Numerical Simulation of an Industrial Fluid Catalytic Cracking Regenerator
- Purdue Univ. Calumet, Hammond, IN (United States). Center for Innovation Through Visualization (CIVS)
- BP Refining and Logistics Technology, Naperville, IL (United States)
Fluid catalytic cracking (FCC) is one of the most important conversion processes in petroleum refineries, and the FCC regenerator is a key part of an FCC unit utilized in the recovery of solid catalyst reactivity by burning off the deposited coke on the catalyst surface. Furthermore, a three-dimensional multiphase, multispecies reacting flow computational fluid dynamics (CFD) model was established to simulate the flow and reactions inside an FCC regenerator. The Euler–Euler approach, where the two phases (gas and solid) are considered to be continuous and fully interpenetrating, is employed. The model includes gas–solid momentum exchange, gas–solid heat exchange, gas–solid mass exchange, and chemical reactions. Chemical reactions incorporated into the model simulate the combustion of coke which is present on the catalyst surface. We validated the simulation results using plant data.
- Research Organization:
- Purdue Univ. Calumet, Hammond, IN (United States). Center for Innovation Through Visualization (CIVS)
- Sponsoring Organization:
- USDOE National Nuclear Security Administration (NNSA)
- DOE Contract Number:
- NA0000741
- OSTI ID:
- 1344400
- Journal Information:
- Journal of Thermal Science and Engineering Applications, Vol. 7, Issue 2; ISSN 1948-5085
- Publisher:
- ASME
- Country of Publication:
- United States
- Language:
- English
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