Printer Friendly

Fundamentals of Heterogeneous Catalysis: a Study of N2O Mitigation Reaction Over Modified Zeolite Catalysts.

Byline: Naseer A. Khan and Naveed ul Hasan Syed

Keywords: Nitrous oxide (N2O), Reaction catalysis, Zeolite supports.


Chemical industrial emissions, fuel combustions, and spraying chemicals on agriculture fields are few main reasons behind the environmental degradation [1]. Few years back, world health organization (WHO) gathered data from different parts of the world and reported thousands of deaths because of air pollution [2]. Only 2 AdegC rise in earth surface temperature may result in the extinction of millions of living species, can initiate cyclones, activate volcanoes, and earthquakes [3]. For this reason, world leaders (Kyoto summit, 1997) agreed to enforce the emissions control regulations for six greenhouse gases, i.e. carbon dioxide (CO2), nitrous oxide (N2O), methane (CH4), sulfur hexafluoride (SF6), hydrofluorocarbons (HFCs), and perflurocarbons (PFCs) [4].

N2O is a potent greenhouse gas, whereas its atmospheric concentration in pre-industrial age remained constant between the values of 270 - 288 ppbv [5]. However, now a days fertilizers, chemicals, fuel combustion (both stationary and mobile stations), and sewerage treatment reactions are releasing 7 million tons of N2O annually into the environment [6]. N2O in the troposphere is non-reactive molecule, however, its presence in the stratosphere layer (12 km - 50 km, from the earth surface) actively absorbs infrared radiation, and is more hazardous gas when compared to other greenhouse gases [7, 8]. N2O global warming potential (GWP) is 15 and 310 times of CH4 and CO2, respectively [9]. Moreover, the photolysis of N2O leads to the production of stratospheric NOx, a molecule active in ozone (O3) depletion reactions [10-12].

The presence of O3 layer is essential for the absorption of lethal high frequency radiations [13]. The probable mechanism of N2O/NOx and O3 conversion reactions are still under experimental discussions [10, 12].

Nitric acid and adipic acid production plants are the main chemical industries responsible for the N2O emissions [5,11,12]. Luckily, the mitigation of most of the greenhouse gases is possible when reacted over suitable solid catalyst. For example, N2O can be converted in N2 and O2 under favorable reaction conditions. Till date, a number of solid catalysts were found active for N2O conversion reactions. This review paper encompasses a brief overview of heterogeneous catalysis, zeolites materials, and N2O conversion reactions.

Introduction to reaction catalysis

In 1836, the term "catalysis" was used by a Swedish chemist, Jons Jakob Berzelius (1779 - 1848). Whereas, Ostwald was the first scientist who used the word catalyst in 1885. According to Ostwald a catalyst is primarily used to increases the rate of a reaction [14]. However, dealing with reaction catalysis is not new, i.e. for the past 1000 years, different enzymes were commonly used in numerous fermentation reactions. All reactants have to overcome an energy barrier before conversion into product species. The catalyst lowers the energy barrier and provide a new route for the conversion reaction [14]. Ideally, reactants chemically interact with the catalyst and then convert into product species as presented in Fig. 1. Theoretically, the catalyst composition should remain the same, but in real reactions the molecular chemistry of catalyst changes because of reactants and catalyst interactions [14].

Moreover, catalysts can be classified on the basis of phases (solid, liquid, or gas), chemical composition, and the state of reactants/products collection (homogeneous and heterogeneous). For example, as shown in the following homogeneous reactions, both catalysts and reactants are in the same phase, i.e. nitric oxide (NO) is a gas phase catalyst for the conversion of molecular oxygen into ozone (O3) gas.

1/2 O2(g) +###NO(g)###NO2(g)



Whereas in heterogeneous catalytic reactions, reactants and catalysts are in a different phase. For example, in the Fischer-Tropsch reaction, carbon monoxide reacts with hydrogen over cobalt (solid phase) catalyst and forms gasoline.

8 CO(g) + 17 H2(g) a C8H18(l) + 8 H2O(l)

This solid phase catalyst is a combination of active sites and less active catalyst support [14]. Most of the industrial metal catalysts are actually loaded metal sites over less active metal oxide supports. Silica, alumina, activated carbon, and zeolites are few of the commonly used catalyst supports. These supports have high surface area (~200 m2/g) and maintains the surface area even at extreme high reaction temperatures (> 600 AdegC). The reactant species hooks up to active metal sites and forms transition species and finally converts into reaction products. The stability (performance) of catalysts usually decreases with time (during the progress of reaction) and at higher temperatures [15].

