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首页> 外文期刊>Energy Conversion & Management >Performance prediction of a decentralized power plant (120 kWe) using a multi-particle model of a downdraft biomass gasification process
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Performance prediction of a decentralized power plant (120 kWe) using a multi-particle model of a downdraft biomass gasification process

机译:使用向下气流生物质气化过程的多粒子模型预测分散式发电厂(120 kWe)的性能

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摘要

A one-dimensional model of a downdraft biomass gasifier is presented to investigate the effect of operating parameters on the performance of a power plant. The approach considers the biomass fed to the reactor by employing discrete particle size distribution (DPSD) to simulate the real operational conditions of a gasification power plant (120 kW(e)/400 kW(th)). Char production (byproduct) and producer gas (PG) flow are the targets of the model; the model has been validated using data from an industrial power plant (biomass consumption, pressure drop, and PG composition) with an average relative error of 1.8%. The model achieved stable and reliable results using DPSD for 16 different particle sizes. The increase in the mean biomass particle diameter (15-60 mm) diminished the PG power (363.8-285.3 kW) and the cold gas efficiency (CGE) (63.2-54.36%) because of low particle surface/volume ratio. When biomass moisture content increased (5-25 wt%), the PG power decreased (364.14-318.75 kW) because of low gasification temperature. Moreover, when the number of driven engines was increased from 2 to 5 (electric power), the CGE decreased (68.17-59.17%) due to the low residence time of the solid and gas phases, which inhibited the gasification reactions, in the reactor.
机译:提出了一种向下流式生物质气化炉的一维模型,以研究运行参数对电厂性能的影响。该方法通过采用离散粒度分布(DPSD)来模拟气化发电厂的实际运行条件(120 kW(e)/ 400 kW(th)),从而考虑了进料到反应器中的生物质。焦炭生产(副产品)和生产气体(PG)流量是该模型的目标。该模型已使用来自工业发电厂的数据(生物质消耗,压降和PG组成)进行了验证,平均相对误差为1.8%。使用DPSD对16种不同的粒径,该模型获得了稳定可靠的结果。由于较低的颗粒表面积/体积比,平均生物质颗粒直径(15-60 mm)的增加降低了PG功率(363.8-285.3 kW)和冷气效率(CGE)(63.2-54.36%)。当生物质水分含量增加(5-25 wt%)时,由于气化温度低,PG功率降低(364.14-318.75 kW)。此外,当从动发动机的数量从2个增加到5个(电力)时,CGE下降(68.17-59.17%),这是由于固相和气相的停留时间短,从而抑制了气化反应, 。

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