Chemical looping hydrogen generation with multi-layer core-shell oxygen carrier of Fe@Al-Ti
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摘要: Fe-Al-Ti载氧体在化学链制氢工艺中具有良好的循环稳定性和抗积炭性能，但反应形成FeAl2O4会降低抗烧结性能和氢气产率。为抑制FeAl2O4的生成并进一步提升载氧体反应性能，本研究采用自组装模板燃烧法制备多层核壳结构载氧体，以TiO2为介层阻隔Fe2O3与Al2O3，形成多层核壳Fe@Al-Ti载氧体，在固定床上进行化学链制氢循环，评价多层核壳结构对反应性能的影响。结果表明，Fe@Al-Ti载氧体的介层有效阻隔Fe2O3与Al2O3的接触，抑制了FeAl2O4形成，抗烧结性能得到进一步提升。Fe@Al-Ti载氧体在化学链制氢循环实验中无明显积炭和团聚现象，制氢能力随循环次数逐渐增加，循环稳定性较好；尤其物质的量比Al∶Ti=3.5∶1的核壳载氧体的碳转化率、制氢率和储氧量最高，分别为57.4%、75.0%和6.01 mmol/gOC，比非核壳Fe-Al-Ti载氧体分别增加28.4%、30.0%、26.9%。
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关键词:
- 化学链制氢 /
- Fe2O3/TiO2/Al2O3 /
- 核壳结构 /
- 固定床
Abstract: Fe-Al-Ti oxygen carriers have good cycling stability and good properties of anti- carbon deposition in the chemical looping hydrogen generation(CLHG) process. However, the formation of FeAl2O4 reduces hydrogen yield and increases sintering. To weaken the formation of FeAl2O4 and to promote properties, the core-shell oxygen carriers of Fe@Al-Ti were prepared by self-assembly template combustion method, which took TiO2 as the inter-layer to separate Fe2O3 and Al2O3. The effect of multi-layer core-shell structure on reaction performance was evaluated on a fixed bed. The results indicated that the inter-layer of Fe@Al-Ti oxygen carriers effectively weakened the contact between Fe2O3 and Al2O3, thus reducing the formation of FeAl2O4 and improving properties of anti-sintering. The Fe@Al-Ti oxygen carriers significantly prevented carbon deposition and surface agglomeration, and had great cycling stability during the CLHG cycles. The core-shell oxygen carrier with a molar ratio of Al∶Ti=3.5∶1 got the highest carbon conversion rate and H2 yield , and oxygen storage capacity in a single cycle, with 57.4%, 75.0%, and 6.01 mmol/gOC, respectively, which are 28.4%, 30.0%, and 26.9% higher than those of non core-shell Fe-Al-Ti oxygen carriers.-
Key words:
- chemical looping hydrogen generation /
- fe2o3/tio2/al2o3 /
- core-shell /
- fixed bed
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图 2 化学链制氢固定床装置示意图
Figure 2 Schematic diagram of fixed bed for chemical looping hydrogen generation
图 3 不同载氧体20次循环下碳转化率变化
Figure 3 Carbon conversion rate of different oxygen carriers under 20 cycles
图 4 不同载氧体20次循环积炭率
Figure 4 Carbon deposition rate of different oxygen carriers in 20 cycles
图 5 不同载氧体20次循环下H2产量
Figure 5 Hydrogen yield of different oxygen carriers under 20 cycles
图 6 不同载氧体20次循环下储氧量变化
Figure 6 Oxygen Storage Capacity of different oxygen carriers under 20 cycles
图 7 不同载氧体单次循环中H2产率随时间变化趋势（第3、10、17次循环）
Figure 7 H2 yield of different oxygen carriers in a single cycle (Cycle No.3, 10 and 17)
图 8 载氧体循环前后平均粒径
Figure 8 The average grain size of oxygen carriers before and after cycles
图 10 载氧体化学链制氢循环前后XRD谱图
Figure 10 XRD images of oxygen carriers before and after cycles
表 1 载氧体制备原料及制备方法
Table 1 Materials and methods of oxygen carriers prepared in this work
Sample Preparation method Materials/g Al2O3 TiO2 Fe(NO3)3·9H2O CO(NH2)2 SATC(3.5∶1) SATC 7.00 2.00 68.18 23.25 SATC(2∶1) SATC 6.00 3.00 68.18 23.25 IM Impregnation 7.00 2.00 68.18 − Sol-gel Sol-gel 9.00 − 68.18 − 
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表 2 化学链制氢实验循环工况
Table 2 Experimental procedure in a cycle
No. Experimental stage Time/min Gas flow rate/(L·min−1) 1 CO reduction 20 CO∶0.30 N2∶1.50 2 nitrogen blowing 8 N2∶1.50 3 steam oxidization 4 N2∶1.50 H2O(l)∶0.45mL/min 4 nitrogen blowing 8 N2∶1.50 5 air oxidization 10 O2∶0.30 N2∶1.50 6 nitrogen blowing 8 N2∶1.50
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表 3 载氧体XRD物相及晶体尺寸
Table 3 XRD phase and crystallite of oxygen carrier
Crystal Form Crystallite/A Fresh After 10 Cycles After 20 Cycles SATC(3.5∶1) Fe2TiO5 − − 365.5 FeAl2O4 − − − SATC(2∶1) Fe2TiO5 − 364.7 364.7 FeAl2O4 − − 406.5 IM Fe2TiO5 370.0 366.6 363.8 FeAl2O4 − 437.4 496.5
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