Neutralising acid gases and harmful emissions down to the limits — before an enforcement order requires it.
Each unit has its own job: the cyclone takes out the coarse fraction, the scrubber or absorber takes up the gas, the mist eliminator stops carry-over and the dosing unit holds the pH.
Wet gas cleaning with an absorbent: removal of acid gases, ammonia, VOCs and odours. It cools the hot gas at the same time.
Column units that dissolve and then recover the target component. Sized from the process equilibrium curve; they often work in tandem with a scrubber.
Dry and wet precipitators for large gas volumes at low resistance. A WESP captures aerosols and acid mist; rebuilding the fields is cheaper than replacement.
They take the coarse fraction out ahead of the scrubber — less reagent used, less packing wear and a lower load on the effluent system.
They catch liquid carry-over after the scrubber — otherwise droplets go up the stack and into the air. Periodic washing is needed: a blocked mist eliminator raises the ΔP of the whole line.
Reagent dosing and control: without a stable pH the scrubber efficiency halves. pH-based control saves reagent.
Adsorption stage for odours, VOCs and selected gas contaminants after sorbent-capacity verification.
| Parameter | Value |
|---|---|
| Efficiency | up to 99.5% |
| Substances removed | SO₂, HCl, HF, NH₃, VOCs, odours |
| Gas flow | 1,000 – 300,000 m³/h |
| Gas temperature | up to 200 °C |
| Irrigation rate | 2 – 8 l per m³ of gas |
| Reagents | NaOH, Ca(OH)₂, lime milk |
| Pressure drop | 800 – 2,000 Pa |
The cyclone takes the coarse fraction out ahead of the scrubber: less reagent is used, packing wear drops and its service life grows, and the load on the effluent system falls. A typical arrangement for cement, lime, metallurgy and CHP fly ash.
The scrubber efficiency halves. pH-based control saves reagent; monitoring covers pH, ORP and flow, with a PLC and data logging in control. Lime milk needs protection against scaling.
Yes, but the loop needs heating. Without heating, wet cleaning does not fit sub-zero temperatures. The site must also have an effluent treatment system.
It catches liquid carry-over after the scrubber — otherwise droplets go up the stack and into the air. Carry-over after the stage is below 50 mg/m³. Periodic washing is needed: a blocked mist eliminator raises the ΔP of the whole line.
For large gas volumes (20,000 – 1,500,000 m³/h) with a low allowable pressure drop (150 – 300 Pa), at temperatures up to 450 °C. A wet precipitator (WESP) captures aerosols and acid mist. Dust resistivity is analysed before selection; on an existing precipitator, rebuilding the fields is cheaper than replacement.
Absorbers and strippers are column units that dissolve and then recover the target component. They are sized from the process equilibrium curve, need a steady flow and concentration, and often work in tandem with a scrubber.
If the primary duty is dry dust, see the dust collection solution; for continuous measurement of the cleaning result, see environmental monitoring.
Dry dust collection and process extraction — from a single machine to a whole workshop: baghouse and cartridge filters, cyclones, electrostatic precipitators, hoppers and fans.
Open →Environmental monitoringCEMS and AQMS stations, sampling, gas analysers, dust monitors and online water and effluent monitoring — with data transmission to the regulator.
Open →An engineer replies with a selection and specification within one working day.