
Quick read
- “ePTFE versus traditional filter media” is not a comparison of two products. It is a comparison of a surface membrane against depth-loaded media, and that distinction decides every number anyone is going to argue about.
- The comparison your datasheet is missing is quality factor. Efficiency and pressure drop move together, so neither alone ranks a media. QF = -ln(1 – efficiency) / pressure drop compresses both into one figure of merit, and it is the number published under the ISO 29463 and EN 1822 series.
- Independent published work on biaxially stretched PTFE membrane confirms the mechanism and the trade-off in one sentence: higher molecular weight and lower particle-size dispersion favour finer fibres and narrower pores, giving efficiencies close to 100 %, but with increased pressure drop and slightly reduced quality factor.
- ePTFE is not the answer for every duty cycle. Where the air is dry dust at moderate temperature, conventional or nanofibre media remain the economical choice, and saying so is what makes the rest of the comparison credible.
- When specifying, require four numbers that cannot be argued with: efficiency and pressure drop measured at the same face velocity and same test aerosol, the MPPS used, and the QF computed from them. A media quoted without all four is being compared on a single axis.
What kind of comparison this actually is
The phrase traditional filter media covers several mechanisms that behave differently from each other, and most disagreement about ePTFE is really disagreement about what is being compared against it.
Two families matter here. Depth-loaded fibrous media, which includes glass fibre, cellulose, polyester, meltblown and electret polypropylene, trap particles inside a three-dimensional mat rather than on a surface. A particle that enters the mat is captured somewhere in its thickness, and loading progressively reduces the effective pore space. Mechanical pore media, which includes ePTFE, filter by sieving at a defined surface. The pore size is fixed by the manufacturing process, so a particle larger than the pore cannot pass, and captured material accumulates on the face where it can be removed.
That single structural difference produces three consequences that explain almost every performance claim in this category.
First, loading behaviour differs. A depth medium reaches a terminal pressure drop as its mat fills. A surface membrane can be cleaned, and our published field data on emulsion-foam-coated ePTFE filters records pressure drop rising only slowly across thirty cleaning cycles, from 319 to 392 Pa, with the lowest mass loss in the comparison set. Cleaning restores a surface membrane toward its original pressure drop; cleaning a depth medium removes only part of what it has trapped.
Second, the efficiencies are not measured the same way. A depth medium reports a penetration that depends on loading state and fibre charge. A mechanical membrane reports a pore-defined performance that is far less sensitive to how dirty it is, which is why the same media can be quoted at essentially the same efficiency before and after cleaning.
Third, the failure modes are different. Electret media rely on stored electrostatic charge, and that charge decays under humidity and temperature. Our published comparison records a conventional electrostatic filter dropping to 84.7 % efficiency on 0.3-0.5 µm particles at 100 °C while the ePTFE membrane held above 99 % across all particle sizes, and dropping sharply to 41 % after immersion in isopropanol where the ePTFE membrane stabilised at 82.5 %. Independently published work on fibrous aerosol filtration makes the same structural point in general terms: polypropylene electret filters depend on stored electrostatic charges that decay under humid or thermal conditions, and conventional fibrous media carry high airflow resistance at the most penetrating particle size of roughly 0.1-0.3 µm. The broader theory, including single-fibre capture mechanisms and the definition of the most penetrating particle size, is set out in a peer-reviewed review of fibrous aerosol filtration, and the comparative behaviour of mechanical and electret media in one framework is covered in a review of membrane-based air filtration technologies.
For background on the filtration grading that these media are sold into, the regulatory and measurement framework is set by national agencies rather than by any single manufacturer; the US Environmental Protection Agency publishes the air quality context, and the National Institute of Standards and Technology maintains the reference measurement infrastructure that particulate measurement depends on. For a general reference on how air filters are classified and where they sit in a building ventilation system, the air filter reference page is a useful starting point, and the separation-process definitions behind membrane media are on the microfiltration reference page.
If you want the mechanism reference in one place, the ePTFE air filter membrane category page documents the CNbeyond membrane range and the fact that pore size, pore size distribution and open area are process controls rather than outcomes, which is what allows resistance and efficiency to be tuned together instead of traded off blindly.
The number that should decide this comparison: quality factor
Here is the practical problem with an ePTFE versus traditional media comparison conducted on efficiency alone.
Efficiency is bounded. Once a media is above roughly 99.9 %, incremental improvement is nearly invisible on a spec sheet, while the cost of reaching it continues. Pressure drop is unbounded and sets the fan energy. Efficiency and pressure drop are not independent: a denser or finer structure raises both at once. So a media that is slightly more efficient and substantially more restrictive looks like a winner on efficiency alone.
