摘要
Catalyst durability is one of the major problems hindering the commercialization of partial oxidation of methane (POM) for syngas production. We report that a Pt/MgAl 2 O 4 -HS catalyst with the MgAl 2 O 4 -HS support being synthesized via hydrolysis solvothermal (HS) method demonstrates high stability for POM during a 500 h life testing at 900 °C without detectable coke formation, while a Pt/MgAl 2 O 4 -CP counterpart in which MgAl 2 O 4 was prepared by an optimized co-precipitation (CP) method exhibits continuous deactivation accompanied by coking. Using a suite of characterizations incluidng BET, H 2 chemisorption, XRD, STEM, TEM, TG/DTA and TPD of NH 3 and CO 2 , we reveal that the high catalytic durability of the Pt/MgAl 2 O 4 -HS is due to the spinel surface of MgAl 2 O 4 -HS that can efficiently stabilize Pt against sintering. The Pt/MgAl 2 O 4 -CP, however, has defect Al 2 O 3 or MgO-like species on the MgAl 2 O 4 -CP surface, inhibiting its capability to stabilize Pt. We confirm that the POM reaction undergoes a combustion-reforming pathway by monitoring the temperatures and gaseous product compositions along the catalyst bed. These results provide guidance for rational design of a longevity catalyst for POM process.
危险品化学品经营许可证(带存储)