油棕叶下吸式气化炉的建模与仿真研究

S. M. Atnaw, S. Sulaiman
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引用次数: 16

摘要

生物质气化提供清洁、可燃、能量充足的气体,可用于发电、发动机等。然而,气化炉的成功设计和操作并不简单。没有整齐的规则,因为气化炉操作的热力学还没有很好地理解。本文对油棕叶下吸式生物质气化炉的运行和性能进行了初步研究。性能研究部分使用ASPEN PLUS过程模拟器软件进行建模和模拟气化过程的各个区域(干燥、热解、氧化和还原)。由于ASPEN PLUS没有内置的气化炉模型,因此使用模拟器的各种反应器的组合来模拟气化过程。利用该模型对不同工作温度、压力和空燃比下的产气成分进行了预测。此外,还进行了初步实验,以确定OPF作为气化原料的可行性。模拟研究表明,在较低的空燃比和较低的压力(低于5bar)下,可以获得较高的CO和CH4质量分数。在500 ~ 700℃范围内,CO的质量分数随着氧化区温度的升高而急剧增加。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
Modeling and simulation study of downdraft gasifier using oil-palm fronds
Gasification of biomass provides clean and combustible gas with sufficient energy, which can be used for electricity generation, engine applications etc. However, successful design and operation of gasifiers are not simple. There are no neat rules as the thermodynamics of gasifier operation are not well understood. In this paper, a preliminary study of the operation and performance of downdraft biomass gasifier using oil palm fronds (OPF) is done. The performance study is partially carried out using ASPEN PLUS process simulator software for modeling and simulating the various zones of the gasification process (drying, pyrolysis, oxidation and reduction). As ASPEN PLUS does not have a built in gasifier model, a combination of the various reactors of the simulator are used to model the gasification processes. This model is used to predict the producer gas composition for different operating temperatures, pressure and air-fuel ratio. In addition a primary experiment is carried out to determine the feasibility of OPF as a gasification feedstock. From the simulation study it is shown that higher mass fraction of CO and CH4 can be obtained at lower Air-Fuel ratio, and lower pressure (below 5bar). The mass fraction of CO increases sharply with increase in the oxidation zone temperature, for the range 500–700°C.
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