Dust Collector Air-to-Cloth Ratio and Bag Derate
Air-to-cloth ratio is a velocity, and pushing air through fabric too fast blinds a collector permanently.
Example
You enter
- System airflow (cfm) 12000
- Number of bags 200
- Bag diameter (in) 6
- Bag length (ft) 8
- Range for this cleaning type, low (ft/min) 3
- Range for this cleaning type, high (ft/min) 5
- Bags plugged or blanked off 30
You get
- Cloth area (ft²) 2513.27
- Air to cloth 4.77465
- Derated cloth area (ft²) 2136.28
- Derated air to cloth 5.61723
- Derated increase (%) 17.6471
- Max airflow (CFM) 12566.4
Details, formula, and sources
Too fast and the dust cake is driven into the weave instead of sitting on it, the cleaning pulse can no longer release it, and differential pressure climbs over weeks in a way cleaning does not recover. Slow enough and the cake stays on the surface where it belongs and does most of the filtering. A pulse-jet collector with 200 bags at 6 in by 8 ft carries 2,513 sq ft of cloth, so a 12,000 cfm system runs at 4.77 ft per minute -- comfortable for pulse-jet cleaning. TWO FIELD CHANGES MOVE IT SILENTLY. Add a hood and take the airflow to 16,000 cfm and the ratio becomes 6.37: still nominally in the pulse-jet range but at the top of it, and on an abrasive or fine dust that is where blinding starts. And bags out of service change the denominator directly: blank off 30 of the 200 and the cloth area falls to 2,136 sq ft, the ratio rises to 5.62 at the ORIGINAL airflow, and every remaining bag is working 18% harder. That is why bag failures cascade once they start, and why computing the ratio after any change is a thirty-second check that predicts a failure months in advance. The typical ranges are broad conventions. The correct ratio for a specific dust depends on particle size, shape, cohesiveness, moisture, temperature, and loading, and a fine cohesive dust may need a ratio well below the generic range for its cleaning type. This does not select fabric or media treatment, size the cleaning system, evaluate can velocity (the upward velocity between bags, which independently causes re-entrainment on tall collectors), size the hopper and discharge, or address the interstitial and inlet velocities that cause bag abrasion. It does not evaluate explosion protection, which is mandatory for combustible dust and is a separate calculation, and it does not size hoods or ductwork or verify capture velocity at the source, which is where dust control actually succeeds or fails. The collector manufacturer's data, ACGIH Industrial Ventilation, and NFPA 652 where the dust is combustible govern.
cloth area = bag count x pi x bag diameter x bag length for round bags; air-to-cloth ratio = airflow / cloth area; bags out of service reduce the denominator directly.
The air-to-cloth (filtration velocity) relation by name, with typical ranges -- shaker 2 to 3, reverse-air 1.5 to 2.5, pulse-jet 3 to 5, cartridge 0.5 to 1.5 -- entered as broad conventions. The collector manufacturer's data, ACGIH Industrial Ventilation, and NFPA 652 where the dust is combustible govern.
Geometry and division on the user's own collector data; no manufacturer selection table is reproduced.
Estimate. AHJ and licensed professional govern.
Field names used by the API: airflow_cfm, bag_count, bag_diameter_in, bag_length_ft, range_low, range_high, bags_out_of_service, cloth_area_sqft, air_to_cloth, derated_cloth_area_sqft, derated_air_to_cloth, derated_increase_pct, max_airflow_cfm
- The ratio is a velocity through fabric too fast drives the cake into the weave and the blinding is not recoverablebaghouse practice
- Adding a hood moves it silently more airflow, the same cloth area, and no alarm anywherebaghouse practice
- Bags out of service cascade the survivors work proportionally harder, which is why failures come in runsbaghouse practice