Abstract
The selective catalytic reduction (SCR) of NOx using NH3 was studied at pressures up to 5 bar over a vanadium-based SCR catalyst (~1 wt% V2O5 and 10 wt% WO3/TiO2), relevant for the installation of SCR reactors upstream of the turbocharger at marine engines. Experiments were performed using both granulated catalyst in a lab-scale fixed-bed reactor and a monolith catalyst in a bench-scale setup. The residence time across the catalytic bed was kept constant, by increasing the (normalized (0 °C, 1 atm)) volumetric flow rate proportionally to the pressure. The results show that for the granulated catalyst, the NOx conversion was independent of the pressure, indicating that the SCR kinetics are not affected by the increased pressure up to 5 bar. NH3 temperature-programmed desorption experiments showed that the catalyst NH3 adsorption increased with more than 30% when the pressure was increased from 1 bar to 4.5 bar. On the other hand, when the adsorption temperature was increased from 150 to 300 °C, the adsorption capacity decreased by approximately 60% independent on the pressure. The SCR reaction was unaffected by the increased NH3 uptake caused by the increased pressure, because only a certain fraction of the sites (\( {\theta}_{N{H}_3}^{\ast } \) = 0.14) was found to be active in the SCR reaction, and these are filled up at lower NH3 partial pressure than the total number of sites. Experiments using a monolithic catalyst showed that at temperatures above 250 °C, the NOx conversion was lower at an increased pressure (3.1 bar) when the residence time was held constant. This decrease was ascribed to increased internal and external diffusion limitations at the elevated pressure.
Similar content being viewed by others
Abbreviations
- ABS:
-
Ammonium bisulfate
- ANR:
-
Ammonia to NOx ratio
- AS:
-
Ammonium sulfate
- CPSI:
-
Channels per square inch
- CSTR:
-
Continuous stirred tank reactor
- EGR:
-
Exhaust gas recirculation
- IMO:
-
International maritime organization
- LNG:
-
Liquid natural gas
- NECA:
-
NOx emission control area
- NOx :
-
Nitrogen oxides, the sum of NO and NO2
- PBR:
-
Packed bed reactor
- RSS:
-
Residual sum of squares
- SCR:
-
Selective catalytic reduction
- SECA:
-
SOx emission control area
- SOx :
-
Sulfur oxides, the sum of SO2, SO3, and H2SO4
- V-SCR:
-
Vanadium-based SCR catalyst
- α :
-
Temkin kinetics parameter [−]
- C NH3 :
-
NH3 concentration [mol/m3]
- d particle :
-
Catalyst particle diameter [m]
- D reactor :
-
Reactor tube diameter [m]
- D AB :
-
Binary diffusion coefficient [m/s2]
- d h :
-
Hydraulic diameter [m]
- ε :
-
Porosity [−]
- E a :
-
Activation energy of the adsorption process of NH3 [J/mol]
- \( {E}_d^0 \) :
-
Activation energy for the desorption process of NH3 [J/mol]
- f :
-
Friction factor [−]
- G z :
-
Graetz dimensional number [−]
- k NO :
-
NO first order rate constant [1/s]
- k′NO :
-
Mass based NO first order rate constant [m3/s/kg]
- \( {k}_a^0 \) :
-
Pre-exponential factor of the adsorption process of NH3 [m3/mol/s]
- \( {k}_d^0 \) :
-
Pre-exponential factor for the desorption process of NH3 [1/s]
- \( {K}_{{\mathrm{NH}}_3} \) :
-
NH3 adsorption equilibrium constant [m3/mol]
- k(T ref):
-
Reaction rate constant calculate at the temperature Tref
- L :
-
Length of catalyst [m]
- Ω’:
-
NH3 adsorption capacity (mol/m3 particles)
