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Hydrogen Production via the Oxy-Steam Reforming of LNG or Methane on Ni Catalysts

机译:通过LNG或甲烷对Ni催化剂的氧蒸汽重整氢气产生

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摘要

Ni catalysts supported on ZrO2, 5%CeO2-ZrO2, and 5%La2O3-ZrO2 were prepared via the impregnation method and tested in the oxy-steam reforming of methane and liquified natural gas (LNG). All tested catalysts exhibited high catalytic activity in the studied process at 700 and 900 °C. The improvement of the stability of Ni catalysts after the addition of CeO2 oxide in the studied oxy-steam reforming of LNG process was confirmed. In addition, high activity and selectivity towards hydrogen was proven in the oxy-steam reforming process at 900 °C over a 20%Ni/5%CeO2-ZrO2 catalyst. It was also proved that the addition of CeO2 onto a ZrO2 carrier leads to a decrease in the NiO and metallic Ni crystallite sizes that were detected by the X-Ray diffraction (XRD) technique. The solid solution formation between NiO and ZrO2 and/or NiO and CeO2 was proved. Superior reactivity in the oxy-steam reforming of CH4 and the LNG process exhibited a 20%Ni/ZrO2 catalyst, which showed the highest methane conversions at 500 and 600 °C, equal to 63% and 89%, respectively. In addition, also in the case of the LNG reforming reaction, the most active catalyst was the 20%Ni/ZrO2 system, which demonstrated 46.3% and 76.9% of the methane conversion value at 500 and 600 °C and the total conversion of others hydrocarbons (ethane, propane and butane). In addition, this catalytic system exhibited the highest selectivity towards hydrogen formation in the oxy-steam reforming of the LNG reaction equal to 71.2% and 71.3% at 500 and 600 °C, respectively. The highest activity of this system can be explained by the uniform distributions of Ni species and their highest concentration compared to the rest of the monometallic Ni catalysts. Time-of-flight secondary ion mass spectrometry (ToF-SIMS) results also confirmed a strong interaction of NiO with ZrO2 in the case of the 20%Ni/ZrO2 catalysts. The presence of selected NiZrO+ ions emitted from the investigated surface of the 20%Ni/ZrO2 system was detected.
机译:担载Ni催化剂上的ZrO 2,5%的CeO 2-ZrO 2和通过浸渍法制备5%镧-ZrO 2和在氧 - 蒸汽甲烷和液化天然气(LNG)的重整试验。所有测试催化剂在700和900℃下在研究过程中表现出高催化活性。证实了在研究LNG过程中加入CEO2氧化物后Ni催化剂的稳定性的改善。此外,在900℃的氧 - 蒸汽重整过程中经过900℃,在20%Ni / 5%CeO 2-ZrO 2催化剂中被证明在氢气中的高活性和选择性。还证实,在ZrO2载体上加入CeO 2导致通过X射线衍射(XRD)技术检测的NiO和金属Ni微晶尺寸的降低。证明了NiO和ZrO2和/或NiO和CeO2之间的固溶体形成。 CH4的氧蒸汽重整中的优异反应性和LNG工艺表现出20%Ni / ZrO 2催化剂,其显示为500和600℃的最高甲烷转化,分别等于63%和89%。此外,在LNG重整反应的情况下,最活性催化剂是20%Ni / ZrO2系统,其展示了500和600℃的甲烷转化值的46.3%和76.9%,以及其他的总转化碳氢化合物(乙烷,丙烷和丁烷)。此外,该催化系统在LNG反应的氧 - 蒸汽重整中致氢形成的最高选择性分别等于500和600℃的71.2%和71.3%。该系统的最高活性可以通过与其余的单金属Ni催化剂相比,Ni种类的均匀分布及其最高浓度来解释。飞行时间二次离子质谱(TOF-SIMS)结果也证实了NIO与ZrO2的强烈相互作用在20%Ni / ZrO 2催化剂的情况下。检测到从研究的20%Ni / ZrO2系统的研究表面发出的所选Nizro +离子的存在。

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