| 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 |