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Chemical looping combustion of a Chinese anthracite with Fe2O3-based and CuO-based oxygen carriers

机译:Fe2O3基和CuO基氧载体对无烟煤的化学循环燃烧

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Chemical looping combustion (CLC) of coal has received great attention for its verified advantage in the inherent separation of CO2 without great cost penalty. It would be meaningful to adopt anthracite as fuel for CLC application in China due to its abundant reserve in China and also a great challenge for its low reactivity. A typical Chinese anthracite as Yang Quan (YQ) coal was selected in this research as a model fuel and its reaction with both synthesized CUO/Al2O3 and Fe2O3/Al2O3 oxygen carriers (OCs) was performed in a thermo-gravimetric analyzer (TGA) to investigate the reaction peculiarities involved. Fourier transform infrared spectroscopy (FTIR) was used to in-situ detect the emitted gasses from TGA. Field scanning electron microscopy/energy-dispersive X-ray spectrometry (FSEM-EDX) was used to study the morphology and elemental compositions present in the solid residues collected from the reaction of YQ. with these two OCs, and the related phase was identified by X-ray diffraction (XRD), In order to further explore the reaction mechanisms involved, a more realistic reaction system with 426 species was designed for thermodynamic simulation. Through all these measures, two reaction stages were observed for the reaction of YQ with Fe2O3/Al2O3 or CUO/Al2O3 at 300-600 °C and 600-850 °C after dehydration, respectively. The maximum weight loss rate for YQ with CUO/Al2O3 at the second stage was pronounced enough to reach up to 2,8 wt.%/min. greatly higher than that of YQ with Fe2O3/Al2O3, The mixture conversion index for YQ with CUO/Al2O3 was far bigger than that of YQ with Fe2O3/Al2O3. which further indicated that CUO/Al2O3 was more suitable to YQ in CLC. At these two stages throughout 400 to 1100 °C, CuO and CUAl2O4 contained in CUO/Al2O3 OC were mainly reduced to Cu and Cu2O or CuAlO2 and Al2O3 by transfer of the lattice oxygen [0] involved to YQ in a sequential mode; however, above 800 °C, Cu2O and CuAlO2 were also produced through direct decomposition of CuO or CuAl2O4 by emission of gaseous oxygen O2, which was beneficial to the direct combustion of coal. During reaction of YQ with CUO/Al2O3 OC, active CuO was found to tend to react with various sulfur species produced from YQpyrolysis and formed to Cu2S, but the Al2SiO5 was formed through the interaction of Al2O3 with SiO2 in the YQ, which resulted in the loss of the inert support involved in the CUO/Al2O3 OC and further degraded its reactivity to YQ due to the lower resistance to sintering.
机译:煤的化学循环燃烧(CLC)由于其固有的CO2分离优势而被证实具有优势,而不会造成很大的成本损失,因此备受关注。由于无烟煤在中国的储量丰富,并且由于其低反应性而面临巨大挑战,因此采用无烟煤作为在中国用于CLC的燃料将是有意义的。在本研究中,选择了典型的无烟煤作为阳煤(YQ)煤作为模型燃料,并在热重分析仪(TGA)中将其与合成的CUO / Al2O3和Fe2O3 / Al2O3氧载体(OCs)进行了反应,调查涉及的反应特性。傅里叶变换红外光谱(FTIR)用于原位检测TGA排放的气体。使用场扫描电子显微镜/能量色散X射线光谱法(FSEM-EDX)研究了从YQ反应中收集的固体残留物中的形态和元素组成。用这两种OC进行反应,并通过X射线衍射(XRD)鉴定了相关的相。为了进一步探索涉及的反应机理,设计了一种更逼真的反应体系,包含426种物质,用于热力学模拟。通过所有这些措施,在脱水后,YQ与Fe2O3 / Al2O3或CUO / Al2O3分别在300-600°C和600-850°C观察到两个反应阶段。在第二阶段,使用CUO / Al2O3的YQ的最大失重率足以达到高达2.8 wt。%/ min。远高于含Fe2O3 / Al2O3的YQ,含CUO / Al2O3的YQ的混合转化指数远大于含Fe2O3 / Al2O3的YQ的混合转化指数。这进一步表明CUO / Al2O3更适合CLC中的YQ。在整个400到1100°C的这两个阶段中,CUO / Al2O3 OC中所含的CuO和CUAl2O4主要通过顺序模式将涉及的晶格氧[0]转移到YQ中而主要还原为Cu和Cu2O或CuAlO2和Al2O3。然而,在800℃以上,通过气态氧O 2的释放直接分解CuO或CuAl 2 O 4也产生了Cu 2 O和CuAlO 2,这有利于煤的直接燃烧。在YQ与CUO / Al2O3 OC反应期间,发现活性CuO倾向于与YQ热解产生的各种硫物质反应并形成Cu2S,但通过Al2O3与SiO2在YQ中的相互作用形成Al2SiO5。 CUO / Al2O3 OC中惰性载体的流失,由于对烧结的抵抗力降低,进一步降低了其对YQ的反应性。

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