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飞灰沉积行为与粒度分布关系的研究 被引量:2

Studying on the Relationship Between Fly Ash Deposition Behavior and the Particle Size Distribution
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摘要 针对Shell煤气化装置合成气冷却器段出现的积灰与堵灰现象,选取Shell煤气化飞灰(SH)与电厂飞灰(DH),利用Shell煤气化冷态模拟装置采集沉积于器壁的飞灰样品,并采用激光粒度分析仪进行粒度分布的研究。结果表明:DH飞灰粒度大于SH飞灰,喷射时间相同时,DH飞灰沉积质量大于SH飞灰,且DH飞灰与SH飞灰分别在沉积30 s与60 s时D 50为最大值,其他喷射时间下D50相差不大,随着喷射时间的延长,DH飞灰颗粒(0~5μm)与SH飞灰颗粒(0~1μm)含量不断增多,DH飞灰颗粒(38~75μm)百分含量与SH飞灰颗粒(38~75μm)百分含量分别在沉积30 s与60 s时为最大值。 According to fly ash deposit and plugging at the synthetic gas cooling tower of the Shell coal gasification. Chose Shell coal gasification fly ash (SH) and power plant fly ash (DH).Shell Coal Gasification Cold Model Unit was applied to collect the fly ash samples deposit on the wall. And Laser Particle Size Analyzer was applied to study on particle size distribution. The study results showed that, DH fly ash particle size is greater than the SH fly ash. In the same spraying time, the deposition quality of DH fly ash is more than SH fly ash. The D50 of DH fly ash and SH fly ash is a maximum respectively in sedimentary 30 s and 60 s. In other spraying time, the D50 differ not quite. Along with the extension of spraying time,the percentage of DH fly ash particles (0-5 μm) and SH fly ash particles (0-1 μm) increased, and the percentage of DH fly ash particles (38-75 μm) and SH fly ash particles (38-75 pro) is a maximum respectively in sedimentary 30 s and 60 s.
出处 《广东化工》 CAS 2012年第18期10-12,31,共4页 Guangdong Chemical Industry
基金 安徽理工大学博士基金资助项目(2010yb008)
关键词 飞灰 冷态模拟装置 沉积 粒度分布 fly ash cold model unit deposition particle size distribution
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  • 1常祖山.壳牌煤气化装置特点及存在问题和解决方案[J].大氮肥,2010,33(1):42-45. 被引量:5
  • 2许世森,任永强,夏军仓,王保民,李小宇,刘刚,张东亮,刘沅,李明亮,程健.两段式干煤粉加压气化技术的研究开发[J].中国电力,2006,39(6):30-33. 被引量:22
  • 3Bilski J,McLean K,McLcan E,et al.Preliminary studies on a coal fly ash utilization as growth media for selected cereal crops[J].Electronic Journal of Environmental,Agricultural and Food Chemistry,2012,11(5):558-564. 被引量:1
  • 4Oboirien B O,Engelbrecht A D,North B C,et al.Mineralchar interaction during gasification of high-ash coals in fluidized-bed gasification[J].Energy Fuels,2011,25(11):5189-5199. 被引量:1
  • 5Kelebopile L,Sun R,Liao J.Fly ash and coal char reactivity from thermo-gravimetric(TGA)experiments[J].Fuel Processing Technology,2011,92(6):1178-1186. 被引量:1
  • 6Gu J,Wu S Y,Wu Y Q,et al.Differences in gasification behaviors and related properties between entrained gasifier fly ash and coal char[J].Energy Fuels,2008,22(6):4029-4033. 被引量:1
  • 7Jing X L,Wang Z Q,Yu Z L,et al.Experimental and kinetic investigations of CO2gasification of fine chars separated from a pilot-scale fluidized-bed gasifier[J].Energy Fuels,2013,27(5):2422-2430. 被引量:1
  • 8Li S H,Wu Y X,Whitty J K.Ash deposition behavior during char-slag transition under simulated gasification conditions[J].Energy Fuels,2010,24(3):1868-1876. 被引量:1
  • 9Bartels M,Lin W G,Nijenhuis J,et al.Agglomeration in fluidized beds at high temperatures:mechanisms,detection and prevention[J].Progress in Energy and Combustion Science,2008,34(5):633-666. 被引量:1
  • 10Zhao X L,Zeng C,Mao Y Y,et al.The surface characteristics and reactivity of residual carbon in coal gasification slag[J].Energy Fuels,2010,24(1):91-94. 被引量:1

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