Quality factor is the correction. The published definition is QF = -ln(1 – η) / ΔP, where η is filtration efficiency expressed as a fraction and ΔP is the pressure drop across the media. Higher is better. It is the figure of merit used in the ISO 29463 and EN 1822 test series, and it is the right single number to compare media across grades because it rewards media that deliver high efficiency at low resistance rather than either one alone.
Our own ePTFE versus nanofibre comparison uses exactly this metric, and states that for typical commercial media at H11 to H13 grade the quality factor is the meaningful discriminator rather than efficiency. The method is not ours; it is the long-established figure of merit for filter media, and the broader context of how fibrous filter performance parameters are defined together is covered in the independent review of fibrous aerosol filtration. An independently published study of biaxially stretched PTFE membranes measured filtration efficiency, pressure drop and quality factor according to ISO 29463-3 using 0.1-0.3 µm aerosols, and reported the trade-off directly: the highest quality factor belonged to the least dense group, while the group with the finest and most uniform pore network achieved near-100 % efficiency together with the highest pressure drop in the set. The best overall compromise in that study was not the highest-efficiency sample but the one balancing both, with a filtration efficiency of 99.9999 % at a pore size of 0.328 µm and an average fibre diameter of 126.75 nm. The full material study is available through Preparation and material-structure-performance relationships of biaxially stretched PTFE membranes, which is also where the bubble point method is described as the pore size determination technique for this membrane class.
Three rules follow directly, and they are worth more than any single efficiency figure.
Ask for efficiency and pressure drop at the same face velocity and the same test aerosol. A media quoted at low velocity will look efficient and cheap on resistance. Without the test condition, the two numbers are not comparable.
Ask which particle size the efficiency was measured at. Efficiency is a curve, not a constant, and the least efficient point on that curve is the most penetrating particle size. Comparing a media measured at 2.5 µm against one measured at 0.3 µm is meaningless, and it is one of the most common ways a comparison goes wrong in writing.
Ask for the quality factor, or compute it yourself from the other two. If a supplier declines to supply pressure drop alongside efficiency, the reason is usually that the quality factor does not favour their media.
Definitions for the underlying metrics are on the quality factor reference page, and the filter grade framework those tests belong to is documented on the HEPA reference page and in our H11 versus H12 versus H13 grade explanation.
A contradiction in our own published comparison, and what it teaches
While preparing this article we went back through our published ePTFE versus traditional media comparison and found an inconsistency worth publishing rather than quietly correcting.
The pressure drop and permeability table in that article gives ePTFE membrane at 528 Pa with a permeability of 80 dm³/m²/s, cellulose at 312 Pa and 838 dm³/m²/s, and polyester at 370-410 Pa and 540-685 dm³/m²/s. On those figures, ePTFE is the highest-resistance and lowest-permeability option in the table. The text immediately after the table then states that ePTFE offers significantly lower initial pressure drop compared to traditional glass fibre filters, which contradicts the table it sits under.
That contradiction is instructive for anyone evaluating media, which is why it is worth stating plainly rather than fixing quietly.
The likely explanation is that the table and the sentence were measured under different conditions, probably different face velocity, different test aerosol or different media configuration, and the conditions were not recorded alongside either. That is precisely the failure mode described in the previous section. Two pressure drop numbers are only comparable when the velocity, the aerosol and the configuration are identical, and when they are not, the comparison is meaningless in both directions.
The practical lesson is that any supplier quoting a pressure drop advantage without stating the face velocity is making a claim you cannot check. The full comparison article is on our site as the ePTFE versus traditional filter materials comparison, and the equipment-level context for why delivered static pressure matters sits in our bubble point membrane and composite filter media ranges.
We have corrected our own published table and added the test conditions to it. If you hold a datasheet from us that quotes either figure, ask for the conditions and we will supply them.
Where ePTFE genuinely wins, and where it does not
A comparison that only lists advantages is not a comparison, and it is also the reason so much media purchasing goes badly. The honest position is that ePTFE wins decisively in a defined envelope and loses on price in most air filtration outside it.
The case for ePTFE is strongest where four conditions coincide. The air is wet, oily or condensing; the temperature is high or the cycle is cyclic through extremes; the chemistry is aggressive enough to attack a polymer; and the required grade is genuinely high. In that envelope a surface membrane is not incrementally better, it is qualitatively different, because the alternatives degrade exactly where the duty is hardest.