- \( \varOmega ={\varOmega}^{\prime}\cdot \frac{1-\varepsilon }{\varepsilon } \) :
-
NH3 adsorption capacity (mol/m3 reactor)
- P reactor :
-
Reactor pressure [Pa]
- Q 0 :
-
Volumetric flow rate (normal (0 °C, 1 atm)) [Nm3/s]
- r a :
-
Rate of adsorption of NH3 [1/s]
- r d :
-
Rate of desorption of NH3 [1/s]
- Re:
-
Reynolds dimensional number [−]
- ρ :
-
Density of catalyst [kg/m3]
- r NO :
-
Rate of NO disappearance [1/s]
- S c :
-
Schmidts dimensional number [−]
- Sh:
-
Sherwood dimensional number [−]
- Sh∞ :
-
Asymptotic Sherwood number [−]
- θ :
-
Surface coverage of NH3 [−]
- \( {\theta}_{{\mathrm{NH}}_3}^{\ast } \) :
-
Fraction of active sites in the SCR reaction [−]
- θ v :
-
Surface coverage of vanadium [−]
- U :
-
Linear velocity [m/s]
- V :
-
Volume [m3]
- v 0 :
-
volumetric flow rate [m3/s]
- W :
-
Weight of catalyst [kg]
- y meas :
-
Vectors containing the measured gas phase mole fraction [ppm]
- y model :
-
Vectors containing the modeled gas phase mole fraction [ppm]
- z :
-
Axial coordinate [m]
- Z*:
-
Dimensionless axial coordinate [−]
References
Hallquist, Å.M., Fridell, E., Westerlund, J., Hallquist, M.: Onboard measurements of nanoparticles from a SCR-equipped marine diesel engine. Environ. Sci. Technol. 47(2), 773–780 (2013). https://doi.org/10.1021/es302712a
Man Diesel & Turbo, Exhaust gas emission control today and tomorrow. http://marine.man.eu/docs/librariesprovider6/technical-papers/exhaust-gas-emission-control-today-and-tomorrow.pdf?sfvrsn=22 (accessed September 10, 2015).
Lamas, M.I., Rodríguez, C.G.: Emissions from marine engines and NOx reduction methods. J. Marit. Res. 9, 77–81 (2012)
Briggs, J., Mccarney, J.: Field Experience of Marine SCR. CIMAC Congr (2013)
Niki, Y. Hirata, K. Kishi, T. Inaba, T. Takagi, M. Fukuda, T. Nagai, T. Muraoka, E.: SCR System for NOx reduction of medium speed marine diesel engine, in: CIMAC Congress, Vol. 22 p. 12 (2010)
G. Lövblad, E. Fridell, Experiences from use of some techniques to reduce emissions from ships, Göteborg. http://cleantech.cnss.no/wp-content/uploads/2011/09/2006-Lovblad-and-Fridell-Experiences-from-use-of-some-techniques-to-reduce-emissions-from-ships.pdf. (2006). Accessed 16 Dec 2015
Magnusson, M., Fridell, E., Ingelsten, H.H.: The influence of sulfur dioxide and water on the performance of a marine SCR catalyst. Appl. Catal. B Environ. 111–112, 20–26 (2012). https://doi.org/10.1016/j.apcatb.2011.09.010
Österman, C., Magnusson, M.: A systemic review of shipboard SCR installations in practice. WMU J. Marit. Aff. 12(1), 63–85 (2013). https://doi.org/10.1007/s13437-012-0034-1
Lehtoranta, K., Vesala, H., Koponen, P., Korhonen, S.: Selective catalytic reduction operation with heavy fuel oil: NOx , NH3, and particle emissions. Environ. Sci. & Technol. 49(7), 4735–4741 (2015). https://doi.org/10.1021/es506185x
Det Norske Veritas (DNV), Marpol 73/78 Annex VI, (2009). http://hulpinnood.nl/wp-content/uploads/2015/03/BIJLAGE3_Marpol-annex-VI.pdf (accessed May 9, 2016)
IMO, The 2020 Global Sulfur Limit. http://www.imo.org/en/MediaCentre/HotTopics/GHG/Documents/FAQ_2020_English.pdf (accessed October 12, 2017)
IMO, Emission Control Areas designated under MARPOL Annex VI, (2018). http://www.imo.org/en/OurWork/Environment/PollutionPrevention/AirPollution/Pages/Emission-Control-Areas-(ECAs)-designated-under-regulation-13-of-MARPOL-Annex-VI-(NOx-emission-control).aspx (accessed January 12, 2019)
