Dergiler / Turkish Journal of Chemistry / 2018 / Cilt: 42 - Sayı: 6

Experimental and theoretical study of NH3 adsorption and desorption over a Cu-chabazite NH3 -SCR catalyst

Sayfa
1768–1780
Yayın Tarihi
2022-11-01
DOI
—
🏛️Bu makalenin bibliyografik verileri ve tam metin bağlantısı DergiPark üzerinden sağlanmıştır.
DergiPark Kaydı ↗
✨

Yapay Zeka Hızlı Bakış & Çıkarımlar

AI Insight
⚡ TL;DR(1 Cümlede Hızlı Çıkarım)

The three-site model, which uses site density values obtained using dry adsorption ofNH3 , best represented the experimental data.

📌 3 Maddede Bu Makale

🎯
Amaç & Hipotez:NH3 adsorption and desorption behavior of a commercial Cu-chabazite (CHA) NH3 selective catalyticreduction (NH3 -SCR) catalyst was studied in the presence and absence of H2 O.
📊
Temel Bulgular & Veri:NH3 uptake values at various adsorptiontemperatures were obtained during various steps of the adsorption and temperature-programmed desorption (TPD)experiments.
💡
Sonuç & Katkı:The three-site model, which uses site density values obtained using dry adsorption ofNH3 , best represented the experimental data.
🔬Tür:Modelleme & Sayısal Simülasyon
📍Kapsam:Genişletilmiş Akademik Örneklem
⚙️Değişkenler:Alan Parametreleri

Abstract

NH3 adsorption and desorption behavior of a commercial Cu-chabazite (CHA) NH3 selective catalyticreduction (NH3 -SCR) catalyst was studied in the presence and absence of H2 O. NH3 uptake values at various adsorptiontemperatures were obtained during various steps of the adsorption and temperature-programmed desorption (TPD)experiments. Total NH3 uptake decreased from 4.6 to 1.6 g NH3 /L catalyst when the adsorption temperature wasincreased from 50 to 300 ◦ C. Three major adsorption sites for NH3 adsorption could be identified and quantified usingTPD experiments, namely loosely, moderately, and strongly bound NH3 with peak centers at around 147, 266, and 447◦ C. The total NH3 uptake was significantly affected by the presence of H2 O in the feed. This resulted in a significantuptake loss (nearly 60%) for the loosely bound NH3 . Three single-site and one three-site model were developed andcompared in terms of NH3 uptake and release. The effects of site density values and thermodynamic restrictions inone-site models were investigated. The model using site density values obtained during the TPD phase resulted in thebest fit among one-site models. The three-site model, which uses site density values obtained using dry adsorption ofNH3 , best represented the experimental data.

🔖

Bu Makaleye Atıf Yap

ŞİMŞEK, M., DEMİR, O., YILDIZ, D. Ş., BOZBAĞ, S. E., ERKEY, C., ÖZENER, H. B., HİSAR, G. (2022). Experimental and theoretical study of NH3 adsorption and desorption over a Cu-chabazite NH3 -SCR catalyst. Turkish Journal of Chemistry, Cilt: 42 - Sayı: 6, 1768–1780. https://ajindex.com/articles/601746

📄 Tam Metin PDF Okuyucu

📄

PDF görüntüleyici hazırlanıyor...

Kaynakça (19)

  1. Kwak, J. H.; Tonkyn, R. G.; Kim, D. H.; Szanyi, J.; Peden, C. H. F. J. Catal. 2010, 275, 187-190
  2. Kwak, J. H.; Tran, D.; Burton, S. D.; Szanyi, J.; Lee, J. H.; Peden, C. H. F. J. Catal. 2012, 287, 203-209
  3. Gao, F.; Kwak, J. H.; Szanyi, J.; Peden, C. H. F. Top. Catal. 2013, 56, 1441-1459
  4. Brandenberger, S.; Krocher, O.; Tissler, A.; Althoff, R. Catal. Rev. 2008, 50, 492-531
  5. Colombo, M.; Nova, I.; Tronconi, E. Catal. Today 2012, 197, 243-255
  6. Janssens, T. V. W.; Falsig, H.; Lundegaard, L. F.; Vennestrom, P. N. R.; Rasmussen, S. B.; Moses, P. G.; Giordanino, F.; Borfecchia, E.; Lomachenko, K. A.; Lamberti, C. et al. ACS Catal. 2015, 5, 2832-2845
  7. Chatterjee, D.; Burkhardt, T.; Bandl-Konrad, B.; Braun, T.; Tronconi, E.; Nova, I.; Ciardelli, C. SAE Technical Paper Series 2005-01-965; SAE International: Warrendale, PA, USA, 2005,
  8. Chatterjee, D.; Burkhardt, T.; Weibel, M.; Nova, I.; Grossale, A.; Tronconi, E. SAE Technical Paper Series 2007- 01-1136; SAE International: Warrendale, PA, USA, 2007,
  9. Olsson, L.; Sjovall, H.; Blint, R. J. Appl. Catal. B-Environ. 2008, 81, 203-217
  10. Olsson, L.; Wijayanti, K.; Leistner, K.; Kumar, A.; Joshi, S. Y.; Kamasamudram, K.; Currier, N. W.; Yezerets, A. Appl. Catal. B-Environ. 2015, 174, 212-224
  11. Supriyanto; Wijayanti, K.; Kumar, A.; Joshi, S.; Kamasamudram, K.; Currier, N. W.; Yezerets, A.; Olsson, L. Appl. Catal. B-Environ. 2015, 163, 382-392
  12. Sjovall, H.; Blint, R. J.; Olsson, L. Appl. Catal. B-Environ. 2009, 92, 138-153
  13. Bates, S. A.; Verma, A. A.; Paolucci, C.; Parekh, A. A.; Anggara, T.; Yezerets, A.; Schneider, W. F.; Miller, J. T.; Delgass, W. N.; Ribeiro, F. H. J. Catal. 2014, 312, 87-97
  14. Woertink, J. S.; Smeets, P. J.; Groothaert, M. H.; Vance, M. A.; Sels, B. F.; Schoonheydt, R. A.; Solomon, E. I. P. Natl. Acad. Sci. USA 2009, 106, 18908-18913
  15. Groothaert, M. H.; Lievens, K.; van Bokhoven, J. A.; Battiston, A. A.; Weckhuysen, B. M.; Pierloot, K.; Schoonheydt, R. A. ChemPhysChem 2003, 4, 626-630
  16. Groothaert, M. H.; van Bokhoven, J. A.; Battiston, A. A.; Weckhuysen, B. M.; Schoonheydt, R. A. J. Am. Chem. Soc. 2003, 125, 7629-7640
  17. Wang, D.; Zhang, L.; Li, J. H.; Kamasamudram, K.; Epling, W. S. Catal. Today 2014, 231, 64-74
  18. Paolucci, C.; Verma, A. A.; Bates, S. A.; Kispersky, V. F.; Miller, J. T.; Gounder, R.; Delgass, W. N.; Ribeiro, F. H.; Schneider, W. F. Angew. Chem. Int. Edit. 2014, 53, 11828-11833
  19. Giordanino, F.; Borfecchia, E.; Lomachenko, K. A.