The case against is strongest where conditions are mild. Our own published guidance is that for dry dust at moderate temperature, conventional or nanofibre media are the economical choice and the ePTFE premium is not justified. The same article frames the decision as which media fits the operating environment rather than which is better in absolute terms.
The single most misunderstood variable is time at temperature. A media that is comfortable at room temperature can fail on a hot gas stream, and the failure is not gradual. Our published thermal comparison records the electrostatic alternative losing a large share of its efficiency on 0.3-0.5 µm particles at 100 °C while the ePTFE membrane retained above 99 %. If your duty includes temperature, that is the number to ask about, and it is more decision-relevant than the room-temperature efficiency on the datasheet.
For background on why particle size and filtration grade matter together rather than separately, the reference definitions for particulate matter fractions are collected on the particulate matter reference page.
Moisture changes the filter class, not just the condition. Because ePTFE is hydrophobic it does not wet out in humid, misty or oily airstreams. That single property is why it is used outdoors, on gas turbine intakes and in pharmaceutical exhaust, where a fibrous depth medium changes behaviour once it becomes damp.
Cost is real and should be stated as a ratio, not a verdict. Our published comparison gives the per-square-metre cost of ePTFE membrane as three to ten times that of conventional or nanofibre media, with service life two to five times longer. Whether that is a good trade depends entirely on the duty cycle and the replacement labour. Our sustainability in filtration article sets out the arithmetic properly: roughly 70 to 80 percent of the lifecycle advantage of long-life ePTFE media comes from media lifespan rather than from material chemistry or end-of-life pathway, and the case holds on duty cycles of 10,000 hours per year and above. Below that, the per-unit premium outweighs the lifespan advantage.
How to specify a media comparison that survives procurement
Most media disputes are resolved by asking for evidence rather than by arguing about materials. This is the specification that prevents them.
Require a single test report covering all four media on one test aerosol, at one face velocity, with the MPPS stated. A quote assembled from four suppliers’ best numbers is not a comparison; it is a collection.
Require the quality factor for each media, computed from the reported efficiency and pressure drop at that condition. If a supplier will not provide pressure drop, they have effectively conceded the comparison.
Require the dust-holding capacity for any depth-loaded candidate, defined as the particle load captured at the maximum allowable pressure drop. Without it, a depth medium’s efficiency figure has no service-life meaning attached.
Require the temperature and humidity exposure the efficiency claim survives. Ask specifically about electrostatic media and about any hydrophilic coating, because those are the two that degrade, and our published comparison gives both the wet-isopropanol and the 100 °C data points.
Require the cleanability method. A surface membrane cleaned by pulse-jet, by wash or by spray recovers differently, and the recovery percentage over a defined number of cycles matters more than the first-cycle pressure drop.
Require the substrate and support structure for any membrane media in a pleated configuration. A membrane without support is mechanically delicate, and this is the honest limitation of ePTFE rather than a footnote.
Independent verification is worth using here, and it is worth knowing which laboratory actually performs the test rather than assuming any certificate means the same thing. Recognised third-party verification bodies publish how they certify filtration media and safety-critical equipment, and the distinction between an in-house test report and an independent one is exactly the distinction this section is about. The British Standards Institution publishes its certification and standards framework, UL Solutions certifies electrical and fire-hazard safety for equipment sold into North America, and TWI publishes its materials and product testing services. Established media manufacturers also publish their own test methodology openly, which is a useful cross-check on any single supplier’s numbers: Donaldson documents its filtration test standards on its technical pages.
For the wider material range and the customised configurations we build against a specific duty, the contact page is where a media comparison brief should start, and our manufacturing capability is documented on the factory tour and about pages.
A short decision procedure
If you want the answer in four questions rather than a matrix.
Is the air dry and is the temperature moderate? If yes, conventional or nanofibre media are the economical answer and no further comparison is needed.
Does the duty include water, oil, condensation or a wash cycle? If yes, a depth medium changes behaviour when it wets, and ePTFE’s hydrophobicity is doing structural work.
Does the duty exceed room temperature, or cycle through extremes? If yes, check the media at temperature, not at ambient, and discount anything that depends on stored charge or on a hydrophilic coating.
Is the required grade genuinely high, or is the specification inherited? This is the question buyers skip most often, and it is the one that decides. If the required efficiency is well below what the membrane class delivers, paying the membrane premium is buying capability the process will never use.
If all four answers point the same way, the comparison is settled. If they do not, the honest answer is that the duty needs a composite or laminated media rather than a single-ply choice, which is a conversation worth having early rather than at the point of purchase order.
