利用aspen plus®对下吸式气化炉蒸汽气氛下微藻气化的研究

Senem Sezer, F. Kartal, Berna Kekik, Uğur Özveren
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摘要

由于人口增长和化石燃料的不确定性,能源生产面临着环境和经济问题。这些担忧促使研究人员寻找广泛可用和可再生的替代品,如生物质能代替化石燃料。微藻因其生长速度快、热值高而成为生物燃料的发展方向之一。与其他热化学转化过程相比,蒸汽气化是一种将生物质转化为H2含量较高、CO2含量较低的合成气的替代方法。在目前的工作中,使用Aspen Plus®程序开发了下气流气化炉模型,该模型具有研究微藻气化性能的能力。在气化性能评价前,已成功完成了模型的验证,实验研究发现H2、CO2、CO和CH4的出口气体组成与所建立的模型非常接近。考察了蒸汽/生物质比、气化温度等主要工艺参数对合成气组分和合成气高热值(HHV)的影响。结果表明,温度的升高对合成气H2和CO的组成有较大影响,分别从50.72%增加到56.47%和28.11%增加到28.84%。模拟结果还表明,S/B比的提高有利于蒸汽相关反应的进行,提高了合成气中H2的含量。CH4的下降趋势导致合成气的HHV随温度和蒸汽的变化而降低。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
INVESTIGATION OF MICROALGAE GASIFICATION UNDER STEAM ATMOSPHERE IN DOWNDRAFT GASIFIER BY USING ASPEN PLUS®
Energy production is facing the environmental and economic issues due to growing population and uncertainties about the fossil fuels. These concerns prompt the researchers to find widely available and renewable alternative such as biomass instead of the fossil fuels. Microalgae is one of the promising biofuels owing to its rapid growth speed and higher calorific value. Steam gasification is an alternative way converting biomass to syngas with higher H2 and lower CO2 content compared with the other thermochemical conversion processes. In the present work, the downdraft gasifier model was developed by using Aspen Plus® program that has the capability to investigate the performance of microalgae gasification. Before the performance evaluation of the gasification, validation of the model successfully completed and exit gas compositions of H2, CO2, CO and CH4 were found very close for experimental study and the developed model. Effects of the main parameters of the process such as steam/biomass ratio and gasification temperature were assessed on the syngas composition and higher heating value (HHV) of syngas. The obtained results were stated that the increment in the temperature showed great effect on the H2 and CO compositions of syngas, they increased from 50.72% to 56.47% and 28.11% to 28.84% respectively. The simulation results also illustrated that the rising of the S/B ratio was favored the steam related reactions and increased the H2 content in syngas. However decreasing trend of the CH4 caused reducing of the HHV of syngas as a function of temperature and steam as well.
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