2.2 dtex (2.0D)×38/51mm PP Staple Fiber for Thermal Bonded Nonwoven

    • Product Name: 2.2 dtex (2.0D)×38/51mm PP Staple Fiber for Thermal Bonded Nonwoven
    • Factroy Site: Donghai County Economic Development Zone, Jiangsu Province
    • Price Inquiry: sales1@liwei-chem.com
    • Manufacturer: Jiangsu Botao New Material Co Ltd
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    Specifications
    HS Code 660360
    Product Name 2.2 dtex (2.0D) × 38/51 mm PP Staple Fiber for Thermal Bonded Nonwoven
    Material Polypropylene
    Fiber Type Staple fiber
    Linear Density 2.2 dtex
    Denier 2.0D
    Cut Length 38 mm or 51 mm
    Crimp Number 8-12 crimps/25 mm
    Crimp Ratio 10-15%
    Tenacity 2.5-3.5 cN/dtex
    Elongation At Break 100-200%
    Melting Point 160-170 °C
    Density 0.90-0.91 g/cm³
    Moisture Regain ≤0.1%
    Thermal Bonding Temperature 130-150 °C
    Color White
    Fiber Cross Section Round
    Surface Finish Thermal bonding compatible finish
    Chemical Resistance Good against acids, alkalis, and solvents
    Uv Resistance Good

    As an accredited 2.2 dtex (2.0D)×38/51mm PP Staple Fiber for Thermal Bonded Nonwoven factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing 2.2 dtex PP staple fiber packed in 250 kg compressed bales, PP woven fabric wrapped, strapped; 20 bales per 40HQ container.
    Container Loading (20′ FCL) 20′ FCL: 2.2 dtex (2.0D) × 38/51 mm PP staple fiber for thermal bonded nonwoven, bale-packed, approx. 13–15 MT.
    Shipping 2.2 dtex (2.0D) × 38/51 mm PP staple fiber for thermal bonded nonwoven is non-hazardous and not regulated for transport. It is compressed into bales, wrapped in PP woven bags/film, strapped, palletized, and loaded into dry containers. Keep dry, avoid moisture, oil, sunlight, and contamination. Store in a ventilated warehouse.
    Storage Store in a clean, dry, well-ventilated warehouse at ambient temperature, away from direct sunlight, rain, moisture, and heat or ignition sources. Keep original packaging sealed and palletized, off the floor and away from walls. Avoid contact with strong oxidizers, acids, and oils. Use first-in, first-out; prevent crushing, prolonged heavy stacking, UV degradation, and static buildup. Ensure good housekeeping.
    Shelf Life Recommended shelf life: 12 months under normal storage conditions in original packaging, cool, dry, ventilated, away from sunlight and moisture.
    Application of 2.2 dtex (2.0D)×38/51mm PP Staple Fiber for Thermal Bonded Nonwoven

    Calendered Coverstock in Disposable Hygiene Lines

    On high-speed carded lines producing hydrophobic coverstock at 2400–3600 mm working width, the 2.2 dtex (2.0 D) × 38 mm PP staple fibre is selected when the converter prioritizes lower web defects over maximum softness. Compared with 1.7 dtex fibre, the 2.2 dtex filament cross-section reduces card cylinder wrap and fly, but it also lowers fibre count per gram and increases mean pore diameter. When the 51 mm cut is substituted onto the same card, machine-direction tensile rises but card loading increases; the measurable outcome on a double-doffer card at ≥650 m/min cylinder surface speed is a higher nep count and greater web weight variability across the cross-machine profile. Compliance baseline for hygiene coverstock supplied into the EU market is OEKO-TEX Standard 100 Annex 6 product class I, with additional converter audits requiring nonwoven lot release against ISO 9073-2:1995 for tensile and ISO 9073-1:1989 for basis weight. REACH Annex XVII restrictions on PAH content apply when post-industrial recycled PP is introduced into the blend; virgin polymer with documented supplier declaration is preferred for skin-contact layers. The fibre addition ratio in final web is either 100 % by fibre mass for standard 18–28 g/m² thermal-bonded coverstock, or 25–35 wt% of the 2.2 dtex grade blended with 65–75 wt% of 1.3 dtex soft-touch fibre. In the blend, the 2.2 dtex fraction functions as the thermal bonding backbone because its higher melt mass per filament creates larger bond sites at equivalent calender pressure; lowering the 2.2 dtex share below 20 wt% produces a measurable decline in web tear strength and increases pinhole defects after embossing. Downstream production is carding, crosslapping where specified, and heated calender point bonding. Calender roll surface temperature is maintained at 148–153 °C with engraved bond area 16–19 % and linear pressure 60–90 N/mm. Finished forms include urine acquisition layer carrier tissue, leg-cuff nonwoven, femcare pad coverstock, and ADL support scrim; the 38 mm grade is typically not used for 3D embossed top sheets because the coarser filament diameter reduces emboss pattern sharpness.

