(66b) CFD Simulation of an Industrial High-Efficiency FCC Regenerator
AIChE Spring Meeting and Global Congress on Process Safety
2016
2016 AIChE Spring Meeting and 12th Global Congress on Process Safety
19th Topical Conference on Refinery Processing
Advances in Plant Simulation and Design I
Tuesday, April 12, 2016 - 8:30am to 9:00am
A three-dimensional simulation of the gas-particle flow behavior, heat transfer, and coke combustion inside commercial high-efficiency FCC regenerator that includes a combustor and a regenerator vessel was carried out. The simulation has several goals: to evaluate the behavior under present conditions of operation, identify and propose solutions to operating troubles. The kinetic for coke combustion was simulated in MATLAB to understand its performance. The CFD simulation based on the Eulerian-Eulerian model for coke combustion was conducted using a commercial CFD package Fluent 15.0, that uses the finite volume method to solve the partial differential equations of continuity, momentum, energy and species transport by discretizing the equations over finite volumes. The Phase Coupled SIMPLE algorithm was used to adjust the pressure and velocities after each iteration when solve the gas-solid momentum equations. For simulate the combustor, a CFD simulation of the gas distributor was needed in order to define boundary conditions of the gas inlet for the combustor. The results obtained of the CFD simulation of the combustor shows lower concertation of the solid particles in this zone of the regenerator. Homogeneous mixture between solid particle and gas in the regeneration process is critical since most of the catalyst in the bed has very little coke on it, about 1 %w. At the same time, the CO content in the flue gases is high due inefficient mix between the air and the particles. Afterburning results when the CO content in the flue gases mix with the high oxygen content gases in the regenerator vessel. Afterburning causes thermal deactivation of the catalyst FCC and damage on cyclons due to hot spots. To correct these problems, different designs of the spent catalyst distributor was evaluated. The results obtained with the new designs of the distributor showed decreased of the afterburning phenomenon in the regenerator vessel.
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2016 AIChE Spring Meeting and 12th Global Congress on Process Safety
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