The kinetics of hydrodearomatization (HDA) is studied in an isothermal high-throughput reactor over three catalysts (CoMo, NiMo, and NiMoW) to produce clean diesel fuel according to China’s latest emission standards....The kinetics of hydrodearomatization (HDA) is studied in an isothermal high-throughput reactor over three catalysts (CoMo, NiMo, and NiMoW) to produce clean diesel fuel according to China’s latest emission standards. The influences of reaction temperature, pressure, the ratio of H2 to oil, and space time were systematically investigated. By analyzing the reaction mechanism, a four-lump kinetic model considering the influence of competitive adsorption was proposed for the hydrodearomatization reaction, and the model parameters were optimized with good fitting. It was found that nitrogen compounds inhibited the hydrodearomatization reaction. The simulation of various catalyst stacking schemes based on the HDA kinetic model is close to the experimental data, proving the reliability of the model. The concentration of aromatic compounds of different loading sequences was predicted with the catalyst gradation model.展开更多
This work synthesized a series of Ni/CeO_(2)/Al_(2)O_(3) catalysts with varying CeO_(2) doping amounts to enhance low-temperature CO_(2) methanation.The introduction of CeO_(2) weakens the interaction between Ni and A...This work synthesized a series of Ni/CeO_(2)/Al_(2)O_(3) catalysts with varying CeO_(2) doping amounts to enhance low-temperature CO_(2) methanation.The introduction of CeO_(2) weakens the interaction between Ni and Al_(2)O_(3),leading to the formation of Ni-CeO_(2) active sites.This results in a high dispersion of Ni and CeO_(2),improved catalyst reducibility,increased number of active sites,and enhanced the CO_(2) methanation.This work further investigated the impact of WHSV and catalyst stacking configuration to enhance the reaction.When the catalyst is stacked into three segments with a temperature gradient of 330℃,300℃,and 250℃under WHSV=9000 ml·h^(-1)·g^(-1),the CO_(2) conversion significantly increases to 95%,which is remarkably close to the thermodynamic equilibrium(96%).展开更多
基金Funding from the National Key R&D Program of China (2017YFB0306601)
文摘The kinetics of hydrodearomatization (HDA) is studied in an isothermal high-throughput reactor over three catalysts (CoMo, NiMo, and NiMoW) to produce clean diesel fuel according to China’s latest emission standards. The influences of reaction temperature, pressure, the ratio of H2 to oil, and space time were systematically investigated. By analyzing the reaction mechanism, a four-lump kinetic model considering the influence of competitive adsorption was proposed for the hydrodearomatization reaction, and the model parameters were optimized with good fitting. It was found that nitrogen compounds inhibited the hydrodearomatization reaction. The simulation of various catalyst stacking schemes based on the HDA kinetic model is close to the experimental data, proving the reliability of the model. The concentration of aromatic compounds of different loading sequences was predicted with the catalyst gradation model.
基金financial support of the National Natural Science Foundation of China(22178265)Tianjin Science and Technology Project(21JCYBJC00400)Open Project for Ningbo Key Laboratory of Green Petrochemical Carbon Emission Reduction Technology and Equipment(ZITJU2023-ZYDK001).
文摘This work synthesized a series of Ni/CeO_(2)/Al_(2)O_(3) catalysts with varying CeO_(2) doping amounts to enhance low-temperature CO_(2) methanation.The introduction of CeO_(2) weakens the interaction between Ni and Al_(2)O_(3),leading to the formation of Ni-CeO_(2) active sites.This results in a high dispersion of Ni and CeO_(2),improved catalyst reducibility,increased number of active sites,and enhanced the CO_(2) methanation.This work further investigated the impact of WHSV and catalyst stacking configuration to enhance the reaction.When the catalyst is stacked into three segments with a temperature gradient of 330℃,300℃,and 250℃under WHSV=9000 ml·h^(-1)·g^(-1),the CO_(2) conversion significantly increases to 95%,which is remarkably close to the thermodynamic equilibrium(96%).