Any modifications of catalyst surface alter the yield of reaction products. For example, acid or steam treatment of H-ZSM-5 causes dealumination, whereas alkaline treatment removes the silica content of the H-ZSM-5 framework, and both these supports when loaded with same metal have different selectivity for several hydrocarbon oxidation reactions [16]. For example, in CH4 and N2O oxidation reaction, Bitter and co-workers treated H-ZSM-5 by stirring it in a solution of NaOH and observed an improvement in methanol selectivity in comparison to formaldehyde [16-18].

Pellet size and shape of catalysts used for any reaction is dependent on the scale of reactor. Few commonly used shapes and sizes are shown in Fig. 2. The powder form is generally used for small scale laboratory reactors (micro reactors). For medium and large scale reactors, which may hold several tons of catalyst, the powdered catalyst is compressed under pressure to form large pallets. In some cases the shape of catalyst is also important in order to minimize the pressure drop across the catalyst bed [16].

Last but not least, a good catalyst should have a high surface area for maximum reactants interactions, however, it is also true that in some cases the external surface area of catalyst is intentionally decreased in order to increase the selectivity towards desired reaction products. Catalyst can be prepared by different methods, such as ion exchange, impregnation, slurry precipitation, co-precipitation, fusion, physical mixing, and wash coating. For most reactions, the catalyst having the same composition when prepared by different methods have different activity and selectivity [15]. For example, Co-ZSM-5 prepared by ion exchange and impregnation methods have different activity for N2O conversion reactions [19-21].

Zeolite, a catalyst support

Zeolites are microporous aluminosilicate sieves and because of structural aluminum its framework contains negative charge sites. The first natural zeolite (stilbite) was discovered in 1756 by a Swedish mineralogist named Axel Fredrick Cronstedt (1722-1765). The term Zeolite is derived from two Greek words, i.e. boiling stone [22]. Moreover, chabazites, mordenite, and clinoptildite are few common natural zeolites [23]. The melting of zeolites occurs at very high (>1000 Adeg C) temperatures [22]. These minerals contains a network of cages and more importantly have the ability to trap ions, atoms, and molecules [23]. Usually water, alkali, and alkaline earth metals ions are part of zeolite framework, whereas, these bonded ions can be replaceable with other cations [22]. Zeolites have a number of commercial applications, for example, these are used as a catalyst, water softeners (removing magnesium and calcium ions), in concrete mixture, and for gas separations.

Natural zeolites contains several undesired chemical impurities and therefore usually not suitable for catalytic reactions [24]. Later on scientists synthetically prepared several zeolites with enhance catalytic properties having unique framework structures. For example, faujasites (zeolites X and Y) synthesized in 1962 is now commonly used for the catalytic cracking of heavy petroleum distillates [24]. There are several other industrial reactions, such as synthesis of ethylbenzene, and isomerization of xylene etc., where synthetic zeolites have improved the reaction selectivity [25].

The framework of zeolite is a three dimensional network of alumina (AlO4) and silica (SiO4). These adjacent tetrahedra are connected via common oxygen atoms forming macromolecular structures [24]. These materials are microporous with size range from 0.2 to 1 nm [24]. The net formulae of the tetrahedra is SiO2 and AlO2A-, i.e. one negative charge resides in each tetrahedron containing aluminum [24]. These negative sites may compensate numerous equivalent cations. The topology of zeolite is described by a three letter code, for example ZSM-5, a specific MFI structure. The ratio of Si to Al determines the cation exchange capacity [24].

H-ZSM-5 (Zeolite Socony Mobil-5), a synthetic zeolite, have gained an extensive importance in heterogeneous catalysis [26, 27]. In 1972, Argauer and Landolt synthesized this material, and Mobil Oil Company filed the patented in 1975 [27]. Alumina, silica, alkali metal oxide, water, and tetraalkylammonium compounds are hydrothermally treated under high pressure to form H-ZSM-5 zeolites [28].These frame work can compensate several cations at exchange sites [28]. H-ZSM-5 is highly microporous and contains perpendicular intersections with zig-zag patterns [29]. These channels are formed by a 10 membered oxygen rings as shown in Figure 3[29]. The unit cell structure is orthorhombic, while the crystallographic unit cell has 96 T sites (alumina or silica), 192 oxygen sites, and a fixed number of compensating cations (depends on Si/Al ratio) [30].

