breaking the hydrocarbon cascade...

Breaking the Hydrocarbon Cascade in Electric Process Heating: Strategies for Upgrading Fuel Gas Streams

In this work, we use plasma-catalysis to convert leftover methane (CH₄) and carbon dioxide (CO₂) in industrial flue gases (e.g., Fischer-Tropsch) into valuable fuels like methanol (MeOH). This approach tackles greenhouse gas emissions from fossil fuel heating while utilizing waste streams.

Summary of Research Outcomes

  1. Energy yield: Currently 2.5 μg methanol/J but projected to reach 25 μg methanol /J with process optimization, surpassing conventional methods while achieving zero CO2 emissions.

  2. Catalyst deactivation: A major challenge overcome by introducing H2 as a co-reactant, preventing oxidation and improving methanol selectivity from 8% to 24%, ~ 300% increase at ambient conditions.

  3. Catalyst optimization: Tuning catalyst properties enhanced selectivity; copper exhibits 10 times higher performance than nickel.

  4. Reaction mechanism: DRIFTS analysis reveals that copper facilitates CH3O* formation, a key precursor to methanol, through dissociative adsorption of CO2 and CH4.

Summary of Project Impacts

  1. Electrified conversion: Converts unused fuel gas to valuable products at near ambient conditions.

  2. Tunable selectivity: Achieves high selectivity for liquid fuels by adjusting plasma, gas phase, and catalyst properties.

  3. Enhanced efficiency: Adding co-reactants improves selectivity to ~24% and increases overall efficiency

Principle Investigators


Dr. Michael Baldea

Dr. Thomas Underwood

Dr. C. Buddie Mullins

Team Members


Varanasi Sai Subhankar

Zachary Feng

Charan R Nallapareddy

Jiefeng Diao

Caroline C Leung

Graeme Henkelman

Project Publications

Controlling Catalytic Reaction Pathways with Plasma-activated Co-reactants for Selective Liquid Fuel Extraction

Varanasi Sai Subhankar, C. Buddie Mullins, Thomas C Underwood, and Michael Baldea