| HS Code | 297222 |
| Material | Polypropylene |
| Fiber Type | Staple Fiber |
| Linear Density | 1.5 D |
| Cut Length | 38 mm |
| Color | Natural White |
| Crimp | Crimped |
| Fiber Diameter | Approximately 15 µm |
| Tenacity | 2.5-4.5 cN/dtex |
| Elongation At Break | 20-60% |
| Density | 0.90-0.91 g/cm³ |
| Melting Point | 160-170 °C |
| Softening Point | 140-150 °C |
| Moisture Regain | 0.01-0.1% |
| Acid Resistance | Excellent |
| Alkali Resistance | Excellent |
| Uv Resistance | Poor unless stabilized |
| Thermal Conductivity | Low |
| Electrical Insulation | Good |
| Flammability | Combustible; melts and drips |
As an accredited 1.5D*38mm Polypropylene Staple Fibe factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | 1.5D*38mm Polypropylene Staple Fiber is packaged in 250 kg compressed bales, wrapped in woven polypropylene and secured with strapping. |
| Container Loading (20′ FCL) | 1.5D*38mm Polypropylene Staple Fiber loaded in a 20′ FCL container, in bales or pallets, shrink-wrapped and secured for ocean transport. |
| Shipping | 1.5D*38mm polypropylene staple fiber is packed in compressed bales or woven bags, palletized and shrink-wrapped for moisture protection. It is non-hazardous and ships via standard truck, rail, or container freight. Keep dry, clean, and away from ignition sources. No special dangerous-goods documentation required. Handle with care to avoid package damage. |
| Storage | Store 1.5D×38mm polypropylene staple fiber in a cool, dry, well-ventilated warehouse. Keep in original sealed packaging on pallets, away from direct sunlight, heat, ignition sources, moisture, oils, acids, and alkalis. Maintain moderate temperature and humidity. Avoid prolonged compression or heavy stacking to prevent deformation. Handle carefully to reduce dust and static. Follow supplier SDS and local regulations. |
| Shelf Life | Typically 24 months in original unopened packaging, stored dry, cool, and away from direct sunlight, moisture, and contamination. |
The 1.5 denier 38 mm polypropylene staple fibre, equivalent to 1.67 dtex at 0.91 g/cm³, is supplied as a crimped staple with a nominal cut length of 38 mm. Homopolymer PP melt point ranges from 160°C to 170°C, and the fibre exhibits a moisture regain below 0.05% at 65% RH; this low regain generates triboelectric charging during carding if finish application falls below 0.08% by weight. The linear density of 1.5 denier is fine enough to produce uniform carded webs but reduces card production speed relative to 3.0 denier staple by approximately 15-25% on worker-stripper nonwoven cards. Downstream routes must therefore be selected on the basis of mechanical entanglement or a bicomponent binder fibre, because PP homopolymer alone cannot form stable calender thermal bonds without surface melting at temperatures exceeding 158°C, which degrades fabric hand and shrinks webs. All statements below refer to fibre that has been pre-opened and conditioned to 50±10% RH for 24 h unless otherwise noted.
In automotive carpet backing operations where 1.5 denier 38 mm PP staple fibre is used as the primary structural layer, the cut length is specified to reduce card cylinder loading while retaining sufficient mechanical entanglement in high-speed needlelooms. A typical formulation is 100% PP homopolymer staple, with 10-30% recycled PP staple substituted in closed-loop production when FMVSS 302 burn-rate performance is not downgraded. Some constructions use a fibre blend of 70-80% PP staple and 20-30% PET staple to raise dimensional stability above 90°C; PET-containing blends require a needling density at least 15% higher than 100% PP webs to prevent delamination of the two fibre populations. Compliance for automotive-grade material is governed by IATF 16949:2016 for the manufacturing system, ISO 3795/FMVSS 302 for horizontal burn rate, and REACH (EC 1907/2006) Annex XVII for restricted substances. Fabric tensile properties are tested according to ISO 9073-3, tongue tear according to ISO 9073-4, and mass per unit area according to ISO 9073-1.
The production process begins with staple fibre opening through a bale opener, followed by fine opening and blending with recycled fibre in a weigh-pan blender. A double-doffer card with worker-stripper rollers produces a web of 15-25 g/m² that is crosslapped to a final mass per unit area of 300-1200 g/m². Needlepunching is performed on a downstroke/upstroke machine with needle boards fitted with 15×18×32×3.5 barb needles, and needle density ranges from 500 to 1500 punches/cm² depending on final stiffness; excessive needle density above 1500 punches/cm² shears fibre and increases airborne mineral oil. Terminal products include nonwoven carpet backing, trunk floor coverings, wheel arch liners, parcel shelf substrates, and under-seat insulation pads. On production-scale lines, crosslapper edge weight thickening exceeding 8% appears when card feed lot mixing of recycled PP is not homogenized, and card cylinder loading is observed at ambient humidity above 60% RH.
