(417h) Thermocatalytic Fluidized Bed Co-Pyrolysis of Methane and Plastic Waste into Hydrogen and Carbon Nanotubes over a Multi-Metallic Catalyst
AIChE Annual Meeting
2020
2020 Virtual AIChE Annual Meeting
Fuels and Petrochemicals Division
Fuel Processing for Hydrogen Production
Wednesday, November 18, 2020 - 9:15am to 9:30am
In this context, decomposition of methane and plastics in a fixed bed, as well as fluidized bed reactor (FBR), were investigated. The catalyst used for the process is nickel-based copper-zinc promoted and alumina supported granular powder. By optimizing the concentration of promoters (i.e. copper and zinc), a specific metal crystal size range is obtained which ultimately lead to the high selectivity of the specific form of carbon i.e. carbon nanotubes (CNT). In the current work, the temperature is optimized for maximum hydrogen yield from methane and waste plastics. As the carbon is continuously depositing on the catalyst, the fluidized bed reactor is chosen for the reaction to accommodate spent catalyst regeneration and CNT separation. One of the challenges of the process is maintaining proper hydrodynamic condition in the fluidized bed reactor. The produced carbon is in the form of CNTs which is a valuable by-product which can help in improving the economy of the process. As waste plastic is a major source of carbon, its addition increases the yield of CNTs. At optimum reaction conditions, 75% methane conversion was observed along with the complete conversion of plastics to CNTs and Hydrogen. The obtained CNTs are multi-layered bamboo-shaped carbon nanotubes (Diameter: ~60 nm, Length: 2 microns).