The Venturi Rod Scrubber, similar to the MVS technology, is an enhanced version of a standard device that employs rods installed in the throat to create additional turbulence. These rods, positioned across the flow, also promote vortex formation, thereby increasing the interaction between the phases. This process leads to more effective capture of both particulate and gaseous contaminants.
D = √(4 * Q / (π * V))
where:
D — diameter of the unit (ft),
Q — volumetric flow rate of the effluent (CFS),
V — velocity of the medium entering the cleaner (ft/s).
This is a simplified expression and does not take into account factors such as allowable pressure drop in the system, expected pollutant concentration, and capture efficiency. Filter manufacturers include additional cyclone scrubber calculation and empirical relationships to accurately match equipment characteristics to specific production requirements.
The height of the build also plays a crucial role. It regulates the residence time of the contaminated phase inside the mechanism, which impacts particle deposition. The height of the filter can be related to its volume. For example, assuming the device has a cylindrical shape (which is true for the cylindrical part of a real purifiers), the following formula applies:
V_cyc = (πD² / 4) * H
where:
D — diameter (ft),
H — height (ft),
V_cyc — volume (ft³).
Knowing the airflow rate Q, you are able to adjust the height of the air pollution cyclone scrubber to achieve the desired gas residence time and, consequently, improve dust deposition:
t = V_cyc / Q
where:
t — residence time of the medium inside the unit (s),
Vcyc — volume of the equipment (ft³),
Q — volumetric flow rate of the effluent (CFS).
The shape of the chamber can be selected from various options, including the most common cylindrical (greater velocity, reduced cleaning depth) and conical (superior efficiency) forms, depending on the specific application.
The calculation of centrifugal force is influenced by the characteristics of the undesirable components, such as their size, concentration, and density. Additionally, determining the velocity of the incoming airstream is critical for creating the necessary vortex motion inside the cyclone scrubber. Typically, the stream velocity should not exceed 65-82 ft/s to avoid pollutants recirculation.
Pressure in the system is also an important parameter, as it affects capture performance. This primarily refers to the difference between the inlet and outlet force levels of the device. Generally, the greater the differential, the higher the velocity and intensity of the centrifugal effect, which promotes better dust deposition, especially for fine particles. It is important to note that excessive drops in levels may lead to increased energy consumption. Empirical data and engineering practices indicate that maintaining a differential between 500 and 1000 Pa is essential for achieving the necessary level of purification. The diameter and shape of the housing, as well as the sizes of the inlet and outlet openings, are calculated to maintain this optimal value.
In summary, the task of cyclone scrubber design in this regard can be formulated as selecting the parameters of the installation that ensure the necessary gas velocity while thoroughly depositing debris without excessive pressure loss.