| HS Code | 808469 |
| Product Name | 0.8 dtex Ultra-Fine PP Staple Fiber for Wet-Laid Paper & Specialty Nonwoven |
| Material | Polypropylene (PP) |
| Fiber Type | Staple fiber |
| Linear Density | 0.8 dtex |
| Denier | 0.72 denier |
| Fiber Diameter | 10-12 µm |
| Cut Length | 3-12 mm |
| Cross Section | Round |
| Tenacity | 3.0-4.5 cN/dtex |
| Elongation At Break | 30-60% |
| Melting Point | 160-170 °C |
| Density | 0.90-0.91 g/cm³ |
| Crimp | 8-15 crimps/25 mm |
| Moisture Regain | <0.1% |
| Finish Oil Content | 0.3-0.8% |
| Thermal Bonding Temperature | 130-150 °C |
| Color | White/Natural |
| Luster | Semi-dull |
| Dispersion In Water | Good |
| Antistatic Property | Antistatic finish available |
| Hydrophilicity | Hydrophilic or hydrophobic grades available |
As an accredited 0.8 dtex Ultra-Fine PP Staple Fiber for Wet-Laid Paper & Specialty Nonwoven factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | 0.8 dtex Ultra-Fine PP Staple Fiber is packaged in 250 kg compressed bales, moisture-resistant wrapped and strapped for shipment. |
| Container Loading (20′ FCL) | Container Loading (20′ FCL): 0.8 dtex ultra-fine PP staple fiber, moisture-protected bales/pallets, optimized payload, for wet-laid paper and specialty nonwoven. |
| Shipping | 0.8 dtex ultra-fine PP staple fiber is non-hazardous. Ship in sealed, moisture-proof bags, cartons, or bales on pallets. Keep containers dry, clean, and ventilated. Avoid moisture, oils, chemicals, compression, direct sunlight, and contamination. No special temperature control required. Standard road, sea, or air freight applies; follow local transport regulations. |
| Storage | Store in a cool, dry, well-ventilated warehouse away from direct sunlight, moisture, heat, and ignition sources. Keep fiber in original sealed packaging on pallets, off the floor, and avoid heavy compression or sharp objects. Maintain clean, low-dust conditions; use FIFO stock rotation. Protect from prolonged UV exposure and strong oxidizers. Recommended storage: 5–30°C, low humidity. |
| Shelf Life | Shelf life: 24 months when stored in original packaging, cool, dry, ventilated conditions, protected from moisture, direct sunlight, and contamination. |
At 0.8 dtex, the equivalent fibre diameter of a round polypropylene filament is approximately 10.6 μm, which yields a calculated geometric surface area near 0.42 m²/g for the unroughened fibre surface. In wet-laid air filtration media, this staple is typically cut to 6 mm to 9 mm and blended into cellulose, glass microfibre, or synthetic furnish at 5–30 wt%. Because the fibre is hydrophobic, a nonionic or anionic wetting agent is required in the whitewater at 0.02–0.10 wt% of slurry volume, with pH controlled between 4.5 and 7.0 to stabilise dispersion on an inclined wire former. Vacuum boxes are operated at 20–60 kPa to dewater the web without pulling fines out of the matrix, and a self-crosslinking acrylic latex binder is added at 8–20 wt% dry on fibre to provide tensile integrity after through-air drying at 130–150°C. The principal process conflict is drainage: the same high-surface-area fibre that increases interception efficiency also raises wet-web water retention, so forming consistency is held between 0.1 wt% and 0.5 wt% to avoid flocking. Against ISO 16890-1:2016, air filtration sheet containing 0.8 dtex PP fibre is used to meet ePM1 and ePM2.5 targets in HVAC panels and cabin-air elements, where the fine denier contributes to inertial interception and diffusion capture at face velocities from 0.5 m/s to 2.5 m/s. Air permeability is assessed by ISO 9237:1995, with measured values typically between 100 L/m²/s and 600 L/m²/s at 200 Pa depending on basis weight and calendering. The operational boundary is thermal: homopolymer PP begins to soften above 145°C, so dryer profiles must avoid forming-belt excursions above 155°C or the web will shrink, embrittle, and lose uniformity across the reel.
