2020 Virtual AIChE Annual Meeting
(213h) Olefins Plant Optimization using SFT Technology in cracking furnaces
Author
They present $6.2 million per year losses in ethylene revenues and up to $70 million per year in OPEX costs. A computational fluid dynamics model (CFD) was adopted to capture the main flow properties of the swirl flow tube. The economic evaluation was performed using Aspen Process Economic Analyzer, considering CAPEX and OPEX estimates, comparing âstraightâ tubes (original design) vs. SFT-M and SFT-H. The simulation results confirm the considerable potential for the application of SFT technology. Incorporating SFT-M (âthe best alternativeâ) would reduce $0,6 per ton of ethylene in utility costs and 17.5% in operational and maintenance costs compared to âstraightâ tubes. It guarantees operational continuity, increases ethylene production of up to 13.5%, reduces OPEX by $0.6 per ton of ethylene, and rises furnace run length of up to 80 days because of reducing coke formation, without affecting mechanical integrity of coils. The SFT-M CAPEX contemplates $577,823.00, which would be retrieved in olefins production in a period no longer than six months.
Index Termsâ: Pyrolysis furnaces, tubular reactor, reactor modeling, olefins production, Swirl Flow Tube