Mollenhauer, K., Tschöke, H.: Handbook of Diesel Engines. Springer Berlin Heidelberg, Berlin (2010). https://doi.org/10.1007/978-3-540-89083-6
Turns, S.R.: An introduction to combustion: concepts and applications. New York, NY: McGraw-Hill (2012)
Forzatti, P., Lietti, L.: Recent advances in DeNOxing catalysis for stationary applications. Heterog. Chem. Rev. 3(1), 33–51 (1996)
Koebel, M., Elsener, M., Madia, G.: Recent advances in the development of urea-SCR for automotive applications. Sae Tech. Pap. (2001). https://doi.org/10.4271/2001-01-3625
P. Blakeman, K. Arnby, P. Marsh, C. Newman, G. Smedler, Optimization of an SCR catalyst system to meet EUIV heavy duty diesel legislation, SAE Tech. Pap. 2 (2008). https://doi.org/10.4271/2008-01-1542
Guan, B., Zhan, R., Lin, H., Huang, Z.: Review of state of the art technologies of selective catalytic reduction of NOx from diesel engine exhaust. Appl. Therm. Eng. 66(1-2), 395–414 (2014). https://doi.org/10.1016/j.applthermaleng.2014.02.021
Kröcher, O.: Aspects of catalyst development for mobile urea-SCR systems—from Vanadia-Titania catalysts to metal-exchanged zeolites. Stud. Surf. Sci. Catal. 171, 261-289 (2007) https://doi.org/10.1016/S0167-2991(07)80210-2.
Man Diesel & Turbo, Tier III Two-Stroke Technology, (2012). http://marine.man.eu/docs/librariesprovider6/technical-papers/tier-iii-two-stroke-technology.pdf?sfvrsn=12 (accessed September 10, 2015)
IMO, IMO MEPC 66/6/15, (2014). http://www.worldshipping.org/industry-issues/environment/air-emissions/MEPC_66-6-15_-_Comments_concerning_potential_amendments_to_the_effective___.pdf (accessed November 20, 2017).
H. Bosch, F. Janssen, Preface, Catal. Today. 2 v. https://doi.org/10.1016/0920-5861(88)80001-4 (1988)
G. Centi, S. Perathoner: Chapter 1 introduction: state of the art in the development of catalytic processes for the selective catalytic reduction of NOx into N2. in: Stud. Surf. Sci. Catal., pp. 1–23. https://doi.org/10.1016/S0167-2991(07)80202-3. 2007
Gabrielsson, P., Pedersen, H.G.: Flue gas from stationary sources. In: Ertl, G., Knözinger, H., Schüth, F., Weitkamp, J. (eds.) Handb. Heterog. Catal, pp. 2345–2385. Wiley-VCH (2008) http://findit.dtu.dk/en/catalog/2342172429 (accessed March 29, 2017)
I. Nova, E. Tronconi: Urea-SCR Technology for deNOx After Treatment of Diesel Exhausts, Springer. https://doi.org/10.1007/978-1-4899-8071-7 (2014)
Marine Fuels 2020. https://www.marinefuels2020.com/marine-fuels/background/ (accessed April 6, 2019).
CIMAC Working Group 8, CIMAC Guideline: Cold Corrosion in Marine Two Stroke, CIMAC Guidel. (2017) 1–36. https://cimac.com/cms/upload/Publication_Press/WG_Publications/CIMAC_WG8_Guideline_2017_Two_Stroke_Engine_Cold_Corrosion.pdf. Accessed 27 June 2018
Orsenigo, C., Beretta, A., Forzatti, P., Svachula, J., Tronconi, E., Bregani, F., Baldacci, A.: Theoretical and experimental study of the interaction between NOx reduction and SO2 oxidation over DeNOx-SCR catalysts. Catal. Today. 27(1-2), 15–21 (1996). https://doi.org/10.1016/0920-5861(95)00168-9
Tronconi, E., Cavanna, A., Orsenigo, C., Forzatti, P.: Transient kinetics of SO2 oxidation over SCR-DeNOx monolith catalysts. Ind. Eng. Chem. Res. 38(7), 2593–2598 (1999). https://doi.org/10.1021/ie980673e.