    In medical face-mask outer-ply and isolation gown lamination lines, the 2.2 dtex × 38 mm PP staple fibre web is calendered as a reinforcing facing against a meltblown polypropylene mid-layer rather than used as an exposed absorbent structure. The outer ply is typically run at 22–28 g/m² and 100 % PP by fibre mass. When the same fibre is used as one layer in a three-layer SMS composite, the staple facing is reduced to 40–55 wt% of the final laminate, with spunbond and meltblown layers contributing the remainder. Compliance is evaluated under EN 14683:2019 for bacterial filtration efficiency and differential pressure; for gowns, EN 13795:2019 and AAMI PB70:2012 liquid-barrier classification govern the laminate rather than the fibre alone. Cytotoxicity testing is performed according to ISO 10993-5:2009, skin irritation to ISO 10993-10:2010, and latex-free verification is recorded because calender roll release agents can introduce trace contamination. A conformance matrix is provided below.

    Medical facing web conformance parameters
    Evaluated propertyTest designationTypical limiting value
    Bacterial filtration efficiency, Type I maskEN 14683:2019≥95 %
    Differential pressure, Type I maskEN 14683:2019<29 Pa/cm²
    CytotoxicityISO 10993-5:2009No lysis
    Skin irritationISO 10993-10:2010No erythema/oedema

    Downstream production on standard carded lines includes web formation at 60–100 m/min, two-roll heated calender point bonding at 143–150 °C, inline corona treatment to raise surface energy to 38–44 mN/m, and rotary ultrasonic edge sealing at 30–35 kHz. A documented failure mode on high-humidity shifts is web wrapping at the calender entry due to condensation on the fibre finish; conditioned fibre moisture above 0.35 % by weight reduces splice strength and increases static decay time. Finished products include surgical mask outer shells, procedure mask facings, isolation gown back panels, disposable cap base layers, and emergency-use respirator outer covers where the staple fibre layer is not the primary filter medium.

    Why Does the 38 mm Staple Grade Outperform 51 mm in Automotive Air-Laid Preforms?

    Automotive nonwoven converters run air-laid or carded crosslapped preforms for acoustic insulation where staple length directly controls loft retention. The 2.2 dtex × 38 mm PP fibre is favoured over 51 mm in air-laid preforms because the shorter cut length reduces fibre roping during silo discharge and improves density distribution in high-loft mats. On a production-scale air-lay machine, the 51 mm cut gives higher tensile strength but also a wider basis-weight coefficient of variation; the 38 mm cut typically narrows cross-direction basis-weight variation to ±3 % at 800 g/m² when fibre finish is held above 0.10 % by mass. Formulation addition ratio in firewall and wheel-arch insulation is commonly 65–80 wt% 2.2 dtex PP staple fibre blended with 20–35 wt% 6.7 dtex hollow or recycled PET. In luggage compartment high-loft panels, PP content falls to 50 wt%, with bicomponent binder fibre added to maintain thermal bond integrity and PET filler to increase recoverable compression. The 2.2 dtex PP fibre remains the carrier because of its elongation before break, which permits the preform to be compressed in heated tooling without tearing. Compliance requirements are set by vehicle manufacturers rather than a single global standard; baseline flammability is evaluated under FMVSS 302 and ISO 3795:1989, where the burn rate must be <100 mm/min on a 100 mm mark. VOC and FOG emissions are assessed by VDA 278:2011, with individual OEM limits applied; odour testing follows VDA 270:2018 because PP fibre can carry thermal oxidation by-products from upstream compounding. REACH Annex XVII applies to any recycled PET fraction introduced. Downstream processing starts with bale opening, carding, crosslapping into 300–800 g/m² batts, and through-air oven bonding at 158–165 °C for 45–90 s. The web is then compression-moulded at 170–190 °C into automotive preforms, die-cut, and finished with polyamide scrim if required. Finished part types include wheel arch liners, trunk side trims, engine bay firewall insulators, under-dash pads, A/B/C pillar insulation, and under-carpet acoustic backboards.