Furthermore, transition metals cations can be loaded on H-ZSM-5 via different routes, such as volatile metal organic complex is decomposed over H-ZSM-5 surface [22], or metal cations are used as precursor salts (direct synthesis) [31], or by incipient or solution impregnation [32], and ion exchange method may also be used for cation loadings [33, 34]. Cobalt containing H-ZSM-5 support has shown excellent catalytic activity and selectivity for various reactions [21, 35]. Isolated cobalt ions are usually characterized as active sites [36], whereas during cobalt loading clusters may also be formed [37]. Different species of cobalt, i.e. Co2+, Co3+, and Co0 have been reported as an active sites for the reactions [20].

Nitrous Oxide conversion reactions

The emissions of N2O into the atmosphere is comparatively low when compared with other greenhouse gases [6]. However, N2O molecule remains stable in stratosphere (2nd layer of the atmosphere) for approximately 150 years, and thus have a higher global warming potential with reference to CO2 and CH4 [38]. These nitrogen oxide molecules affectively absorbs infrared radiations and may reacts with ozone (O3) under favorable reaction conditions [7, 39, 40]. The concentration of N2O remained constant for centuries (the value was approximately 270 ppbv), however, the current numbers are very high (presently around 310 ppbv) [40, 41].

N2O production from point sources, for example, chemical plants (adipic and nitric acids production plants), fuel combustion, and sewage treatment plants are the main emission sources where catalytic emission control systems can be installed. The commencement of new emission reduction projects have already been started as reported in the recent United Nations meeting [42]. For comparison, the current size of emissions from different sources is given in Table 1 [42].

Table 1. Global nitrous oxide (N2O) emissions.

Source###N2O emissions (Mt N2O y-1)




Atmospheric chemistry.###0.2


Agriculture (including fertilizer).###3.5

Nitric acid production.###0.4

Adipic acid production###<0.1

Fossil fuel combustion (stationary)###0.2 - 0.5

Fossil fuel combustion (mobile)###0.4 - 0.9

Biomass combustion###1.0

Sewage treatment###1.5

Total of all sources###Approximately 20

Number of different catalysts, such as M-zeolites (M = Co, Fe, Cu etc.) [35], perovskite-like mixed oxides [43], and precious metal (Pd, Rh, etc.) supported catalysts were found active for the N2O conversion reaction [44]. Few possible N2O (N2O a N2 + 1/2O2) dissociation routes discussed in the literature are:


###N2O###+###*(O)###a###N2###+###(O) * (O)

###(O) * (O)###a###O2###+###*###see[45]

(b)###2N2O###+###*###a###2N2###+###(O) * (O)

###(O) * (O)###a###O2###+###*###See[46]





Where the symbol * is used to represent the active site of the catalyst.

Moreover, the selective catalytic reduction (SCR) with different hydrocarbons (CH4, C2H6, C2H4, C2H2, C3H8, and C3H4), CO, NOx, and NH3 are currently applied for reducing N2O emissions [48]. The Uhde's EnviNOxA(r) is commercially employed catalyst for N2O conversion reaction (Fe-ZSM-5). The literature also reports that the catalytic activity of Fe-ZSM-5 decreases in presence of H2O moisture [5, 49]. Few studied also suggests that Co-ZSM5 are more active than Fe-ZSM5 for N2O dissociation reaction [35]. The activity of reaction changes when same cobalt metal was loaded on different supports [50, 51].


Viable strategies to reduce the emissions of greenhouse gases is highly active research area. The presence of N2O in higher altitudes of atmosphere is more hazardous when compared to other greenhouse gases. A number of catalysts have been studied to convert N2O molecules into cleaner gaseous products. Presently the knowledge of reaction catalysis is well documented, however, the current review only focuses on the relevant concepts of heterogeneous catalysis. For example, the progress of reaction under same reaction condition may change when the physicochemical properties of catalyst are varied. Zeolite minerals, particularly H-ZSM-5 has several practical application including as an active catalyst support for N2O reduction reactions.