Industrial dust collection bags made from 1.5 denier 38 mm PP staple are built as needlepunched felts with a scrim reinforcement of 100% PP woven fabric or PP spunbond, depending on the pulse-jet pressure range. The staple fibre is blended at 100% with 0.5-1.5% of a conductively treated finish to dissipate static charge, but for explosive dust the media requires additional conductive fibre or carbon-black antistatic treatment; published data for this specific configuration is limited because antistatic packages vary by zone classification under EU 1999/92/EC. The compliance framework for cleanable filter media includes ISO 11057 for dynamic filtration performance, ISO 16890 for size-resolved efficiency, and ISO 9237 for air permeability; carcass tensile strength is tested under ISO 9073-3.
The downstream process begins with blending of the PP staple with a lubricated finish add-on of 0.10-0.20% by weight, followed by carding and crosslapping to a web mass of 400-600 g/m². The needleloom is configured with 4 to 6 needle boards and pile heights of 2.0-3.0 mm, after which the felt is singed or calendered at 145-155°C to reduce surface fibre shedding. At calender temperatures above 158°C, the PP surface fuses into a discontinuous film that increases pressure drop and must be discarded; at temperatures below 140°C, singeing creates loose melted droplets that clog filter bag seams. Terminal products include pulse-jet filter bags for cement kiln dust, wood dust extraction sleeves, and liquid filter bags for metalworking coolants.
The dominance of 38 mm staple in PP needlepunched geotextile separation layers is not based on tensile strength alone but on the balance between carding productivity and hydraulic anisotropy. In roadbed separation, the staple is used at 100% polypropylene with an incorporated UV stabilizer package of 0.3-0.8% HALS by weight of the fibre; for drainage geotextiles, 1.5-2.0% of a calcium carbonate masterbatch may be present to reduce film formation during calendering. Compliance for durable geotextiles is governed by ISO 9001:2015 for production quality, ISO 10318 for function terminology, and performance tests include ISO 11058 for water permeability, ISO 12956 for pore size, and ASTM D4833 for index puncture resistance. Tensile strength must be reported under ISO 10319, and weathering under ISO 12224 for UV resistance.
Manufacturing is performed on a high-loft nonwoven line: bale opening, carding, crosslapping to 800-2000 g/m², needlepunching with fork needles, and optional two-roll calendering at 135-150°C. A key process conflict emerges when the crosslapper produces edge folds at web widths above 4.0 m; these folds reduce puncture resistance by 20-30% unless a needling density of at least 700 punches/cm² is applied in the edge zones. Terminal products include nonwoven geotextile sheets for road sub-base separation, underlayment behind retaining walls, landfill drainage composites, and protection layers beneath geomembranes. On production-scale installation, 200 g/m² PP geotextile is susceptible to construction traffic puncture unless protected by a sand layer.
Whereas mechanical entanglement processes use PP staple fibre as the sole fibre, thermal bonded hygiene coverstock requires a bicomponent binder fibre because the homopolymer PP surface cannot form stable bond points below its 160°C melt temperature. Formulations for a carded acquisition/distribution layer (ADL) typically consist of 80% 1.5 denier 38 mm PP staple and 20% 2.0 denier 38 mm polyethylene/polypropylene sheath-core bicomponent fibre; a calender-bonded top cover may use 85/15 PP/bicomponent blends at a web mass of 18-25 g/m². The addition of more than 30% bicomponent fibre increases bond point area above 25% and reduces wettability below acceptable acquisition rates, while less than 12% bicomponent fibre produces web delamination during downstream slitting. Compliance for hygiene nonwovens is governed by ISO 9001:2015 for quality management, REACH (EC 1907/2006) for chemical safety, and EDANA/INDA WSP 70.3 for liquid strike-through time; baby diaper ADL materials are additionally evaluated for cytotoxicity under ISO 10993-5 when marketed as medical devices.
