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                                  | 论文编号: | 
                                  122214O120130254 | 
                                 
                                
                                  | 第一作者所在部门: | 
                                  103组 | 
                                 
                                
                                  | 中文论文题目: | 
                                  
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                                  | 英文论文题目: | 
                                  Fast Co-pyrolysis of Coal and Biomass in a Fluidized-bed Reactor
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                                  | 论文题目英文: | 
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                                  | 作者: | 
                                  王建飞
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                                  | 论文出处: | 
                                  
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                                  | 刊物名称: | 
                                  30th Annual International Pittsburgh Coal Conference.
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                                  | 年: | 
                                  2013
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                                  | 卷: | 
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                                  | 期: | 
                                  1 | 
                                 
                                
                                  | 页: | 
                                  0-0 | 
                                 
                                
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                                  | 收录类别: | 
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                                  | 影响因子: | 
                                  
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                                  | 摘要: | 
                                  The co-pyrolysis of coal/biomass is one of the most promising options for the
utilization of renewable fuels and has recently become one of the most desired
technologies to be worldwidely developed. Coal/biomass blends were prepared using
Yilan subbituminous (YL) and corncob (CB), the ratios of coal in mixtures were
varied between 0 and 100wt%. Co-pyrolysis characteristics were investigated in a
thermogravimetric analyzer (TGA) from 30 to 700℃with a heating rate of 10°C/min
and 40℃/min under the condition of nitrogen atmosphere and a flow of 100mL/min.
The residues of co-pyrolysis were less than the calculated. With the increase of
heating rate, the residues decreased severely more compared to expected values for all the blending ratios; In the fast pyrolysis fluidized-bed reactor, when the YL blending
ratios were less than 60%, the yields of pyrolysis-oil were higher than the expected at
the temperature of 600℃, this may be ascribed to the transfer of H/OH in volatiles of
biomass to coal. | 
                                 
                                
                                  | 英文摘要: | 
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