Scrubber Design Calculation Excel Hot Free -
Assuming a typical gas velocity of 3-5 m/s, let's use 4 m/s for this example.
The throat velocity must typically range between 60 m/s to 120 m/s (200–400 ft/s) for effective atomization.
An advanced Excel workbook designed for hot gas scrubbing is not just a calculator; it is a robust engineering tool. Here is what you should look for when downloading a spreadsheet or building your own:
Designing a wet scrubber for high-temperature ("hot") gas streams requires balancing pollutant removal efficiency with heat recovery and structural integrity scrubber design calculation excel hot
are the industry standard for removing pollutants from hot gas streams because they provide maximum surface area for gas-liquid contact while minimizing pressure drop. Designing a scrubber for high-temperature applications requires careful thermodynamic and aerodynamic balancing to avoid structural failure, solvent boiling, or poor absorption efficiency.
Entering gas at high temperatures can crack standard fiber-reinforced plastic (FRP) or ceramic scrubber internals. Ensure your spreadsheet flags inlet temperatures above 250∘C250 raised to the composed with power C
combines the gas mass velocity, packing surface area, and mass transfer coefficients. It typically ranges from depending on the packing size. Step 3: Total Bed Height ( Assuming a typical gas velocity of 3-5 m/s,
) and saturated volume is critical for sizing the shell diameter. www.mchip.net Step-by-Step Calculation Logic in Excel Gas Volume Correction
Here is an example calculation for a scrubber design using Excel:
Liquid density, viscosity, and surface tension. Here is what you should look for when
Tower diameter holds operational gas velocity safely within the non-flooding window (
$$ L = \frac223.2 \times 1.540 \times 1000 = 8.37 , \textm³/h $$
) depends on the difficulty of the separation and the efficiency of the packing material. It is calculated using the Number of Transfer Units (NTU) and the Height of a Transfer Unit (HTU): Z=NTU×HTUcap Z equals NTU cross HTU
