Large Volume Inorganic Chemicals - Ammonia ... - ammk-rks.net

Chapter 3PlantTypeN 2 O emission levelkg/tonneppmBaseline N 2 Okg/tonne 100 %HNO 3RemarkYARA , AmbèsYARA, MontoirYARA, PardiesM/M 2.0 325 Implemented from May 2002 to June 2003. Achieved with 50 % catalyst fillingM/M 3.3 5357Implemented from January 2004 to March 2006. Achieved with 40 % catalystfillingM/H 2.8 4455.2Implemented in August 2003, 25 % catalyst fillingM/H 0.8 130Implemented in Augut 2005, new catalyst, 75 % fillingM/MBASF, LudwigshafenL/MImplemented in 1999. The DeN 2 O catalyst was removed in 2002 because ofcapacity loss. Now under developmentBASF, Antwerp SZ2 M/H 1.8 2856.7Implemented in 2005/2006, 12 cm catalyst filling, new catalystBASF, Antwerp SZ3 M/H 1.7 272Implemented in 2005/2006, 12 cm catalyst filling, new catalystLovochemie KD6 M/M 5.5 890 Achieved with Heraeus catalystGrande Paroisse, Rouen M/H 1.9 300Ube Industries,YamaguchiAchieved with Heraeus catalyst in combination with an improved oxidationcatalyst (FTCplus)BASF catalyst, 2001F&C Ltd, Israel H/H YARA catalyst, in planningNCIC Ltd, China M/? BASF catalyst, in planningNFL Ltd, India M/? BASF catalyst, in planningSasolHeraeus catalyst, in planningTable 3.12: Example plants applying catalytic N 2 O decomposition in the oxidation reactor[87, infoMil, 2001, 106, Yara, 2006, 109, Lenoir, 2006, 110, F&C, 2005, 111, NCIC, 2004, 113, Sasol, 2006, 154, TWG on LVIC-AAF, 2006]126 Large Volume Inorganic Chemicals – Ammonia, Acids and Fertilisers