1. Key Terms & Performance Indicators
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Filter Media: Woven fabric, needle-felt, PTFE/nano-membrane coatings, surface treatments (anti-static, oil/water repellent, non-stick).
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Filter Bags: Traditional fabric bags with cages & venturis. Cleaning methods include pulse-jet, reverse-air, or shaker systems.
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Pleated Cartridge / Conical-Cylindrical Filters: Folded design increases effective surface area, widely used in cartridge dust collectors & vacuum receivers.
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Pleated / Star Bags: A pleated alternative to long filter bags, enlarging area and lowering A/C ratio.
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A/C Ratio (Air-to-Cloth): Air volume ÷ filter surface area. Lower ratios prevent blinding and slow down ΔP increase.
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ΔP (Pressure Drop): Difference between chamber inlet and outlet pressure, key indicator for cleaning efficiency and replacement cycles.
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MERV / EN1822: MERV (ASHRAE 52.2) defines general efficiency; EN1822 covers HEPA/ULPA grades (H13/H14).
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Surface Resistivity / Anti-Static: Required for combustible dust; typically <10⁸ Ω via conductive fibers, carbon, or stainless weave.
2. Quick Selection by Material (Temperature × Chemistry × Powder Properties)
Material |
Max Temp (°C) |
Resistance |
Typical Use |
Notes |
Polyester (PES) |
~135 |
Cost-effective; hydrolysis risk under high heat/humidity |
General dust |
Add ePTFE, hydrophobic, anti-static |
Acrylic |
~120 |
Acid-resistant, low dew-point corrosion |
Acidic flue gas |
Keep air-to-cloth ratio low |
Polypropylene (PP) |
~100 |
Excellent chemical & moisture resistance |
Chemical / alkaline mist |
Limited by low temp |
Aramid (Nomex) |
~200 |
Heat resistant, oxidation sensitive |
Asphalt, drying, metallurgy |
Avoid high-oxygen atmospheres |
PPS (Ryton) |
~190 |
Acid/alkali/sulfur resistant |
Boilers, chemicals |
Caution with high NOx/oxidizers |
P84 (Polyimide) |
~240 |
Excellent fine particle efficiency |
High-temp fine dust |
Higher cost |
Fiberglass |
~260 |
High-temp, low ΔP, brittle |
Hot gas filtration |
Needs PTFE coating/surface finish |
PTFE (w/ ePTFE membrane) |
~240–260 |
Best chemical resistance |
Sticky/corrosive dust, cleanroom |
High cost, requires correct cleaning |
Sintered PE/SS |
80–200+ |
Washable, CIP/SIP capable |
Food, pharma, sticky dust |
Higher initial ΔP, customizable pores |
Key Takeaway:
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Sticky/oily/moist dust → PTFE/nano membrane + hydrophobic coating.
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High-temp/corrosive → PPS, Aramid, P84, PTFE, Fiberglass.
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Washable / sanitary → Sintered PE or stainless steel.
3. Filter Forms: Bag vs. Cartridge vs. Pleated vs. HEPA vs. Sintered
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Baghouse Filters: Rugged, high dust load capacity, easy maintenance. Less surface area efficiency, higher A/C, prone to blinding with sticky dust.
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Cartridges: Compact, high area, low ΔP, efficient cleaning. Need pre-separation for sticky powders.
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Pleated / Star Bags: Retrofit option; 1.5–2.5× area vs. long bags. Must check cage/venturi compatibility.
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HEPA (H13/H14): Final polishing stage for cleanroom/recirculation. Requires PAO/DOP integrity testing + ΔP monitoring.
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Sintered (PE/SS): Washable, durable, hygienic. Higher cost/ΔP. Ideal for food, pharma, sticky dust.
4. Automatic Cleaning & ΔP Control
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Pulse Pressure: 0.4–0.6 MPa.
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A/C Reference: Cartridges 0.8–1.6 m/min; Bags 0.9–1.8 m/min.
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ΔP Baseline Method:
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Initial: 600–900 Pa
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Normal: 1000–1500 Pa
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Alert: ≥1700 Pa
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Intervention: ≥2000 Pa
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5. Vacuum Loader / Powder Feeder Filter Selection
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Types: Cartridges, pleated bags, short canister filters, sintered tubes.
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Materials: PTFE/nano-membrane, hydrophobic/oil-repellent, anti-static, food-grade SS/ePTFE for pharma/food.
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Cleaning: Pulse-jet triggered by ΔP, avoid over-cleaning.
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HEPA: Recommended for indoor recirculation/cleanroom.
6. Anti-Static & Explosion Protection
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Conductive filter media (<10⁸ Ω).
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System-wide grounding & equipotential bonding.
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Explosion protection: Flame isolation valves, venting panels, chemical suppression.
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Spark detection & extinguishing upstream for grinding/cutting operations.
7. Common Failures & Remedies
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ΔP spikes → Sticky/moist dust → Use ePTFE, improve pre-separation, heating/drying.
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Blinding (caking) → Dew point condensation/oil mist → Use hydrophobic filters, pre-coat powders.
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High penetration → Wrong/damaged media → Switch to PTFE membrane, integrity test.
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Abrasive wear → Hard particles/high velocity → Use abrasion-resistant media, add baffles.
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Static discharge → Poor grounding → Use conductive filters & bonding checks.
8. Acceptance & Quality Tests (FAT/SAT)
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Particle size/efficiency testing.
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ΔP stability under continuous load.
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Leak tests (smoke, decay, ultrasonic).
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Cleaning performance validation.
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ESD compliance.
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Documentation: Certificates, SOPs, BOM, maintenance manuals.
9. Maintenance & Stocking Strategy
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Base cleaning/replacement on ΔP trends, not calendar days.
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Keep safety stock (1–2 replacement cycles).
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IoT monitoring of ΔP, airflow, cycle count, alarms.
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ESG metrics: kWh per ton dust, filter consumption, downtime, recovery rates.
10. Filter Selection Checklist
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Powder properties: particle size, stickiness, abrasiveness, explosibility.
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Temperature & chemistry: acids, alkalis, corrosion, dew point.
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Performance: airflow, vacuum/pressure, HEPA requirement.
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Safety: anti-static, grounding, explosion venting.
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Acceptance: efficiency, ΔP, leak, noise, HEPA validation.
11. FAQ
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Q1: Best filter for <5 μm dust? → ePTFE/nano membrane + pre-separation, add HEPA if required.
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Q2: Sticky/oily powders clogging filters? → Hydrophobic treatment, heating/dehumidification, ΔP-based cleaning.
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Q3: Save energy with bag vs. cartridge? → Cartridges or pleated bags = larger area, lower ΔP.
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Q4: Where to place HEPA? → After fan: Main filter → Fan → HEPA (with PAO/DOP test).
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Q5: Is anti-static filter mandatory for combustible dust? → Strongly recommended with full grounding/explosion strategy.
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Q6: Filter replacement cycle? → Based on ΔP trend, cleaning efficiency, and integrity tests, not fixed dates.