| Blend ratio (PP/bicomponent) | Bonding route | Web mass | End product |
|---|---|---|---|
| 85/15 | Calender | 18-25 g/m² | Hygiene coverstock |
| 80/20 | Through-air | 20-40 g/m² | Acquisition/distribution layer |
| 70/30 | Through-air | 40-80 g/m² | Molding pad precursor |
Processing begins with high-speed carding at 60-100 m/min on a random card equipped with 0.5 mm chamfered wire. The blended fibre is opened in a fine opener, and the web is directed through a through-air bonding oven set at 135-145°C for PE sheath fusion; the actual melting threshold of the sheath is 128-132°C, while the PP core remains unmelted. If the oven temperature exceeds 150°C, the PP staple shrinks by 5-8% and produces non-uniform basis weight. The terminal product range includes diaper ADL strips, feminine hygiene coverstock, adult incontinence core wrap, and wound pads with acquisition layers. On production lines, batch-to-batch variation in bicomponent sheath melt index shifts the bonding window by ±5°C; this is the primary source of delamination failure during high-speed converting.
Thermoformable PP fibre mats replace bitumen-based acoustic inserts when vehicle platforms require adhesive-free assembly and incineration without halogen by-products. The fibre blend consists of 70-75% 1.5 denier 38 mm PP staple, 25-30% 2.0 denier PE/PP bicomponent binder, and optionally 5-10% PET staple for increased crush resistance. This formulation omits halogenated flame retardants; instead, compliance with FMVSS 302 is achieved by alkali-washed PP and a non-flammable polyolefin binder sheath. Acoustic absorption is measured in an impedance tube according to ISO 10534-2, and the target sound absorption coefficient in the 800-2500 Hz range is specified by the OEM. Thermal resistance is measured under ISO 11092; odour testing follows VDA 270; restricted substance compliance is documented under REACH (EC 1907/2006).
Processing requires air-lay or carded web formation to a mass per unit area of 500-1500 g/m², followed by through-air bonding in an oven zone at 130-140°C and then a cooling zone at 10-15°C with a residence time of 30-60 s to prevent blocking. The semi-rigid mat is reheated to 180-200°C in an infrared oven and cold-formed in a water-cooled mould at 25-40°C for 30-90 s. The critical processing threshold is the reheat window: below 175°C the PP/bicomponent mat will not conform to deep-draw radii under 80 mm; above 205°C the PP staple begins oxidative surface degradation, visible as yellowing and odour. Terminal products include engine bay acoustic panels, door panel absorbers, roof insulator pads, and dashboard firewall inserts.
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The designation 1.5 D × 38 mm polypropylene staple fiber identifies a melt-spun, drawn, crimped, and cut fiber produced from fiber-grade isotactic polypropylene homopolymer. The model string 1.5D*38mm encodes nominal linear density and cut length; supplier suffixes may identify spin finish chemistry, cross-section, optical-brightener content, crimp configuration, and color. The nominal linear density is 1.5 denier, equivalent to 1.67 dtex under the conversion factor 1.111 dtex/D. The cut length is 38 mm, with a common commercial tolerance of ±1.5 mm. The fiber is supplied in compressed bales with a spin finish applied at 0.10 %–0.30 % by mass. The standard spin finish is hydrophobic; a durable hydrophilic finish is specified separately for hygiene acquisition layers and wet-laid processes.
Feedstock melt mass-flow rate is typically controlled at 18 g/10 min–25 g/10 min at 230 °C and 2.16 kg load per ISO 1133-1:2022. The fiber is available in raw white, optical white, semi-dull, and solution-dyed grades; round cross-section is standard, while trilobal and hollow cross-sections are separate commercial variants. During staple production, melt-spun filaments are hot-drawn and stuffer-box crimped before cutting to 38 mm. Crimp frequency is typically 10–16 crimps per 25 mm when assessed by ASTM D3937. Lot-to-lot variation in crimp frequency outside this range influences carding cohesion and web cloudiness.
The 1.5D*38mm designation is a dimensional specification rather than a chemical identifier. Two suppliers may supply fiber with the same denier and cut length but different melt flow rate, spin finish chemistry, crimp geometry, antioxidant package, and optical brightener. These secondary properties determine carding speed, thermal bonding temperature, web tensile strength, and outdoor durability. Therefore, the dimensional designation alone does not establish fitness for a given nonwoven process.
End-use routes include carded thermal-bonded hygiene coverstock, needlepunched geotextiles, automotive interior substrates, air and liquid filtration media, acoustic insulation, and dry-laid wipes. The 38 mm cut length is compatible with roller-top carding, cross-lapping, air-laying, and wet-laying systems; the 1.5 D fineness increases fiber count per unit mass and supports uniform web formation at low basis weights.
