIK S,BRIDGWATER A V.Overview of applications of biomass fast pyrolysis oil[J].Energy & Fuels,2004,18:590-598.
  • 3BABU B V.Biomass pyrolysis:A state-of-the-art review[J].Biofuels,Bioproducts & Biorefining,2008,2(5):393-414.
  • 4DENG C J,LIU R H,CAI J M.State of art of biomass fast pyrolysis for bio-oil in China:A review[J].Journal of the Energy Institute,2008,81(4):211-217.
  • 5DEMIRBAS M F,BALAT M.Biomass pyrolysis for liquid fuels and chemicals:A review[J].Journal of Scientific & Industrial Research,2007,66:797-804.
  • 6DESISTO W J,HILL II N,BEIS S H,et al.Fast pyrolysis of pine sawdust in a fluidized-bed reactor[J].Energy & Fuels,2010,24:2642-2651.
  • 7郑志锋,蒋剑春,戴伟娣,孙云娟.生物质能源转化技术与应用(Ⅲ)——生物质热解液体燃料油制备和精制技术[J].生物质化学工程,2007,41(5):67-77. 被引量:17
  • 8林木森,蒋剑春.生物质快速热解技术现状[J].生物质化学工程,2006,40(1):21-26. 被引量:39
  • 9刘宝亮,蒋剑春,岳金方,蔡明远.冷态鼓泡流化床中木屑流化速度的研究[J].林产化学与工业,2007,27(3):49-52. 被引量:8
  • 10GOOSSENS W R A,DUNMONT G L,SPAEPEN G L.Fluidization of binary mixtures in the laminar flow region[C].Chem Eng Prog Symp,1971,67:38-45.

二级参考文献125

共引文献60

同被引文献15

引证文献2

二级引证文献3

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