Customer |
Location |
Gas source |
Gas Vol.
Wet Basis |
Supplied Equipment |
Year |
ZAO Carat TSM |
Sorsk,
Russia
|
Lead smelter |
23.000 Nm3/h |
wet electrostatic precipitator |
2010 |
Sachtleben |
Duisburg, Germany |
Pyrit roasting |
43.000 Nm3/h |
wet electrostatic precipitator |
2007 |
Rhodia Eco Services Ltd. |
Staveley Works, Chesterfield, U.K. |
Spent Gas cleaning plant |
55.000 Nm3/h |
H2O2-scrubber |
2003 |
Röhm AG |
Worms, Germany |
Spent acid regeneraion |
110.000 Nm3/h |
Quench tower, gas cooling tower |
2002 |
Anglo Platinum |
Rustenburg, South Africa |
Platinum electric furnace |
64.000 Nm3/h |
Quench tower, jet scrubber, plate wet electrostatic precipitator, gas cooling tower, square tube wet electrostatic precipitator |
2002 |
Anglo Platinum |
Rustenburg, South Africa |
Platinum smelter |
55.000 Nm3/h |
Quench tower, jet scrubber, plate wet electrostatic precipitator, gas cooling tower, square tube wet electrostatic precipitator |
2002 |
Röhm AG |
Worms, Germany |
Spent acid decomposition |
45.000 Nm3/h |
Wet electrostatic precipitator system |
2001 |
Berzelius Stolberg |
Stolberg, Germany |
Lead smelter |
42.700 Nm3/h |
Plate wet electrostatic precipitator, gas cooling tower, square tube wet electrostatic precipitator |
2000 |
Röhm AG |
Worms, Germany |
Spent acid regeneration |
45.000 Nm3/h |
Wet electrostatic precipitator system |
2000 |
Enami |
Paipote, Chile |
Copper converter |
61.000 Nm3/h |
Wet electrostatic precipitator system |
2000 |
Palabora Mining Corp. |
Phalabowa, South Africa |
Copper converter |
195.350 Nm3/h |
Fluoride scrubber, 2-stage wet electrostatic precipitator system |
1998 |
Formosa Plastics |
Yun-Lai, Taiwan |
Spent acid regeneration |
70.000 Nm3/h |
2-stage wet electrostatic precipitator system |
1998 |
Röhm AG |
Worms, Germany |
Spent acid regeneration |
15.300 Nm3/h |
Wet electrostatic precipitator system |
1997 |
Doe Run |
Herculaneum, USA |
Lead smelter |
61.200 Nm3/h |
Wet electrostatic precipitator system |
1996 |
Bayer AG |
Uerdingen, Germany |
Ferrosulphate decomposition |
61.000 Nm3/h |
Wet electrostatic precipitator system |
1994 |
John Brown |
Kamenogorsk, Kazakhstan |
Lead and zinc smelter |
100.000 Nm3/h |
2-stage wet electrostatic precipitator system |
|
Grillo - Werke |
Duisburg, Germany |
Spent acid regeneration |
35.000 Nm3/h |
Wet electrostatic precipitator system |
1991 |
Pasminco Metals Sulphide Corp. |
Boolaroo, NSW Australia |
Lead sintering |
110.000 Nm3/h |
Pre- and post-quench tower |
1991 |
Outokumpu Metals Oy |
Harjavalta, Finland |
Copper / Nickel smelter |
57.000 + 73,000
Nm3/h |
Hg-removal for two lines and common unit for Hg separation by filtration |
1991 |
Outukumpu Metals Oy |
Harjavalta, Finland |
Copper / Nickel smelter |
64.000 Nm3/h |
Wet electrostatic precipitator system |
1990 |
Rhone Poulenc |
Rieme, Belgium |
Sulphuric acid regeneration |
56.200 Nm3/h |
2-stage wet electrostatic precipitator system |
1990 |
Sulzer AG, Winterthur /CH |
Zilina / Czechoslovakia |
Sodium sulphate decomposition |
12.000 Nm3/h |
Wet electrostatic precipitator system |
1990 |
Stauffer Chemical
Company / Rhone
Poulenc |
Dominguez, Los Angeles, USA |
Sulphuric acid regeneration |
72.000 Nm3/h |
2-stage wet electrostatic precipitator system |
1989 |
Enami |
Las Ventanas, Chile |
Copper converter |
97.600 Nm3/h |
Quench, jet scrubber, cooling tower, two stage wet electrostatic precipitator (plate and square tube), Hg-removal |
1989 |
Outokumpu Metals Oy |
Harjavalta, Finland |
Copper / Nickel smelter |
61.000 Nm3/h |
Wet electrostatic precipitator system |
1989 |
National Iranian
Lead Zinc Co |
Zanjan, Iran |
Lead smelter |
23.800 Nm3/h |
Wet electrostatic precipitator system |
1985 |