    Where the production line is configured for pleated panel filters and cabin air prefilter media, the 2.2 dtex × 51 mm PP staple fibre is not used as the high-efficiency layer; its role is to form a low-pressure-drop prefilter that protects the meltblown or electrospun layer from dust cake impaction. On a commercial filter converting line, the carded PP web is calendered at low bond area to preserve tortuosity, because overbonding above 14 % bond area creates film-like zones that raise pressure drop without improving dust-holding capacity. Formulation addition ratio for the prefilter is 100 % PP staple fibre at 100–180 g/m²; when pleat stiffness is required, 60–70 wt% PP is blended with 30–40 wt% recycled PET fibre. The 51 mm length is selected when pleat retention after scoring is a parameter, whereas 38 mm is used for thin, flexible prefilter layers. Filter media compliance is classified under ISO 16890:2016 as coarse to ePM10, not as high-efficiency; automotive cabin filter test methods follow ISO 11155-1:2001 for particle removal and differential pressure. REACH Annex XVII limits apply to any recycled PET input. Downstream production includes carding, crosslap or inline feed, belt calendering at 145–155 °C, belt preheating to 120–130 °C before calender entry, and then pleating at 25–35 mm pleat pitch. A production-scale bottleneck occurs when web moisture exceeds 0.3 %, causing steam blowholes at the calender nip and variable pleat geometry. Finished product types include cabin air filter prefilters, commercial HVAC coarse panels, paint booth intake mats, and respirator prefilter wraps.

    When Thermal Calendering Replaces Latex Bonding in Mattress Insulation Nonwovens

    In mattress border wrap and upholstery cushion interliner programmes, latex binder removal is driven by VOC control and by the need to avoid cellulose degradation in humid storage. The 2.2 dtex × 51 mm PP staple fibre enters the formulation as the melt-fusion component, but it is not a flame barrier. The fibre is dosed at 20–35 wt% of total fibre mass, combined with 40–60 wt% flame-retardant rayon, 10–25 wt% polyester, and 0–5 wt% bicomponent fibre. Exceeding 35 wt% PP raises the fibre-melt drip area during open-flame testing and reduces char integrity; dropping below 20 wt% produces weak sheet integrity and delamination after mattress compression cycles. Compliance for the finished interliner is tested to 16 CFR 1633 for full-mattress open-flame performance, 16 CFR 1632 for cigarette smoulder, and BS 5852:2006 ignition source scheduling where the product is exported to the UK. Upholstery applications are additionally assessed under California TB 117-2013 smoulder criteria. The nonwoven sheet itself is tested for tensile loss after heat ageing at 70 °C for 96 h, but published data for this specific PP grade in FR rayon blends is limited; converter trials typically establish lot-specific retention values before full production. Downstream processing uses a carded crosslapper to build 200–400 g/m² batts, followed by through-air oven bonding at 155–162 °C with a dwell of 60–90 s. The web is then cooled below 45 °C before rotary-knife cutting to prevent deformation. A process conflict on mixed-fibre lines is finish dilution: FR rayon can strip lubrication from PP fibre, so inline static control and monitoring of finish-on-fibre below 0.08 % are necessary to prevent card wrap. Terminal forms include mattress border wrap, spring insulator felt, upholstery cushion wrap, furniture deck pad, and bed base dust cover.

    For bituminous roofing carrier web production, the 51 mm cut is normally selected because the longer staple increases cross-machine tensile after needle-and-thermal prebonding, while the 2.2 dtex filament diameter preserves enough closed area to limit bitumen bleed-through during coating. The carded carrier is run at 120–200 g/m²; 100 % PP staple fibre is used when low water absorption is required, but in high-tear self-adhesive membranes the PP fraction is reduced to 60–75 wt% with 25–40 wt% polyester fibre, with the PP function shifting to thermal matrix and dimensional stabiliser. Compliance is structured around EN 13707:2018 for flexible sheets for roofing waterproofing, supported by EN 12311-1:1999 for tensile properties, EN 1849-1:1999 for thickness, and EN 1109:2013 for cold bend temperature. When the membrane is intended for contact with drinking water in some civil structures, additional member-state approvals apply; published data for this specific fibre grade in potable-water contact roofing systems is limited and must be verified at the converter level. Downstream processing includes bale opening, carding, crosslapping, pre-needling at 80–120 punches/cm², then inline thermal bonding at 150–160 °C. The bonded carrier is coated with oxidised bitumen at 170–180 °C; prolonged exposure above 180 °C induces shrinkage in the PP fibre and must be controlled by line speed interlock. Finished products include bituminous roof underlayment, SG tinned roofing membrane carrier, self-adhesive waterproofing membrane reinforcement, and bridge tunnel waterproofing base sheet.

