Fate of ilmenite as oxygen carrier during 1 MWth chemical looping gasification of biogenic residues

Paul Dieringer , Falko Marx , Florian Lebendig , Michael Müller , Andrea Di Giuliano , Katia Gallucci , Jochen Ströhle , Bernd Epple
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Abstract

Chemical looping gasification (CLG) is a novel gasification technology, allowing for the efficient conversion of different solid feedstocks (e.g. biogenic residues) into a high-calorific syngas. As in any chemical looping technology, the oxygen carrier (OC), transporting heat and oxygen from the air to the fuel reactor, is crucial in attaining high process efficiencies. To investigate the fate of the OC during CLG in an industrial environment, ilmenite samples, collected during >400 hours of chemical operation in 1 MWth scale using three different biomass feedstocks, were analyzed using different lab techniques. In doing so, changes in OC particle morphology and composition induced by CLG operation were determined. Moreover, the most important physical and chemical characteristics of the utilized OC were measured. The ensuing dataset allowed for an in-depth evaluation of the CLG technology in semi-industrial scale in terms of OC lifetime and durability. It was found that in the absence of agglomeration, the cycled OC exhibits an oxygen transport capacity of 2.6 wt.-%, a particle density of 3400 kg/m3 and particle diameters between 60 and 250 µm in steady-state conditions. Moreover, it was found that OC loss via particle attrition determines the lifetime of the OC inside the 1 MWth CLG system. On the other hand, feedstock-related agglomeration, observed during CLG operation with wheat straw, was shown to impede OC circulation between AR and FR and thus prevent efficient CLG operation. In summary, the present study thus not only highlights that generally long-term CLG operation in industry-like conditions is feasible, but also provides important insights into measures to improve OC lifetime and durability inside an industrial chemical looping system, such as an optimization of cyclone efficiency or tailored pre-treatment of the utilized feedstock.

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钛铁矿作为载氧体在生物渣化学环气化过程中的命运
化学循环气化(CLG)是一种新型的气化技术,可以将不同的固体原料(如生物残留物)有效地转化为高热量的合成气。与任何化学环技术一样,氧载体(OC)将热量和氧气从空气输送到燃料反应堆,对于实现高工艺效率至关重要。为了研究工业环境CLG过程中OC的命运,使用三种不同的生物质原料,在1兆瓦规模的化学操作中收集了400小时的钛铁矿样品,并使用不同的实验室技术进行了分析。在此过程中,测定了CLG操作引起的OC颗粒形态和组成的变化。此外,还测定了利用OC最重要的物理和化学特性。随后的数据集允许对CLG技术在半工业规模下的OC寿命和耐久性进行深入评估。结果表明,在无团聚的情况下,循环OC的稳态输氧能力为2.6 wt.-%,颗粒密度为3400 kg/m3,粒径在60 ~ 250µm之间。此外,还发现颗粒磨损造成的OC损失决定了1 mth CLG体系中OC的寿命。另一方面,在麦秸CLG操作过程中观察到的与原料相关的团聚现象,表明阻碍了AR和FR之间的OC循环,从而阻碍了CLG的有效运行。综上所述,本研究不仅强调了CLG在类似工业条件下的长期运行是可行的,而且还为提高工业化学环系统内OC寿命和耐久性的措施提供了重要见解,例如优化旋风器效率或对所用原料进行定制预处理。
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