Calendering of wet-laid liquid filtration media containing 0.8 dtex PP fibre imposes a squeeze-out threshold that must be balanced against pore-size reduction. The web is formed at 60–150 g/m² with fibre cuts from 9 mm to 12 mm, then saturated with a resol-phenolic or carboxylated acrylic binder selected for resistance to hot lubricating oil. After drying, the sheet is passed through a two-roll calender at 40–100 N/mm linear load and surface temperature between 110°C and 130°C, using a steel-to-steel nip or a steel-to-composite nip with a heated top roll. Capillary flow porometry under ASTM F316-03(2019) shows that increasing calender load from 40 N/mm to 100 N/mm reduces mean flow pore diameter by approximately 30–50%, with corresponding air permeability loss of 40–60%. The trade-off is assessed against multipass filtration performance under ISO 16889:2022, where a target beta ratio of β₁₀(c)=10 is evaluated with ISO MTD test dust at a base upstream gravimetric concentration of 10 mg/L. Process instability occurs when calendering temperature exceeds 135°C: the PP fibre surface can film over, sealing the sheet and creating a laminate-like structure rather than a porous medium. On production lines with hydraulic filter sheet widths above 1.2 m, cross-web calender deflection produces edge densification unless a heated roll with a 0.4–0.8 mm crown compensation is used. Bubble-point measurements under ISO 2942:2018 are used as a rapid release test, with acceptance limits tied to the pore-size distribution rather than bulk density alone. Published data for this specific configuration is limited at the very finest pore grades, but the general performance envelope is reproducible across commercial wet-laid machines.
| Calender load (N/mm) | Mean flow pore diameter (μm) | Air permeability at 200 Pa (L/m²/s) | ISO 16889:2022 β₁₀(c) midpoint (μm(c)) |
|---|---|---|---|
| 40 | 14–18 | 350–450 | 12–18 |
| 70 | 10–13 | 220–310 | 8–11 |
| 100 | 6–9 | 130–190 | 5–8 |
For heat-sealable paper used in single-serve tea and coffee pouch converting, the addition of 5–15 wt% ultra-fine PP fibre changes the failure mode from fibre pull-out to cohesive polymer rupture under the sealing jaw. The furnish is prepared with 6 mm cut fibre and formed on an inclined wire at low consistency to prevent hydrophobic clumping, using a food-grade nonionic dispersant. The critical control parameters are heat-seal jaw temperature between 160°C and 175°C, dwell time from 0.4 s to 1.2 s, and contact pressure from 0.3 MPa to 0.6 MPa. Below 160°C the seal remains peelable rather than cohesive, and above 178°C the PP phase can flow into the web structure and create pinholes at the seam edge. Wet burst strength is measured by TAPPI T 403 om-15, and wet tensile retention is compared with TAPPI T 456 om-15; the PP fraction supplies the thermoplastic sealing plane but does not increase wet tensile retention in proportion to fibre loading. Food-contact compliance is anchored to FDA 21 CFR 177.1520 for olefin polymers and to Commission Regulation (EU) No 10/2011, where overall migration into aqueous food simulant must not exceed 10 mg/dm². The process is incompatible with quaternary ammonium sanitising agents used in high-rate whitewater treatment when they exceed 10 ppm residual concentration because cationic adsorption onto the fibre can reduce wetting and create odour carryover in hot-melt sealing.
