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Kinetic parameter estimation of a commercial Fe-zeolite SCR

  • Tae Joong Wang
  • , Seung Wook Baek
  • , Hyuk Jae Kwon
  • , Young Jin Kim
  • , In Sik Nam
  • , Moon Soon Cha
  • , Gwon Koo Yeo
  • Korea Advanced Institute of Science and Technology
  • Doosan Infracore Co., Ltd.
  • Pohang University of Science and Technology
  • Samsung
  • ORDEG Corporation
  • Hyundai-Kia Motors

Research output: Contribution to journalArticlepeer-review

54 Scopus citations

Abstract

In this work, an in-house computational code capable of simulating highly coupled physicochemical phenomena occurring in ammonia/urea SCR (selective catalytic reduction) was developed. On the basis of this computational code, the kinetic parameters of catalytic reactions were newly calibrated using the experimental results obtained over a commercial ammonia/urea SCR washcoated Fe-ion-exchanged zeolite-based catalyst. Powder-phase NH3 TPD (temperature-programmed desorption) experiments were performed to calibrate the kinetic parameters of NH3 adsorption and desorption, and core-out monolith experiments were conducted to estimate the kinetic parameters of various deNOx reactions as well as NH3 oxidation. The currently established SCR model and kinetic parameters gave a good prediction for both steady-state and transient experimental results for a wide range of operating conditions. The main objectives of this study were to develop numerical tools and their implementation methodologies that can be cost-effectively applied to the design and development of real-world ammonia/urea SCR systems. Details of the procedures and techniques in numerical modeling and kinetic parameter calibration are described step-by-step in this article.

Original languageEnglish
Pages (from-to)2850-2864
Number of pages15
JournalIndustrial and Engineering Chemistry Research
Volume50
Issue number5
DOIs
StatePublished - 2 Mar 2011

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