Process Simulation Development of Coal Combustion in a Circulating Fluidized Bed Combustor Based on Aspen Plus
文献类型：期刊论文
| 作者 | Liu, Bing1,2; Yang, Xuemin1; Song, Wenli1; Lin, Weigang1 |
| 刊名 | ENERGY & FUELS
 |
| 出版日期 | 2011-04-01 |
| 卷号 | 25期号:4页码:1721-1730 |
| 关键词 | single-particle emissions biomass model cfb n2o boilers riser char gas |
| ISSN号 | 0887-0624 |
| 其他题名 | Energy Fuels |
| 中文摘要 | A process simulation model has been developed to simulate and predict the condition of three kinds of coal combustion in a 30 kW circulating fluidized bed combustor based on Aspen Plus with considering gas-solid hydrodynamics via Aspen Plus in-line FORTRAN codes and combustion reaction kinetics via some external FORTRAN subroutines simultaneously. The related mathematical models in the process simulation, such as a gas-solid hydrodynamics model in the CFB riser, equivalent pyrolysis model of coal, and combustion kinetics model of coal pyrolysis products, have been presented in detail. The profiles of voidage and gas pressure along the height of riser are discussed and preliminarily predicted by the developed model in this paper. It Can be concluded from the results of the process simulation model that increasing gas superficial velocity can lead to a decrease of voidage in the dense region and lower acceleration region, and a slight increase of voidage in the upper acceleration region and completely fluidized region. Furthermore, increasing gas superficial velocity can also effectively increase the total pressure drop of the riser. Therefore, a larger inlet pressure is required when more primary air is introduced into the riser bottom. |
| 英文摘要 | A process simulation model has been developed to simulate and predict the condition of three kinds of coal combustion in a 30 kW circulating fluidized bed combustor based on Aspen Plus with considering gas-solid hydrodynamics via Aspen Plus in-line FORTRAN codes and combustion reaction kinetics via some external FORTRAN subroutines simultaneously. The related mathematical models in the process simulation, such as a gas-solid hydrodynamics model in the CFB riser, equivalent pyrolysis model of coal, and combustion kinetics model of coal pyrolysis products, have been presented in detail. The profiles of voidage and gas pressure along the height of riser are discussed and preliminarily predicted by the developed model in this paper. It Can be concluded from the results of the process simulation model that increasing gas superficial velocity can lead to a decrease of voidage in the dense region and lower acceleration region, and a slight increase of voidage in the upper acceleration region and completely fluidized region. Furthermore, increasing gas superficial velocity can also effectively increase the total pressure drop of the riser. Therefore, a larger inlet pressure is required when more primary air is introduced into the riser bottom. |
| WOS标题词 | Science & Technology ; Technology |
| 类目[WOS] | Energy & Fuels ; Engineering, Chemical |
| 研究领域[WOS] | Energy & Fuels ; Engineering |
| 关键词[WOS] | SINGLE-PARTICLE ; EMISSIONS ; BIOMASS ; MODEL ; CFB ; N2O ; BOILERS ; RISER ; CHAR ; GAS |
| 收录类别 | SCI |
| 原文出处 | |
| 语种 | 英语 |
| WOS记录号 | WOS:000289697700044 |
| 公开日期 | 2013-11-28 |
| 版本 | 出版稿 |
| 源URL | [http://ir.ipe.ac.cn/handle/122111/6456]  |
| 专题 | 过程工程研究所_研究所（批量导入） |
| 作者单位 | 1.Chinese Acad Sci, Inst Proc Engn, State Key Lab Multiphase Complex Syst, Beijing 100190, Peoples R China 2.Chinese Acad Sci, Grad Univ, Beijing 100039, Peoples R China |
| 推荐引用方式 GB/T 7714 | Liu, Bing,Yang, Xuemin,Song, Wenli,et al. Process Simulation Development of Coal Combustion in a Circulating Fluidized Bed Combustor Based on Aspen Plus[J]. ENERGY & FUELS,2011,25(4):1721-1730. |
| APA | Liu, Bing,Yang, Xuemin,Song, Wenli,&Lin, Weigang.(2011).Process Simulation Development of Coal Combustion in a Circulating Fluidized Bed Combustor Based on Aspen Plus.ENERGY & FUELS,25(4),1721-1730. |
| MLA | Liu, Bing,et al."Process Simulation Development of Coal Combustion in a Circulating Fluidized Bed Combustor Based on Aspen Plus".ENERGY & FUELS 25.4(2011):1721-1730. |
入库方式： OAI收割
来源：过程工程研究所
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