1 |
Wigley, T. M. L., 1998, The Kyoto Protocol: , and climate implications, Geophys. Res. Lett., 25, 2285-2288.
DOI
ScienceOn
|
2 |
Yang, W. H., Kim, M. H., 2006, Catalytic reduction of by over well-characterized Pt surfaces, Korean J. Chem. Eng., 23, 908-918.
DOI
ScienceOn
|
3 |
Ruszak, M., Inger, M., Witkowski, S., Wilk, M., Kotarba, A., Sojka, Z., 2008, Selective removal from the process gas of nitric acid plants over ceramic catalyst, Catal. Lett., 126, 72-77.
DOI
|
4 |
UN, 1998, Kyoto Protocol to the United Nations framework convention on climate change, United Nations, New York, USA, 1-20.
|
5 |
van den Brink, R. W., Booneveld, S., Pels, J. R., Bakker, D. F., Verhaak, M. J. F. M., 2001, Catalytic removal of N2O in model flue gases of a nitric acid plant using a promoted Fe zeolite, Appl. Catal. B, 32, 73-81.
DOI
|
6 |
Blanco, J., Avila, P., Marzo, L., 1993, Low temperature multibed SCR process for tail gas treatment in nitric acid plant, Catal. Today, 17, 325-332.
DOI
|
7 |
EFMA, 2000, Best available technologies for pollution prevention and control in the European fertilizer industry, Booklet No. 2 of 8: Production of nitric acid, European Fertilizer Manufactures' Association, Brussels, Belgium, 1-36.
|
8 |
EPA, 2006, Industrial processes (Chapter IV), in Global mitigation of non- greenhouse gases, EPA-430- R-06-005, Washington DC, USA, 1-14.
|
9 |
EPA, 2010, Available and emerging technologies for reducing greenhouse gas emissions from the nitric acid production industry, Sector Policies and Programs Division, Office of Air Quality Planning and Standards, Research Triangle Park, NC, USA, 1-27.
|
10 |
Fareid, E., Kongshaug, G., Hjornevik, L., Nirisen, O., 1993, Method by reduction of nitrogen oxide, EP 0359286.
|
11 |
Hevia, M. A. G., Perez-Ramirez, J., 2008, Assessment of the low-temperature Envi variant for catalytic abatement over steam-activated FeZSM-5, Appl. Catal. B, 77, 248-254.
DOI
|
12 |
Ovchinnikova, E. V., Chumachenko, V. A., Piryutko, L. V., Kharitonov, A. C., Noskov, A. S., 2009, Detoxication of nitrose gases formed in the production of adipic acid: The two-stage catalytic cleaning process, Catal. Ind., 1, 76-84.
DOI
ScienceOn
|
13 |
Kim, M. H., 2008, HCCI combustion engines with ultra low and emissions and new catalytic emission control technology, J. Environ. Sci., 17, 1413-1419.
DOI
|
14 |
Kim, M. H., Ham, S. W., 2010, Determination of emissions levels in the selective reduction of by over an on-site-used commercial -/>- catalyst using a modified gas cell, Top. Catal., 53, 597-607.
DOI
ScienceOn
|
15 |
MHSPE(Ministry of Housing, Spatial Planning and the Environment), 2001, Reduction of nitrous oxide () in the nitric acid industry, Netherlands, 1-21.
|
16 |
Perez-Ramirez, J., Kapteijn, F., Mul, G., Moulijn, J. A., 2002, Highly active -resistant ex-framework FeMFI catalysts for direct decomposition, Appl. Catal. B, 35, 227-234.
DOI
ScienceOn
|
17 |
Perez-Ramirez, J., Kapteijn, F., Schoffel, K., Moulijn, J. A., 2003, Formation and Control of in nitric acid production: Where do we stand today, Appl. Catal. B, 44, 117-151.
DOI
ScienceOn
|
18 |
Glauser, J., 2011, CEH Report: Nitric Acid, Chemical Economics Handbook, SRI Consulting, Abstract (http://www.sriconsulting.com/CEH/Public/Reports/ 757.8000/).
|
19 |
IPCC, 2001, Climate change 2001: The scientific basis. Contribution of the working group I to the 3rd assessment report of the IPCC, Houghton, J. T., Ding, Y., Griggs, D. J., Noguer, M., van der Linden, P. J., Dai, X., Maskell, K., Johnson, C. A. (eds), Cambridge University Press, Cambridge, UK and New York, NY, USA, 1-881.
|
20 |
Giecko, G., Borowiecki, T., Gac, W., Kruk, J., 2008, / catalysts for the decomposition in the niric acid industry, Catal. Today, 137, 403-409.
DOI
ScienceOn
|
21 |
Kim, M. H., 2011, Emission control technologies for N2O from adipic acid production plants, J. Environ. Sci., 20, 755-765.
DOI
|