Drainage time on a fourdrinier table increases when 0.8 dtex PP staple replaces part of the cellulose furnish in wet-laid synthetic paper, and the increase is non-linear with loading because the fine filaments pack into interstices between beaten cellulose fibres. Furnish design for synthetic paper typically uses 20–40 wt% PP fibre at 6 mm to 9 mm cut length, with the balance bleached softwood kraft or cotton linters. Refining is applied only to the cellulose fraction; the PP fibre is added post-refining so it is not cut or fibrillated by double-disc refining. A core-shell PP/PE bicomponent binder fibre at 10–30 wt% or a film-forming acrylic latex is used to develop tensile strength because homopolymer PP staple does not bond to cellulose through hydrogen bonding. The wet web is dried in a multi-cylinder section with the first cans set below 120°C, and a final surface sizing pickup of 2–6 g/m² dry is applied to control print mottle. Opacity is tested under ISO 2471:2008, and tensile properties under ISO 1924-2:2008. The inclusion of ultra-fine PP fibre raises opacity per unit basis weight compared with equivalent cellulose furnish because the pigment-free fibre increases interfacial light scattering, but the effect saturates above 30 wt% loading in unsized sheets. Cobb water absorption under ISO 535:2014 is used to confirm the hydrophobic contribution; synthetic paper grades typically measure 20–40 g/m² at 60 s contact, which is lower than comparable cellulosic sheets but still above film-based synthetic paper. The operational limitation is the wet-end retention window: at machine speeds above 200 m/min, retention of the 0.8 dtex fibre drops unless a polyethylene oxide retention aid is dosed at 50–150 ppm relative to total furnish.
Release liner base stock for solvent-free silicone coating lines is tested for holdout rather than bulk absorption, because a base paper with rapid silicone soak-in produces uneven release force after cure. Addition of 0.8 dtex PP staple at 5–20 wt% reduces the open-pore fraction exposed to the coating head and creates a more uniform low-energy surface. The wet-laid web is formed at 50–120 g/m² and calendered before coating to a Sheffield smoothness of 20–60 SU or equivalent Parker Print Surf roughness of 1.0–3.0 μm. Silicone coat weights between 0.8 g/m² and 1.6 g/m² are applied by five-roll differential coating equipment, and cure is carried out at 120–160°C for 10–30 s. Release force is measured under FINAT Test Method FTM 3 with an acrylic PSA tape and a dwell time of 24 h at 23°C and 50% RH; target release values sit between 20 cN/25 mm and 80 cN/25 mm depending on the silicone system. The PP fibre fraction reduces aqueous extractables and improves dimensional stability after exposure to 85°C for 24 h, evaluated by TAPPI dimensional stability methods. However, PP staple does not provide the same anchorage as cellulose for some cationic silicone systems, and the converter must confirm adhesion with FINAT Test Method FTM 4 rub-off testing before production-scale lamination. The process boundary is the calender temperature: above 130°C, the PP fibre can orient and compress into flattened platelets that lower opacity and increase gloss beyond the specification range.
Electrical insulation webs made from 0.8 dtex PP fibre require target ash content and ionic conductivity control before being calendered to a densified sheet. The fibre contributes a dry dielectric constant near 2.2–2.6 at 50 Hz, measured under IEC 60250, and a dissipation factor below 0.001 in the dry state. In wet-laid insulation paper, PP staple is blended with cellulose or polyester fibre at 10–40 wt%, and the web is washed to remove residual wetting agents because even 0.05 wt% ash from surfactant salt can raise ionic conductivity. Dielectric strength is tested according to ASTM D149-20 on 0.2–0.5 mm thick calendered sheets, with typical dry breakdown values between 20 kV/mm and 40 kV/mm depending on density and void content. The application is limited to low-temperature insulation systems because homopolymer PP has a continuous service temperature below 90°C under thermal ageing, and it is not suitable for oil-filled transformer insulation where the thermal class exceeds this limit. Partial-discharge resistance is not inherently high for unmodified PP sheet; if discharge suppression is required, the web must be treated or laminated with mica or a corona-resistant coating. On production lines, batch-to-batch variance in fibre finish can shift the dissipation factor, so incoming fibre must be tested for surface conductivity using IEC 62631-3-2:2015. Published data for this specific configuration is limited, and qualification for a given insulation system should be based on thermal endurance testing under IEC 60216 rather than on short-term dielectric measurements alone.