Table 1 lists lot-level physical data. The values are supplier-lot typical ranges and must be confirmed against a certificate of analysis; they are not universal specification limits for all grades.
| Parameter | Test method | Typical range |
|---|---|---|
| Linear density | ISO 1973:2017 / ASTM D1577 | 1.50 ± 0.10 denier; 1.67 ± 0.11 dtex |
| Cut length | ISO 6989:1981 | 38 ± 1.5 mm |
| Tenacity | ISO 5079:2020 | 3.0–4.5 cN/dtex |
| Elongation at break | ISO 5079:2020 | 70–150 % |
| Density | ISO 1183-1:2019 | 0.90–0.91 g/cm³ |
| DSC melting peak | ISO 11357-3:2018 | 160–170 °C |
| Moisture regain | ASTM D2654 | <0.1 % |
| Crimp frequency | ASTM D3937 | 10–16 crimps per 25 mm |
| Spin finish content | Solvent extraction / gravimetric | 0.10–0.30 % by mass |
Thermal bonding of 1.5 D × 38 mm polypropylene staple occurs in a narrow temperature band because mono-component PP has a single melting endotherm. Differential scanning calorimetry per ISO 11357-3:2018 places the melting peak at 160 °C–170 °C. Calender and through-air ovens are operated with surface or air temperatures from 145 °C to 165 °C. Below 145 °C, surface melting is incomplete and web tensile strength is low; above 165 °C, the fiber forms film, web loft collapses, and bond-point shrinkage appears. The effective processing window can be as narrow as 5 °C. This is the principal difference from PE/PP bicomponent staple, which bonds at 130 °C–135 °C and tolerates broader temperature variation because the sheath polymer carries the adhesion.
On production calender lines, bond area is set by engraved roll pattern, nip pressure, and line speed. For a 20 g/m² coverstock, the process is typically limited by thermal transfer through the web thickness rather than by carding output. Residence time must be reduced when web bulk exceeds 50 g/m² to avoid core melting and surface film formation. Spin finish migration is a batch-sensitive variable: finish content above 0.30 % by mass can reduce calender bond-point adhesion and produce peeling during tensile testing according to ISO 9073-3. Reported production-scale carding experience indicates that doffer wrapper formation increases when spin finish falls below 0.10 % by mass. In needlepunch lines, the 38 mm staple is opened, carded, cross-lapped, and needled before thermal setting. Needle density and depth are set lower than for polyester because polypropylene has lower bending stiffness and a lower melting point; high needle speeds generate local frictional heating and surface fusion if needle parameters are not controlled.
Through-air bonding requires uniform air distribution. A temperature variation across the oven width greater than ±3 °C can produce regional web strength variation, especially at low basis weights. Calender roll surfaces are usually release-coated to prevent fiber sticking; PTFE and similar non-stick roll treatments are common. The polymer does not require pre-drying before carding because moisture regain is below 0.1 % per ASTM D2654, but static charging at relative humidity below 40 % can increase card web breaks unless ionizing bars or humidification are installed.
Polypropylene differs from polyethylene terephthalate staple in density, melting point, moisture regain, and degradation chemistry. PP density is 0.90 g/cm³–0.91 g/cm³, compared with 1.38 g/cm³ for PET. At equal denier and cut length, the lower density yields approximately 50 % more fiber per unit mass. The melting peak for PP is 160 °C–170 °C; PET requires processing or setting above 230 °C. Moisture regain for PP is below 0.1 % by ASTM D2654, while PET regain is approximately 0.4 %. PP is resistant to hydrolysis and to ambient aqueous acids and alkalis; PET undergoes hydrolytic degradation in wet heat above 70 °C in closed systems. Conversely, PP is more sensitive to thermo-oxidative degradation and UV exposure, and unstabilized grades embrittle after extended air aging above 90 °C.
Compared with PE/PP bicomponent staple of the same cut length, mono-component 1.5 D × 38 mm PP staple has a higher bonding temperature and a narrower window. Bicomponent fiber can be through-air bonded at 130 °C–135 °C because the PE sheath melts before the PP core. Mono-component PP is selected when a single melting endotherm is required for downstream thermal stability or when sheath-core morphology is not acceptable. Table 2 compares the product with same-denier PET staple and coarser PP staple.