1. A. M. Liaquat, A. M. Kalam, H. H. Masjuki, and M. H. Jayed, Atmospheric Environment, 44 (2010) 3869.

2. E. Stone, J. Schauer, T. A. Quraishi and A. Mahmood, Atmospheric Environment, 44 (2010) 1062.

3. S. H. Shuit, K. T. Tan, K. T. Lee and A. H. Kamaruddin, Energy, 34 (2009) 1225.

4. Kyoto Protocol to the United Nations Framework Convention on Climate Change, Kyoto, Japan., (1997), pp. Annex A.

5. J. Perez-Ramirez, J. Kapteijn, F. Schoffel, K., and J. A. Moulijn, Applied Catalysis B: Environmental, 44 (2003) 117.

6. S. J. Lee, I. S. Ryu, B. M. Kim and S. H. Moon, International J. Greenhouse Gas Control, 5 (2011) 167.

7. L. Donner and V. Ramanathan, J. Atmospheric Scie., 37 (1980) 119.;2

8. C. N. Hewitt and W. T. Sturges, Springer Netherlands 2013. CAAAQBAJ

9. M. N. Debbagh, C. S. M. D. Lecea and J. Perez-Ramirez, Applied Catalysis B: Environmental, 70 (2007) 335.

10. J. C. Kramlich and W. P. Linak, Nitrous oxide behavior in the atmosphere, and in combustion and industrial systems, Progress in Energy and Combustion Science, 20 (1994) 149.

11. R. Muller, Royal Soci. Chem., (2012).

12. National Research Council. Climatic Impact Committee, National Academy of Sciences (1975).

13. R. W. Portmann, J. S. Daniel and A. R. Ravishankara, Stratospheric ozone depletion due to nitrous oxide: influences of other gases, Philosophical Transactions of the Royal Society B: Biological Sciences, 367 (2012) 1256. https://doi: 10.1098/rstb.2011.0377

14. J. Hagen, Industrial Catalysis: A Practical Approach, Wiley (2015). gAAQBAJ

15. M. Bowker, The basis and application of hetrogeneous catalysis. Edition en anglais, Oxford University Press, Incorporated (1998). gAACAAJ

16. N. V. Beznis, N. V. van Laak, V. A. N. C, B. M. Weckhuysen, B. M. and J. H. Bitter, Microporous and Mesoporous Materials, 138 (2011) 176.

17. R. Giudici, R. H. W. Kouwenhoven and R. Prins, Applied Catalysis A: General, 203 (2000) 101.

18. S. V. Donk, A. H. Janssen, Bitter, J. H. K. P. and de Jong, Catalysis Reviews, 45 (2003) 297.

19. X. Wang, H. Y. Chen and W. M. H. Sachtler, Applied Catalysis B: Environmental, 26 (2000) 227.

20. P. J. Smeets, Q. Meng, Corthals, Leeman, S. H. and R. A. Schoonheydt, Applied Catalysis B: Environmental, 84 (2008) 505.

21. Q. Shen, L. Li, C. He, X. Zhang, Z. Hao and Z. Xu, Asia-Pacific J. Chem. Engineering, 7 (2012) 502. https://doi:10.1002/apj.599

22. P. A. Jacobs, E. M. Flanigen, J. C. Jansen, and H. V. Bekkum, Introduction to Zeolite Science and Practice, Elsevier Science (2001).

23. S. M. Auerbach, K. A. Carrado and P. K. Dutta, Handbook of Zeolite Science and Technology, Taylor and Francis (2003). vAEACAAJ

24. J. Weitkamp, Zeolites and Catalysis, 131 (2000) 175.

25. J. E. Naber, K. P. de Jong, W. H. J. Stork and H. P. C. E. Kuipers. Post, Industrial applications of zeolite catalysis, Studies in Surface Science and Catalysis, Elsevier1994, 2197.