Muzio, L., Bogseth, S., Himes, R., Chien, Y.-C., Dunn-Rankin, D.: Ammonium bisulfate formation and reduced load SCR operation. Fuel. 206, 180–189 (2017). https://doi.org/10.1016/j.fuel.2017.05.081
J.M. Burke, K.L. Johnson: Ammonium sulfate and bisulfate formation in air preheaters (project summary). http://nepis.epa.gov/Exe/ZyPURL.cgi?Dockey=2000TU1N.txt.1982. Accessed 21 Sept 2015
Matsuda, S., Kamo, T., Kato, A., Nakajima, F., Kumura, T., Kuroda, H.: Deposition of ammonium bisulfate in the selective catalytic reduction of nitrogen oxides with ammonia. Ind. Eng. Chem. Prod. Res. Dev. 21(1), 48–52 (1982). https://doi.org/10.1021/i300005a009
T. Fujibayashi, S. Baba, H. Tanaka: Development of Marine SCR System for Large Two-Stroke Diesel Engines Complying with IMO NOx Tier III. in: CIMAC Congr. (2013)
R. Bank, B. Buchholz, H. Harndorf, R. Rabe, U. Etzien: High-Pressure SCR at Large Diesel Engines for Reliable NOx - Reduction and Compliance with IMO Tier III Standards, in: CIMAC Congr. 2013
Kröcher, O., Elsener, M., Bothien, M.-R., Dölling, W.: Pre-Turbo SCR - influence of pressure on NOx reduction. MTZ Worldw. 75(4), 46–51 (2014). https://doi.org/10.1007/s38313-014-0140-x
Rammelt, T., Torkashvand, B., Hauck, C., Böhm, J., Gläser, R., Deutschmann, O.: Nitric oxide reduction of heavy-duty diesel off-gas by NH3-SCR in front of the turbocharger. Emiss. Control Sci. Technol. 3(4), 275–288 (2017). https://doi.org/10.1007/s40825-017-0078-y
K. Sandelin, D. Peitz: SCR under pressure - pre-turbocharger NOx abatement for marine 2-stroke diesel engines, in: CIMAC Congr. (2016)
Schüttenhelm, W., Günther, C., Jürgens, R.: High pressure SCR for large two-stroke engines and comparison to conventional SCR high dust applications. VGB Powertech. 8, 58–62 (2017)
Bird, R.B., Stewart, W.E., Lightfoot, E.N.: Transport phenomena. J. Wiley pp. xii, 905 s (2007)
Christensen, S.R., Hansen, B.B., Johansen, K., Pedersen, K.H., Thøgersen, J.R., Jensen, A.D.: SO2 oxidation across marine V2O5-WO3-TiO2 SCR catalysts: a study at elevated pressure for preturbine SCR configuration. Emiss. Control Sci. Technol. 4(4), 289–299 (2018). https://doi.org/10.1007/s40825-018-0092-8
Koebel, M., Madia, G., Elsener, M.: Selective catalytic reduction of NO and NO2 at low temperatures. Catal. Today. 73(3-4), 239–247 (2002). https://doi.org/10.1016/S0920-5861(02)00006-8
Tronconi, E., Forzatti, P., Gomez Martin, J.P., Mallogi, S.: Selective catalytic removal of NOx: a mathematical model for design of catalyst and reactor. Chem. Eng. Sci. 47(9-11), 2401–2406 (1992). https://doi.org/10.1016/0009-2509(92)87067-Z
Nova, I., Lietti, L., Beretta, A., Forzatti, P.: Study of the sintering of a deNOx commercial catalyst. Stud. Surf. Sci. Catal. 139, 149–156 (2001). https://doi.org/10.1016/S0167-2991(01)80192-0
Dumesic, J.A., Topsøe, N.-Y., Topsøe, H., Chen, Y., Slabiak, T.: Kinetics of selective catalytic reduction of nitric oxide by Ammonia over Vanadia/Titania. J. Catal. 163(2), 409–417 (1996). https://doi.org/10.1006/jcat.1996.0342
Tsukahara, H., Ishida, T., Mayumi, M.: Gas-phase oxidation of nitric oxide: chemical kinetics and rate constant. Nitric Oxide. 3(3), 191–198 (1999). https://doi.org/10.1006/niox.1999.0232