| Parameter | 1.5 D × 38 mm PP staple | 1.5 D × 38 mm PET staple | 6 D × 64 mm PP staple |
|---|---|---|---|
| Density | 0.90–0.91 g/cm³ | 1.38 g/cm³ | 0.90–0.91 g/cm³ |
| Melting peak | 160–170 °C | 250–260 °C | 160–170 °C |
| Moisture regain | <0.1 % | ~0.4 % | <0.1 % |
| Fiber count per unit mass | high | medium | low |
| Dry-laid web mean pore size | smaller | small | larger |
| Thermal bonding window | 145–165 °C | not standard thermal bonding | 145–165 °C |
| Hydrolytic stability | resistant | sensitive in wet heat above 70 °C | resistant |
| UV stability without stabilizer | poor | moderate | poor |
Published data for this specific configuration is limited in open technical literature; the comparative values in Table 2 are typical supplier technical-bulletin data and must be verified for each lot.
When a dry-laid line switches from 6 D × 64 mm polypropylene staple to 1.5 D × 38 mm polypropylene staple, fiber count per unit mass increases by approximately 4 times at equal web density. The finer staple reduces mean pore diameter and increases specific surface area, which is exploited in air and liquid filtration media and in hygiene acquisition layers. In production carding trials, 38 mm staple generates fewer doffer wrappers than 51 mm or 64 mm staple on high-speed roller-top cards, but fine denier increases the number of fibers per unit area and may require lower lickerin and cylinder speeds to prevent static charging and fusion. Reported line data indicate that reducing carding speed by 10 %–20 % relative to coarse-denier settings is a common starting condition when switching to 1.5 D staple; the actual setting must be determined from web uniformity and fiber temperature, not from denier alone.
In needlepunched filtration substrates, the smaller cross-section of 1.5 D fiber yields tighter pore structures. Clean pressure drop increases if web density is held constant; to keep air permeability constant, basis weight or needling intensity can be reduced. Particle capture efficiency for 2 µm–10 µm particles is reported to improve with finer fiber in nonwoven filter media, but the effect is dependent on web density, pore-size distribution, and surface finish. Batch-to-batch crimp variation of ±2 crimps per 25 mm can shift web density and pressure drop; incoming crimp measurement is therefore recommended. For liquid filtration and hygiene acquisition layers, a durable hydrophilic finish changes strike-through and re-wet behavior; these properties should be tested by EDANA/INDA methods because standard spin finish is hydrophobic. Published data for this specific configuration is limited.
For sterile or outdoor nonwoven applications, polypropylene staple fiber is intrinsically hydrophobic, with moisture regain below 0.1 % by ASTM D2654. This eliminates pre-drying before carding and reduces biological growth risk in stored rolls, but it limits liquid absorption unless a hydrophilic finish or bicomponent fiber is incorporated. The fiber withstands aqueous acids and alkalis at ambient temperature and is not subject to hydrolytic degradation; however, it softens in chlorinated solvents and in some hot aliphatic solvents. Thermo-oxidative degradation is the main processing constraint. Continuous exposure above 90 °C in air consumes antioxidant additives and causes discoloration or embrittlement unless the polymer is stabilized for the intended service temperature.
Because the melting peak is 160 °C–170 °C, steam sterilization at 121 °C can produce shrinkage or bond-point creep in load-bearing nonwovens. Polypropylene is therefore specified less often for reusable medical devices requiring repeated autoclaving. For single-use nonwovens sterilized by ethylene oxide or gamma radiation, PP can be specified, but radiation doses above 25 kGy may initiate chain scission in unstabilized grades; lot-specific antioxidant documentation is required. Outdoor geotextiles require carbon-black or UV-stabilized grades; unstabilized PP loses tensile strength rapidly under ASTM D4355 xenon-arc exposure. Carbon-black content of 2 %–3 % by mass is common in UV-stabilized geotextile grades. Unfilled polypropylene has a limiting oxygen index near 17 %–18 % per ISO 4589-2, so automotive interior composites must be tested to FMVSS 302 or ISO 3795 and usually require flame-retardant treatment or lamination. Food-contact grades may reference 21 CFR 177.1520 or Regulation (EU) No 10/2011, but compliance is grade-specific and not implied by denier or cut length.
Material documentation should include a certificate of analysis covering linear density, cut length, tenacity, elongation, spin finish content, and DSC melting peak. Regulatory compliance to EU REACH Regulation (EC) No 1907/2006 and RoHS Directive 2011/65/EU is commonly declared in supplier documentation, but lot-specific verification is required because additive packages vary by grade. If the product is used in through-air bonded high-loft webs, the oven air temperature should not exceed 165 °C, and residence time must be reduced when web bulk exceeds 50 g/m² to avoid core melting and surface film formation.