Venturi scrubber, designed to remove particulate matter (like dust, ash, or soot) from gas streams—commonly used in industrial pollution control, boiler systems, or air cleaning systems.
Working Principle: a venturi scrubber is designed to effectively use the energy from a high-velocity inlet gas stream to atomize the liquid being used to scrub the gas stream. This type of technology is a part of the group of air pollution controls collectively referred to as wet scrubbers.
Advantages of a Venturi System:
Medium to high removal ratio
Capable of removing various parameters
Highly cost effective
The primary function in which the wet scrubbers operate is to cause dust particles to attach to the water droplets. This contact occurs in three phases, these are:
Inertial Impact:
The direct impact of a particle with a water droplet, thus removing it from the emission gas stream. When the velocity between the two objects is relative this typically occurs.
Interception:
If a faster particle is not large enough to impact as water droplets, this gas particle may attempt to go around a slower or stationary object. As it does, its inertial energy will slow subsequently it is likely to impact a following water droplet in a scrubber system thus removing it from a the emission gas stream.
Diffusion:
Occurring in in particles typically less than .3 micron this process provides higher collection than would otherwise be expected due to the mixture of inertial impaction and Interception.
Acid Gas Removal
Calcium carbonate can also be added to water, with the resulting slurry sprayed into a flue gas scrubber. The process is found to be more efficient if a calcium hydroxide/water slurry is used, removing over 95% of Sulphur dioxide. The Sulphur dioxide is absorbed into the spray and precipitates as wet calcium sulphate. By re-circulating the slurry and injecting oxygen, calcium sulphate (gypsum) is formed which can be sold as a by-product. CaSO3 0.5H2O + 0.5O2 + 1.5H2O -> CaSO4 . 2H2O
We can provide a wide range of filtration systems suitable for various types of waste incineration systems.
Packed tower wet scrubber
Venturi scrubber
Cyclone
Deacidification tower
Activated carbon adsorption tower
Bag fliter
| Models | YDF-20 | YDF-30 | YDF-50 | YDF-100 | YDF-150 | YDF-300 | YDF-500 | |
|---|---|---|---|---|---|---|---|---|
| Processing Capacity (kg/batch) | 10-20 | 20-30 | 30-50 | 50-100 | 100-150 | 200-300 | 300-500 | |
| Working Hours Per Batch Cycle* (min) | 90-120 | |||||||
| Primary Chamber Volume (m3) | 0.2 | 0.38 | 0.5 | 1 | 1.5 | 2.4 | 3.5 | |
| Waste Feeding Gate Size (mm) | 380 x 480 | 480 x 600 | 620 x 800 | 700 x 900 | 760 x 960 | 900 x 1100 | 1080 x 1280 | |
| Temperature (℃) | Primary Chamber | 900 | ||||||
| Second Chamber | 1300 | |||||||
| Smoke Residence Time (s) | > 2 sec in second chamber | |||||||
| Applicable Waste Type | Hazard Medical Waste/Consumables, Plastic, Paper, Domestic Waste, Animal Corpse, Electronic Component | |||||||
| Primary Burner - Baltur Italy | BTL-6, 0.11kw | BTL-6, 0.11kw | BTL-10, 0.11kw | BTL-10, 0.11kw | BTL-10, 0.11kw | BTL-10, 0.11kw | BTL-14, 0.18kw | |
| Second Burner - Baltur Italy | BTL-10, 0.11kw | BTL-14, 0.18kw | BTL-14, 0.18kw | BTL-20, 0.18kw | BTL-20, 0.18kw | BTL-26, 0.25kw | BTL-35, 0.37kw | |
| Total Diesel** Consumption (litre/h) | 11-18 | 11-18 | 14-23 | 16-35 | 16-35 | 20-40 | 38-57 | |
| FD Fan Power (kw) | 0.37 | 0.37 | 0.55 | 0.75 | 0.75 | 0.75 | 0.75+0.75 | |
| Applicable Voltage | 380V 3Phase / 220V 1Phase | |||||||
| Outer Dimensions (m) | 1.6 x 1.3 x 2.65 | 1.45 x 0.9 x 2.6 | 1.8 x 1.2 x 3 | 1.86 x 1.4 x 3.2 | 2.1 x 1.5 x 3.5 | 2.25 x 1.6 x 3.8 | 3.0 x 2.0 x 4.8 | |
| Chimney Dimensions (mm) | φ280 x 6000 | φ280 x 6000 | φ300 x 9000 | φ330 x 9000 | φ380 x 9000 | φ400 x 9000 | φ460 x 9000 | |
| Weight (kg) | 2000 | 3000 | 5000 | 6800 | 8000 | 9600 | 15000 | |
| Manufacturing Standard | GB 18484-2020 (equals to EPA or EU standards) | |||||||
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