543688 Catalyst Development for Autothermal Adiabatic Operation of Oxidative Coupling of Methane

Tuesday, June 4, 2019: 5:12 PM
Texas Ballroom A (Grand Hyatt San Antonio)
Wugeng Liang1, Luanyi Li1, Hector Perez1, Sarsani Sagar1, Tian Gu1, David West1 and Balakotaiah Vemuri2, (1)Corporate Research & Development, SABIC, Sugar Land, TX, (2)Department of Chemical and Biomolecular Engineering, University of Houston, Houston, TX

Due to the exothermic nature of oxidative coupling of methane (OCM) reaction, conventional fixed bed reactors are not economically feasible for the process. Based on our analysis, the feasible reactor design will be the autothermal adiabatic reactor with feed temperature near ambient temperature. For reactor to operate in this mode, there are special requirements from the catalyst.

High activity is required so that the near ambient temperature operation can be carried out. The catalyst selectivity is always very important for the reaction. In addition, under the adiabatic operation, there will be a temperature rise in the reactor, therefore, it requires the catalyst to have high selectivity across this temperature range, not only at a narrow temperature range; that is, it requires of high selectivity in a broad temperature range. Last, the catalyst should also have good stability.

Catalyst development were based on OCM reaction mechanism. Oxides which have high methyl radical formation rates are used to enhance catalyst activity. On the other hand, oxides which have low methyl radical stick coefficients are used to enhance catalyst selectivity. Special crystal structure is designed to enhance product diffusion, which will benefit catalyst selectivity. The stability of the catalyst comes from the thermal stability of oxides used under the reaction conditions.

New catalysts system developed demonstrated stable performances which meet or beat the requirement for autothermal, near ambient and adiabatic operation.


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