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Modeling of Catalytic Coupling of Methane

Conference ·
OSTI ID:5688510
 [1];  [1];  [1];  [1]
  1. Lawrence Livermore National Laboratory (LLNL), Livermore, CA (United States)
Catalytic oxidative coupling to ethane or ethylene is an appealing, direct route to utilization of otherwise low value natural gas located in remote sites. Researchers have focused on oxidative coupling of methane for about 15 years, using metal oxide catalysts to facilitate the reaction. Despite intensive efforts, the best yields to C2 hydrocarbons have been in the 20 to 30% range, generally accomplished with catalysts which include an alkali metal on an alkali earth oxide, e.g., Li/MgO. In an attempt to understand and overcome the source of this limitation, more fundamental catalyst studies and modeling have been undertaken. Much of the recent work in oxidative coupling has explicitly recognized the fact that under most conditions, thermally-induced reactions account for a large fraction of products. In previous work, the authors employed a chemical kinetic model (HCT), developed at this Laboratory, to describe the overall homogeneous gas phase reactions of methane and oxygen. The HCT model can be used to describe reaction pathways and determine products for a wide variety of reactor types and conditions. Its application successfully predicted methane conversions and product distributions found experimentally for a reactor containing no catalyst. In this work, they expand the HCT model to include proposed catalytic reaction schemes. The purpose is to predict limits in C2 yield, describe product trends as a function of generalized catalyst behavior and use these results as a guide to catalyst design.
Research Organization:
Lawrence Livermore National Laboratory (LLNL), Livermore, CA (United States)
Sponsoring Organization:
USDOE
DOE Contract Number:
W-7405-ENG-48
OSTI ID:
5688510
Report Number(s):
UCRL-JC--107053; CONF-910402--14; ON: DE91011914
Country of Publication:
United States
Language:
English