One practical note on indoor versus occupational exposure framing, because it changes who writes the specification and what they will accept as evidence. Where a filter protects a process, the grade is set by the process specification. Where it protects people, the requirement usually arrives as an exposure limit or an occupational standard rather than as a media preference, and the relevant framework is administered by regulators rather than by the buyer. The US Occupational Safety and Health Administration publishes the occupational framework applicable in the United States, and the Agency for Healthcare Research and Quality publishes the evidence and guidance base used in healthcare filtration contexts. Asking which of those two situations you are in is the first question, because it determines whether efficiency or service life is the parameter the specification will be judged on.
Where CY-PTFE fits in the air filtration range
Our air filtration membrane line is the CNbeyond ePTFE membrane, manufactured at Ningbo ChaoYue, using PTFE resin as the starting material and controlled through special processing to set pore size, pore size distribution and open area. Because those three parameters are process controls rather than outcomes, resistance and efficiency can be tuned against each other deliberately instead of accepting whatever the line produces. The full line, including the bubble point membrane for precision filtration and the composite filter media for laminated constructions, is on the products page, and the material context for PTFE itself is on the polytetrafluoroethylene reference page.
The same membrane chemistry appears elsewhere in our range, in textile membranes, protective vents and window covers, which is worth knowing only because the same resin and the same stretching process produce those products; the textile application is documented on the ePTFE membrane for textile page. The distinction between a filtration membrane and a breathable vent membrane is a real one and is covered in our hydrophobic versus oleophobic vent membrane guidance, while the common error of treating PTFE and TPU as interchangeable grades of one material is addressed separately in our ePTFE versus TPU comparison. The product-level questions buyers ask before ordering are collected on the faqs page. Product-level questions and the questions buyers most often ask before ordering are collected on the faqs page.
FAQ
Q1: Is ePTFE always better than traditional filter media?
A1: No, and a supplier who says otherwise is selling rather than engineering. ePTFE wins decisively where the air is wet or oily, the temperature is high or cycling, the chemistry is aggressive, and a genuinely high grade is required. In those conditions the alternatives degrade exactly where the duty is hardest. But for dry dust at moderate temperature, conventional or nanofibre media remain the economical choice, and our own published guidance says the ePTFE premium is not justified in that envelope. The comparison is never about which media is better in absolute terms; it is about which fits the operating environment.
Q2: What is quality factor and why should it decide the comparison?
A2: It is the figure of merit that combines the two numbers that actually matter, efficiency and pressure drop, which are otherwise easy to misread because they move together. It is defined as QF = -ln(1 – efficiency) / pressure drop, and it is used in the ISO 29463 and EN 1822 test series. Higher is better. The reason it matters is that efficiency is bounded near 100 % while pressure drop is not, so a slightly more efficient but much more restrictive media looks like a winner on efficiency alone. Independently published work on stretched PTFE membrane shows the effect directly, with the densest pore network giving near-100 % efficiency and the highest pressure drop in the set, while the best quality factor belonged to a less dense group.
Q3: Why does our own published comparison show ePTFE with a higher pressure drop than cellulose?
A3: Because the table and the sentence beneath it were measured under different conditions that were not recorded, and we have corrected it and added the test conditions. The table gave ePTFE at 528 Pa against cellulose at 312 Pa and polyester at 370-410 Pa, which contradicts the claim of lower pressure drop that followed it. The lesson generalises: two pressure drop numbers are only comparable when face velocity, test aerosol and media configuration are identical. A pressure drop quoted without its velocity is not a checkable claim.
Q4: How much more expensive is ePTFE media?
A4: Our published comparison gives a per-square-metre cost of three to ten times that of conventional or nanofibre media, with service life two to five times longer. Whether that is a good trade depends on the duty cycle rather than on the ratio itself. Our sustainability analysis puts roughly 70 to 80 percent of the lifecycle advantage into media lifespan, and finds the case holds on duty cycles of 10,000 hours per year and above; below that threshold the per-unit premium outweighs the lifespan benefit.
Q5: What temperature can ePTFE media handle?
A5: Our air filtration range is published as operating continuously from about -240 to +260 degrees C, which is why it is specified on gas turbine intakes and in high-temperature exhaust. The decision-relevant figure for most industrial duties is the comparison at an elevated rather than ambient temperature. Our published data shows a conventional electrostatic filter falling to 84.7 % efficiency on 0.3-0.5 µm particles at 100 °C while the ePTFE membrane held above 99 % across all particle sizes. Always ask for efficiency at the duty temperature, not at room temperature.
Post time: Oct-23-2026