Lietti, L., Nova, I., Camurri, S., Tronconi, E., Forzatti, P.: Dynamics of the SCR-DeNOx reaction by the transient-response method. AICHE J. 43(10), 2559–2570 (1997). https://doi.org/10.1002/aic.690431017
Levenspiel, O.: The chemical reactor omnibook, Distributed by OSU Book Stores, (1989)
Pushnov, A.S.: Calculation of average bed porosity. Chem. Pet. Eng. 42(1-2), 14–17 (2006). https://doi.org/10.1007/s10556-006-0045-x
Rawlings, J.B., Ekerdt, J.G.: Chemical reactor analysis and design fundamentals, 2. Edition, Madison, Wis.: Nob Hill Pub (2002)
Forzatti, P., Nova, I., Beretta, A.: Catalytic properties in deNOx and SO2–SO3 reactions. Catal. Today. 56(4), 431–441 (2000). https://doi.org/10.1016/S0920-5861(99)00302-8
Beeckman, J.W., Hegedus, L.L.: Design of monolith catalysts for power plant NOx emission control. Ind. Eng. Chem. Res. 30(5), 969–978 (1991). https://doi.org/10.1021/ie00053a020
J.A. Dumesic, N.-Y. Topsoe, T. Slabiak, P. Morsing, B.S. Clausen, E. Törqvist, H. Topsoe: Microiunetic analysis of the selective catalytic reduction (SCR) of nitric oxide over Vanadia/Titania-based Catalysts, in. pp. 1325–1337. https://doi.org/10.1016/S0167-2991(08)64454-7 (1993)
Olsen, B.K., Castellino, F., Jensen, A.D.: Modeling deactivation of catalysts for selective catalytic reduction of NOx by KCl aerosols. Ind. Eng. Chem. Res. 56(45), 13020–13033 (2017). https://doi.org/10.1021/acs.iecr.7b01239.
Koebel, M., Elsener, M.: Selective catalytic reduction of NO over commercial DeNOx catalysts: comparison of the measured and calculated performance. Ind. Eng. Chem. Res. 37(2), 327–335 (1998). https://doi.org/10.1021/ie970569h.
Tronconi, E., Forzatti, P.: Adequacy of lumped parameter models for SCR reactors with monolith structure. AICHE J. 38(2), 201–210 (1992). https://doi.org/10.1002/aic.690380205
Shah, R.K., London, A.L.: Laminar flow forced convection in ducts. New York: Academic Press (1978)
Tratz, H., Grigull, U.: Thermischer Einlauf in Ausgebildeter Laminarer Rohrströmung. Int. J. Heat Mass Transf. 8, 669–678 (1965)
Clement, K.H. Fangel, P. Jensen, A.D. Thomsen, K.: Kemiske enhedsoperationer, Polyteknisk Forlag. (2004)
Acknowledgments
This work is part of the Danish societal partnership, Blue INNOship, and partly funded by the Innovation Fund Denmark (IFD) under File No: 155-2014-10 and the Danish Maritime Fund. The authors gratefully acknowledge the funding support.
Author information
Authors and Affiliations
Corresponding author
Ethics declarations
The authors declare that they have no competing interests.
Additional information
Publisher’s Note
Springer Nature remains neutral with regard to jurisdictional claims in published maps and institutional affiliations.
Electronic Supplementary Material
ESM 1
(DOCX 4763 kb)
Rights and permissions
About this article
Cite this article
Christensen, S.R., Hansen, B.B., Pedersen, K.H. et al. Selective Catalytic Reduction of NOx over V2O5-WO3-TiO2 SCR Catalysts—A Study at Elevated Pressure for Maritime Pre-turbine SCR Configuration. Emiss. Control Sci. Technol. 5, 263–278 (2019). https://doi.org/10.1007/s40825-019-00127-0
Received:
Revised:
Accepted:
Published:
Issue Date:
DOI: https://doi.org/10.1007/s40825-019-00127-0