Baghouse Differential Pressure Calculator
Determine tube sheet differential pressure drop (ΔP in inches w.g.), clean fabric vs dust cake resistance breakdown, and exhaust fan electrical energy costs.
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Baghouse Differential Pressure & Filtration Resistance
Differential pressure (ΔP) across a baghouse tubesheet is the sum of the aerodynamic drag across the clean filter media fabric plus the resistance of the accumulated porous dust cake layer. In fabric filtration, the dust cake actually performs the majority of fine particulate capture (surface sieving).
Empirical Drag & Resistance Formulations
- Darcy's Law for Fabric Filtration:
ΔP_total = ΔP_fabric + ΔP_cake = (K_1 × V) + (K_2 × V × W)
WhereVis filtration face velocity (A/C ratio),K_1is clean fabric drag coefficient,K_2is specific dust cake resistance, andWis dust cake areal density (lb/sq ft). - Fan Power Energy Penalty:
Fan BHP = [ ACFM × ΔP (inches w.g.) ] / [ 6,356 × Fan Efficiency (≈0.70) ]
Frequently Asked Questions
What is a normal operating differential pressure for a baghouse?
A healthy pulse-jet baghouse typically operates between 3.5" and 6.0" inches of water gauge (w.g.) across the tubesheet. Consistently running above 7" to 8" indicates blinded bags.
Why is some dust cake necessary for effective baghouse filtration?
The clean woven or felted fibers have pores larger than fine sub-micron dust. The initial dust cake layer (the primary porous matrix) performs over 99% of fine particulate filtration.
How much energy does an extra 2 inches of baghouse pressure drop consume?
In a 50,000 CFM system, every 2" w.g. of unnecessary differential pressure adds approximately 22.5 brake horsepower to the exhaust fan motor, costing over $8,000 per year in electricity.