26. D. H. Olson, G. T. Kokotailo, S. L. Lawton and W. M. Meier, 85 (1981) 2238.

27. G. T. Kokotailo, S. L. Lawton, D. H. Olson, and W. M. Meier, Nature, 272 (1978) 437.

28. A. V. Kucherov and A. A. Slinkin, Zeolites, 7 (1987) 43.

29. Xu, R. Pang, W. Yu, J. Huo, Q. and J. Chen, Chemistry of Zeolites and Related Porous Materials. 2007. https://doi:10.1002/9780470822371.ch2

30. D. G. Hay, H. Jaeger and G. W. West, The Journal of Physical Chemistry, 89 (1985) 1070.

31. Z. Zhang, S. L. Suib, Y. D. Zhang, W. A. Hines and J. I. Budnick, J. American Chemical Society, 110 (1988) 5569. https://doi:10.1021/ja00224a051

32. A. G. Dhere, R. J. D. Angelis, P. J. Reucroft and J. Bentley, J. Molecular Catalysis, 20 (1983) 301.

33. M. D. Amiridis, T. Zhang and R. J. Farrauto, Applied Catalysis B: Environmental, 10 (1996) 203.

34. H. G. Karge, H. K. Beyer and G. Borbely, Catalysis Today, 3 (1988) 41.

35. Y. Li and J. N. Armor, Applied Catalysis B: Environmental, 1 (1992) 21.

36. A. Jentys, A. Lugstein and H. Vinek, J. Chemical Society, Faraday Transactions, 93 (1997) 4091.

37. J. M. Stencel, V. U. S. Rao, J. R. Diehl, K. H. Rhee, A. G. Dhere and R. J. DeAngelis, J. Catalysis, 84 (1983) 109.

38. J. H. Huang and S. L. Suib, Methane dimerization via microwave plasmas, Research on Chemical Intermediates, 20 (1994) 133.

39. V. Ramanathan, R. J. Cicerone, H. B. Singh and J. T. Kiehl, J. Geophysical Res. Atmospheres, 90 (1985) 5547.

40. M. Kavanaugh, Atmospheric Environment, (1967), 21 (1987) 463.

41. L. S. Kalkstein, J. S. Greene, An evaluation of climate/mortality relationships in large U.S. cities and the possible impacts of a climate change, Environmental Health Perspectives, 105 (1997) 84.

42. F. Kapteijn, J. Rodriguez-Mirasol and J. A. Moulijn, Applied Catalysis B: Environmental, 9 (1996) 25.

43. M. A. Pena and J. L. G. Fierro, Chemical Structures and Performance of Perovskite Oxides, Chemical Reviews, 101 (2001) 1981.

44. Yuzaki, K. Yarimizu, T. K. Aoyagi, S. I. Ito and K. Kunimori, Catalysis Today, 45 (1998) 129.

45. E. V. Kondratenko and J. Perez-Ramirez, J. Physical Chem. B, 110 (2006) 22586.

46. G. D. Pirngruber, M. Luechinger, P. K. Roy, A. Cecchetto and P. Smirniotis, J. Catalysis, 224 (2004) 429.

47. A. Heyden, B. Peters, A. T. Bell and F. J. Keil, J. Physical Chem. B, 109 (2005) 1857.

48. M. Rivallan, G. Ricchiardi, S. Bordiga and A. Zecchina, J. Catalysis, 264 (2009) 104.

49. A. Heyden, N. Hansen, A. T. Bell and F. J. Keil, J. Physical Chem. B, 110 (2006) 17096.

50. N. A. Khan, E. M. Kennedy, B. Z. Dlugogorski, A. A. Adesina and M. Stockenhuber, Australian J. Chem., 70 (2017) 1138.

51. Y. Haibiao, W. Xinping and Y. Li, Catalysis today, 339 (2020) 274.
COPYRIGHT 2019 Knowledge Bylanes
No portion of this article can be reproduced without the express written permission from the copyright holder.
Copyright 2019 Gale, Cengage Learning. All rights reserved.

Article Details
Printer friendly Cite/link Email Feedback
Author:Naseer A. Khan and Naveed ul Hasan Syed
Publication:Pakistan Journal of Analytical and Environmental Chemistry
Geographic Code:9JAPA
Date:Dec 31, 2019
Previous Article:Assessment of Heavy Metals in Vegetables, Sewage and Soil, Grown Near Babu Sabu Toll Plaza Lahore, Pakistan.
Next Article:Appraisal of Trace Element Accumulation and Human Health Risk from Consuming Field Mustard (Brassica campestris Linn.) Grown on Soil Irrigated with...

Terms of use | Privacy policy | Copyright © 2020 Farlex, Inc. | Feedback | For webmasters