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    太阳能驱动熔融盐耦合Ni/Ce基催化剂热解微藻制氢

    Solar-driven pyrolysis of microalgae in molten salt with Ni/Ce-based catalyst for hydrogen production

    • 摘要: 太阳能驱动微藻在熔融氢氧盐中热解是极具潜力的制氢技术,但仍面临热解气体产物中甲烷、C2—C5及焦油含量较高的挑战。为实现清洁高效制氢,提出太阳能驱动熔融盐耦合Ni/Ce基催化剂高效热解微藻制氢技术。首先探究了熔融NaOH-Na2CO3体系下,4种不同Ni/Ce基催化剂对微藻热解特性的影响,发现Ni-ZrO2催化剂中ZrO2的碱性位点促进了水蒸气的吸附,同时Ni基催化剂促进了C—H键的断裂。两者的协同作用促进了挥发分C—H键断裂和氧的吸附迁移,对小分子烃类和焦油的重整转化率最高。一方面,Ni/ZrO2在Ni的负载量为10%时有最优的催化性能,而随着Ni的负载量进一步升高,Ni金属颗粒团聚导致催化性能下降。另一方面,Ni/ZrO2与原料质量比为1时,催化剂对焦油重整效果最好,催化剂过量会增加其床层高度,阻碍挥发分在催化剂内部的扩散,从而降低挥发分整体重整效果。相较于无催化剂时,新技术在最优工况下的甲烷和C2—C5产率分别降低50%和31%,焦油中芳香烃含量下降至0.020 mmol/g,从而实现氢气产率提升26%,最高达93 mmol/g。太阳能驱动熔融盐Ni基催化剂热解微藻制氢,可有效促进甲烷和焦油的水蒸气重整反应,同时实现氢气产率大幅提升与产物品质显著改善,为太阳能−生物质协同转化提供了新路径。

       

      Abstract: Solar-driven pyrolysis of microalgae in molten hydroxides is a promising technology for hydrogen production, yet it faces challenges due to the high content of methane, C2—C5 hydrocarbons, and tar in the gas products. To achieve clean and efficient hydrogen production, this study proposes a solar-driven pyrolysis in molten salt coupled with Ni/Ce-based catalysts of microalgae to produce hydrogen. First, the effects of four different Ni/Ce-based catalysts on microalgae pyrolysis characteristics were investigated in a molten NaOH-Na2CO3 system. It was observed that the basic sites present on the ZrO2 support within the Ni-ZrO2 catalyst facilitated the adsorption of water vapor, whereas the Ni component effectively promoted the scission of C—H bonds. The results showed that the synergistic action of the Ni and ZrO2 catalyst promote C—H bond cleavage in volatiles and oxygen adsorption and migration, achieving the highest conversion rates for small hydrocarbons and tar reforming. On the one hand, optimal catalytic performance was achieved with Ni/ZrO2 at a Ni loading of 10%. Further increasing Ni loading led to decreased catalytic activity due to Ni particle agglomeration. On the other hand, the catalyst exhibited the best tar reforming performance at a catalyst-to-feedstock mass ratio of 1. Excessively high catalyst-to-feedstock ratios increased bed pressure drop and reduced volatile reforming efficiency. Compared with no catalyst, the aromatic hydrocarbon content in the tar was reduced to 0.020 mmol/g, corresponding to a 26% increase in hydrogen yield, which reached a maximum of 93 mmol/g. This solar-driven pyrolysis of microalgae in molten salt with the Ni-based catalyst effectively promotes the steam reforming of methane and tar, simultaneously achieving a marked enhancement in hydrogen yield and product quality. Thus, it provides a new pathway for the synergistic conversion of solar energy and biomass.

       

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