Industrial Filtration

Baghouse Filter Cake Pressure Drop & Pulse Timing

Raise the air-to-cloth ratio to buy fewer bags and pressure drop rises with the square of it. The fan pays that bill every hour of every shift.

Operating Point Gas & dust
m/min
g/m³
min
m²
Resistances & Limits System
Pa/(m/min)

Residual resistance of conditioned media after cleaning.

Pa/(g/m²·m/min)
Pa
%

Total Pressure Drop

— Pa

Media plus cake at the current point in the cleaning cycle

Cycle & Cost

Media Pressure Drop
— Pa
Cake Pressure Drop
— Pa
Areal Dust Loading
— g/m²
Time to Cleaning Trigger
— min
Fan Power at This Drop
— kW

The cake resistance K2 is treated as a constant, but it depends on particle size distribution, moisture and how compressed the cake is, and a fine or damp dust can multiply it — it must come from measurement on the actual dust, not from a table. Media resistance K1 also drifts upward over bag life as fines embed permanently, so the residual drop after cleaning climbs across a bag set and the pulse interval shortens with it. Perfect cleaning back to bare media is assumed here and never happens in practice.

Baghouse Filter Cake Pressure Drop & Pulse Timing — free, with the formula and a worked example, at Textile School.