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    Certification & Compliance
    More Introduction

    The fibre designated 2.2 dtex (2.0 D) × 38 mm or 51 mm is a monocomponent polypropylene staple fibre for dry-laid thermal-bonded nonwoven production. The linear density is normally controlled to ±0.15 dtex by a vibroscopic method such as ISO 1973, while cut length is verified by single-fibre measurement according to ISO 6989 or an equivalent producer internal method. The filament mass places the product between finer 1.7 dtex hygiene coverstock grades and coarser 6.7 dtex high-bulk or needle-punched grades. Polypropylene feedstock with a melt flow rate in the 12–20 g/10 min range at 230 °C under 2.16 kg load, measured to ISO 1133-1:2022, is used where calender bonding must give controlled polymer flow into the engraved bond points without excessive carding stiffness. Typical fibre mechanical data fall in the range of 2.8–3.8 cN/dtex tenacity and 180–350 % elongation at break measured at 20 mm gauge length under ISO 5079, with crimp frequency of 10–14 crimps/25 mm for card cohesion.

    Why does 2.2 dtex filament mass govern thermal bond point morphology?

    Bond point morphology in calender bonding is determined by filament count per unit area, contact area at the embossed roll, and melt viscosity under compression. At a web basis weight of 22 g/m², a 2.2 dtex fibre yields a substantially higher filament count than 6.7 dtex and a lower count than 1.7 dtex. The individual fibre diameter is approximately 20–21 µm for a polypropylene density of 0.905–0.915 g/cm³. Because heat transfer from the calender roll to the fibre core scales with the inverse of fibre radius, the 2.2 dtex filament reaches the crystalline melting range faster than coarser polypropylene staple at the same roll surface temperature. In contrast, the monocomponent structure contains no lower-melting sheath material. A bicomponent polyethylene/polypropylene fibre can form a bond at 120–130 °C while preserving the PP core; the 2.2 dtex monocomponent fibre must be processed near the polypropylene melting range and therefore presents a narrower thermal window. If the web enters the nip with local basis-weight variation above ±10 %, thin areas can overbond and thick areas can remain insufficiently fused, producing non-uniform tensile release under ISO 9073-3.

    On a nonwoven card running with main cylinder surface speeds of 600–1,200 m/min, the staple must bend repeatedly around worker and stripper rolls without static cling, cylinder wrap, or transfer loss to the doffer. The spin finish on the product is formulated as a low-fogging, antistatic lubricant, typically applied at 0.15–0.30 % by mass on fibre. Finish levels below 0.10 % can produce static-charged web at low ambient humidity; levels above 0.40 % may leave a boundary lubricant film on the calender embossments and reduce bond point strength. Storage and bale opening are recommended at 18–25 °C and 45–60 % relative humidity. Condensation on bale surfaces above 65 % RH can transfer through the bale opener and create transient fibre wrap on the card. Fibre crimp is applied after spinning to improve card cohesion; for this grade a crimp frequency of 10–14 crimps/25 mm is common, but excessively high crimp can generate web buckling at cross-lapper infeeds above 150 m/min.

    A narrow calender window defined by melting temperature and nip dwell time

    At the calender nip, monocomponent polypropylene fibre bonds only when the fibre surface enters the crystalline melting range but before the entire filament collapses into a film. Oil-heated or induction-heated steel rolls for this product are commonly set to surface temperatures of 153–163 °C, with nip pressure of 40–80 N/mm and a nip dwell time of 0.002–0.008 s depending on roll diameter and line speed. The upper boundary is the onset of film formation. Above 165 °C, the polymer can spread across the engraved bond point, reducing air permeability and drape; above 168 °C, thermal-oxidative degradation may generate low-molecular-weight residues and visible yellowing. The lower boundary is incomplete surface melting: webs bonded below 150 °C often fail by fibre pull-out rather than cohesive polymer fracture in tensile testing under ISO 9073-3. Melt flow rate also shifts the practical set point; a 12 g/10 min fibre requires a higher calender temperature than a 20 g/10 min fibre at equivalent pressure and speed. The usable window for a given calender roll and engraved pattern is therefore frequently narrower than ±5 °C. Published data for a specific engraved roll configuration is limited, so line trials are required to establish the upper limit before film formation for each pattern and basis weight.

    Process operators monitor the calender by bond point peel rather than visual gloss alone. A peel curve generated at 5 °C intervals shows a steep rise in tensile strength between 150 °C and 158 °C, followed by a plateau and then a strength drop when the bond points embrittle or the web develops pinholes. The exact plateau width depends on the engraved roll pattern, roll hardness, and polymer MFR. In production trials, a 20 g/10 min MFR fibre at 22 g/m² basis weight may require lower temperature than the same basis weight at 12 g/10 min; however, the higher-MFR fibre can also produce more roll wrap on downstream idlers if the web is not fully quenched.