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At a nominal linear density of 0.8 dtex (0.08 g/1000 m), the ultra-fine polypropylene staple fiber designated PPUF-0.8-WL is supplied as a cut-staple furnish for aqueous wet-laid nonwoven and specialty paper production. A cylindrical-filament calculation from ISO 1973:2021 linear density and ISO 1183-1:2019 density returns a mean geometric filament diameter of 10.4–10.8 µm and a geometric specific surface area of approximately 0.42 m²/g. The grade is available in cut lengths of 3 mm, 4 mm, 5 mm, and 6 mm. It is intended for wet-laid filtration media, battery separator base paper, cleanroom wipes, medical packaging, and other specialty nonwovens in which a fine fiber diameter is used to reduce mean flow pore diameter, improve sheet formation, and increase opacity. The fiber is not a continuous filament, a meltblown web, or a dry-laid carded staple; it is cut short and finished to remain suspended under mild agitation in a low-consistency aqueous stock system.
Typical fiber mechanical data for this grade are in the range of 3.0–4.2 cN/dtex tenacity and 70–120% elongation at break when tested on 20 mm gauge length according to ISO 5079:2020. The melting point by differential scanning calorimetry is 160–165 °C under ISO 11357-3. The low crimp configuration, normally ≤2 crimps per cm, is specified specifically for wet-laid dispersion; higher crimp increases the probability of fiber rope formation in the pulper and nonuniform sheet formation.
Because polypropylene has a density below water, at 0.90–0.91 g/cm³, the dry fiber floats unless wet out and incorporated into the stock. Wetting agents and controlled agitation are used to submerge the fiber. Once wetted, the fiber remains dispersed at low consistency, but stoppage of recirculation can allow skimming of hydrophobic fines at the stock surface. This is a production-scale handling difference from polyester staple, whose density of 1.38 g/cm³ makes the dry fiber sink more readily after wetting.
Replacement of 1.7 dtex polyester with 0.8 dtex polypropylene alters filament diameter, polymer density, and surface chemistry simultaneously. The polyester reference has a density of 1.38 g/cm³ and a geometric filament diameter of approximately 12.5 µm, whereas the PP grade has a density of 0.90–0.91 g/cm³ and a diameter of 10.4–10.8 µm. The finer PP filament increases specific surface area by approximately 18–20% compared with the 1.7 dtex PET reference, which raises binder demand at fixed tensile strength and increases drainage resistance during sheet formation. Polypropylene also lowers sheet density at constant caliper, improves alkaline chemical resistance, and reduces thermal stability; the 160–165 °C melting range limits drying and thermal bonding to a lower window than PET, which typically tolerates 220–240 °C in wet-laid drying and calendering.
When PP replaces PET in a wet-laid furnish, the surface energy of the fiber changes from about 43–44 mN/m for PET to about 29–31 mN/m for untreated PP, which may reduce saturation binder wetting unless a dispersing finish or corona treatment is used. This shift also affects aqueous dispersion: the PP surface is hydrophobic, so the dispersing surfactant system must be adjusted to prevent floating, foaming, and agglomeration. In contrast, PET wet-laid grades often disperse with less surfactant due to higher surface energy.
Stock preparation for PPUF-0.8-WL begins with cold-water wet-out at 20–30 °C. Hot stock above 40 °C can destabilize the dispersing finish and cause hydrophobic fiber balls. On an inclined-wire wet-lay pilot line with a 0.6 m forming width, the grade is typically dispersed at headbox consistency below 0.05 wt%; above this level, stock flocculation produces visible fiber clumps and pinhole defects in the formed web. A low-shear pulper with disintegrator plate speed not exceeding 10 m/s and a dwell time of 5–15 min is used. Because the fiber is hydrophobic, a nonionic or anionic dispersing surfactant is added at 0.05–0.20% by fiber mass. Foam control with a silicone or polyether defoamer is required during recirculation. The fiber length and low crimp allow mixing with cellulose, glass microfibers, or fibrillated polyolefin pulps without excessive flocculation.
