| Polypropylene Depth Media | Pre-filtration, process water, chemical solutions, and bulk slurry protection | Approximately 0.5–100 μm nominal, depending on construction | Usually up to approximately 80°C; confirm housing and chemical limits | 1 / 5 Lowest | Low unit cost, but generally disposable; generates polymer cartridge waste | Good for low-to-medium solids loading; service life depends strongly on dirt-holding capacity | Fiber release, premature blinding, or insufficient particle retention when used as final filtration |
| Polyethersulfone Membrane | Fine filtration of ultrapure water, process chemicals, and aqueous cleaning streams | Approximately 0.03–0.45 μm, depending on membrane grade | Commonly up to approximately 80°C for many aqueous applications | 3 / 5 Medium | Single-use formats create polymer waste; longer service is possible with validated cleaning | High and consistent particle retention when pressure, cleaning, and compatibility are controlled | Fouling, oxidation, unsuitable solvents, or excessive differential pressure |
| Polytetrafluoroethylene Membrane | Aggressive chemical filtration, solvent-compatible gas or liquid service, and vent filtration | Approximately 0.05–1.0 μm, depending on membrane construction | Often approximately 100–150°C; actual limit depends on support and seals | 4 / 5 High | Excellent chemical durability can extend service life, but disposal of fluoropolymer media is difficult | Very high chemical resistance; reliability decreases if wetting, pressure, or seal design is unsuitable | Poor wetting in aqueous service, membrane damage, or incompatibility with high-temperature hardware |
| Ceramic Membrane | High-solids slurry separation, silicon-processing wastewater, and applications requiring repeated cleaning | Approximately 0.01–1.4 μm for common microfiltration and ultrafiltration grades | Often capable of approximately 150–250°C, subject to module design | 5 / 5 Highest initial cost | Long service potential and repeated chemical cleaning reduce replacement waste; higher energy demand may result from cross-flow operation | Very high mechanical and thermal durability; suitable for regeneration when cleaning is validated | High capital cost, fragile module handling, and energy consumption from recirculation |
| Sintered Metal Media | High-temperature gas or liquid filtration, catalyst protection, and reusable process filtration | Approximately 0.5–100 μm, depending on metal powder and pore structure | Approximately 300–600°C for selected metal grades and designs | 4 / 5 High | Reusable through backwashing or other cleaning methods; metal recycling is generally more feasible than polymer recycling | Excellent mechanical strength and long life when corrosion and fatigue are controlled | Corrosion, pore blockage, thermal cycling, or inadequate cleaning access |
| Activated Carbon Media | Removal of selected organic contaminants, residual chlorine, and odor-forming compounds from water streams | Adsorptive media; particle filtration is not its primary function | Typically below approximately 60°C in water treatment; verify adsorption and safety limits | 2 / 5 Low to medium | Spent media requires controlled replacement or reactivation; performance is capacity-limited | Reliable for targeted adsorption when breakthrough is monitored; not a substitute for fine particle filtration | Breakthrough, microbial growth, pressure drop, or incorrect contaminant targeting |