    When 38 mm staple is chosen over 51 mm staple on an existing high-speed card

    Because cut length determines how the fibre exits card clothing and accumulates in the web, a change from 51 mm to 38 mm can be used to reduce cylinder wrapping and improve uniformity at high card speed. The shorter staple produces a higher fraction of fibre ends per unit mass, which lowers the mean free length between card wires and can reduce entanglement on worker rolls at speeds above 150 m/min. The trade-off appears in the bonded web: at the same basis weight and bond pattern, 38 mm staple typically gives lower machine-direction tensile strength than 51 mm staple because fewer filaments bridge the distance between adjacent bond points. In cross-direction testing, the difference is smaller because cross-lapper orientation controls load transfer. For hygiene coverstock and topsheet applications, 38 mm is often specified where softness and card productivity dominate; for medical packaging, mattress backing, or furniture decking where tensile integrity under load is critical, 51 mm is selected. When the cut-length specification is changed, card settings such as cylinder-to-doffer spacing, licker-in speed, and cross-lapper profile must be revalidated because the fibre population in the web changes even though the denier remains 2.2 dtex.

    Relative to polyester staple, the 2.2 dtex polypropylene fibre can be thermally bonded without a bicomponent sheath and has a lower density of 0.905–0.915 g/cm³, which provides a yield advantage of approximately 30–40 % over PET at equal basis weight. The continuous-use ceiling is lower: polypropylene thermally bonded webs are generally rated for prolonged exposure only up to 90–110 °C, whereas PET withstands higher service temperatures. The PP surface has a moisture regain below 0.05 % by mass, which is useful for hydrophobic barrier and filtration applications but complicates post-treatment if hydrophilic durability is required. Compared with a PE/PP bicomponent staple, the monocomponent 2.2 dtex fibre is intrinsically recyclable as a single-polymer web and avoids the cost of a sheath resin, but its calender window is narrower because no 120–130 °C melting sheath is available to create a bond while protecting the core fibre. Compared with finer 1.7 dtex polypropylene staple, the 2.2 dtex product gives slightly lower filament density and therefore a somewhat stiffer hand at equal basis weight; compared with 6.7 dtex, it gives higher surface area, smaller pore size, and a softer but thinner web at the same unit mass.

    Thermal-bonding oil finish, fume extraction, and fabric property tests

    The finish package for thermal-bonded polypropylene staple is selected to balance card lubrication and calender residue. Long-chain ethoxylated surfactants can volatilize or degrade at calender temperatures above 150 °C; a low-volatility finish with thermogravimetric mass loss below 15 % at 200 °C is preferred for high-speed lines. On-line fume extraction is sized for the calender exhaust rate, and the embossed roll surface is periodically cleaned when bond point gloss increases or when release strength declines. Fabric samples should be tested for basis weight to ISO 9073-1, thickness to ISO 9073-2, and tensile-elongation to ISO 9073-3. Hygiene and medical converters usually add proprietary wet tensile, friction, and linting requirements because these values depend strongly on bond pattern, basis weight, and post-treatment; no universal specification is attached to the fibre alone. For flammability-sensitive applications, the finished web is evaluated under the final-product standard such as ISO 12952 or 16 CFR 1610, not from fibre composition alone.

    The product is supplied in compressed bales of 200–350 kg with a polyolefin wrap, and visual defect levels are controlled by weigh-pan sampling and card web inspection. Incoming laboratories verify linear density by ISO 1973, cut length by ISO 6989, crimp frequency, finish-on-fibre, and melt flow rate after solvent extraction of finish under ISO 1133-1:2022. Because the product is monocomponent polypropylene, it can be calendered, ultrasonic welded, or thermally embossed after web formation, but it is not a low-temperature binder for cellulosic pulp blends: the calender temperature required to soften the PP surface can thermally damage cellulosic material if papermaking pulp exceeds 30 % by mass. The resin may be supplied against 21 CFR 177.1520 for olefin polymers, but food-contact status of a finished nonwoven requires migration testing under Regulation (EU) No 10/2011 because spin finish and process additives are not automatically covered by the resin compliance. Autoclave exposure at 121 °C requires validation of dimensional stability because polypropylene approaches its heat deflection temperature under load, and the fibre is not recommended where the finished article is subjected to continuous steam service. Published data for the specific bond-temperature shift in cellulosic blends is limited; pilot calender trials are required.