Drainage resistance increases with the specific surface area of 0.42 m²/g. In practice, this means vacuum settings and forming fabric selection must be adjusted when moving from 1.7 dtex PP to 0.8 dtex PP at equal basis weight. A Dynamic Drainage Analyzer is considered more informative than Canadian Standard Freeness for synthetic staple furnishes because synthetic fiber does not hydrate or fibrillate like cellulose. Retention aid dosing is typically reduced relative to cellulose-only stock, but the exact amount depends on white water conductivity and dissolved anionic trash. Published data for this specific configuration is limited; production trials are required to set the retention program.
Because PP staple fiber does not form hydrogen bonds with cellulose, wet-laid sheet tensile development relies on binder addition, blending with fibrillated cellulose or nanofibrillated cellulose, or thermal calendering. At 0.8 dtex, the fiber increases the number of fiber-fiber contact points per sheet volume, but those contacts are frictional and do not contribute significant wet strength without binder.
Thermal calendering of PPUF-0.8-WL containing webs is performed at roll surface temperatures of 150–160 °C, with nip pressure in the range of 40–80 kN/m and line speed of 5–30 m/min. Under these conditions, the fiber softens only at the outermost surface layers. Over-temperature above 165 °C causes film formation, black specks, or sticking. Full thermal bonding of the sheet is not possible unless the fiber is blended with lower-melting sheath-core bicomponent fibers. The low filament diameter permits densification and reduces pore size, but excessive calendering also reduces air permeability and tear strength.
For latex-saturated specialty papers, acrylic, styrene-butadiene, and vinyl acetate-ethylene binders are used at binder solids addition of 10–30 parts per hundred fiber by dry weight. The fine PP fiber increases specific surface area, which consumes more binder than 1.7 dtex PP at equal tensile. Cure temperatures are commonly 120–140 °C in flatbed or through-air dryers; higher temperatures induce shrinkage and loss of caliper. The PP fiber does not absorb water, so binder migration during drying is influenced mainly by wetting and capillary forces. A surface treatment or corona discharge prior to saturation can improve binder wetting when high binder add-on is required.
In wet-laid filtration media, PPUF-0.8-WL is blended at 10–25 wt% with cellulose or glass fiber to reduce mean flow pore diameter and improve capture efficiency for the 2–10 µm particle range. Pore structure is characterised by ASTM F316 bubble point and ISO 9073-15 air permeability. The trade-off is an increase in pressure drop at a given basis weight; gradient layering with coarser fiber on the wire side is used to manage this. In battery separator base paper, the PP fiber improves resistance to alkaline electrolyte and reduces pore size after latex saturation; typical addition is 15–30 wt% with acrylic or styrene-butadiene latex. For cleanroom wipes, the hydrophobic PP fiber is used in blends with cellulosic fiber and binder to create low-lint, solvent-resistant sheets. Because PP is thermoplastic, the wet-laid sheet can be post-calendered to control thickness and surface smoothness.
As a wet-laid staple product, PPUF-0.8-WL differs from meltblown and spunbond polypropylene in both form and function. Meltblown PP can achieve fiber diameters of 1–5 µm, but it is delivered as a continuous entangled web and is not readily dispersible in water without extensive process adaptation. Spunbond PP is a continuous filament web with fiber diameters generally above 15–20 µm. The staple fiber can be shipped in bales, blended with cellulosic or glass furnishes, and formed into wet-laid sheets on standard papermaking equipment. This permits production of hybrid structures with controlled pore size and binder distribution that are difficult to achieve with spunbond or meltblown nonwovens alone.
The table summarises typical property ranges that differentiate PPUF-0.8-WL from coarser PP and polyester wet-laid grades. Values are typical production-lot averages; individual lots must be verified against the mill specification.
| Parameter | 0.8 dtex PP staple | 1.7 dtex PP staple | 1.7 dtex PET staple |
|---|---|---|---|
| Nominal linear density | 0.8 dtex | 1.7 dtex | 1.7 dtex |
| Geometric filament diameter | 10.4–10.8 µm | 15.4–15.6 µm | 12.4–12.6 µm |
| Specific surface area (cylindrical model) | 0.42 m²/g | 0.28–0.29 m²/g | 0.23 m²/g |
| Density | 0.90–0.91 g/cm³ | 0.90–0.91 g/cm³ | 1.38 g/cm³ |
| Melting range | 160–165 °C | 160–165 °C | 250–260 °C |
| Surface energy (untreated polymer) | 29–31 mN/m | 29–31 mN/m | 43–44 mN/m |
| Cut length availability | 3–6 mm | 3–6 mm | 3–6 mm |
| Tenacity | 3.0–4.2 cN/dtex | 3.5–5.0 cN/dtex | 3.5–5.0 cN/dtex |
| Elongation at break | 70–120% | 80–150% | 25–50% |
Batch-to-batch control is specified for linear density within ±0.05 dtex and cut length within ±0.5 mm. Finished fiber is shipped in compressed bales; production lots are traceable to spinneret line, spin finish tank, and cut-line settings.
PPUF-0.8-WL must not be exposed to sustained temperatures above 160 °C unless thermal degradation or partial melting is intended. Drying of the wet-laid sheet is normally held to 120–140 °C web surface temperature. The fiber is hydrophobic and does not retain moisture; however, static charge can build in dry blending, and grounding of chutes and containers is necessary at relative humidity below 30%. Unstabilized polypropylene is susceptible to photo-oxidation; outdoor service requires a UV stabilizer package and cannot be assumed from the base fiber specification alone. Storage should avoid direct sunlight and proximity to strong oxidizing agents.
In aqueous dispersion, the main operational limits are stock temperature, shear, and surfactant balance. Over-dosing anionic dispersants can generate foam and interfere with cationic retention aids. Excessive pulper speed can wrap fibers around the rotor. In one production-scale failure mode, fiber ropes were observed when the stock temperature exceeded 40 °C during initial wet-out, requiring shutdown and manual cleaning of the pulper. The grade should be introduced into the pulper gradually at 20–30 °C water to prevent this.
Regulatory status is batch-specific and must be confirmed against the finished article. The following matrix lists the applicable frameworks commonly referenced for polypropylene staple fibers in wet-laid nonwovens.
| Framework / standard | Relevant scope |
|---|---|
| ISO 9001:2015 | Quality management system for fiber manufacture and lot traceability |
| REACH Regulation (EC) No 1907/2006 | SVHC content below 0.1% w/w per Article 33; duty to communicate information |
| RoHS Directive 2011/65/EU | Annex II restricted substances: Pb 0.1%, Cd 0.01%, Hg 0.1%, Cr(VI) 0.1%, PBB/PBDE 0.1% |
| FDA 21 CFR 177.1520 | Olefin polymers for food contact, subject to extractives limits |
| EU Regulation (EC) No 1935/2004 | Framework regulation for food contact materials |
| EU Regulation (EC) No 10/2011 | Plastic materials in contact with food; overall migration limit 10 mg/dm² |
For wet-laid manufacturers transitioning from 1.7 dtex PP or PET, the practical process adjustments are lower headbox consistency, lower drying temperature, and higher binder demand at fixed tensile strength. The material is not recommended for high-temperature filtration above 120 °C continuous service unless the sheet is designed with a different fiber or has been thermally stabilized. These operational boundaries should be incorporated into mill specifications before substituting PPUF-0.8-WL into an existing wet-laid grade.