| HS Code | 310721 |
| Brand | Kuraray |
| Grade | K-II WN241 |
| Generic Type | PVA (polyvinyl alcohol) fiber |
| Solubility Type | Low-temperature water soluble |
| Dissolution Temperature | 20°C |
| Chemical Family | Vinyl polymer / polyvinyl alcohol |
| Physical Form | Staple fiber |
| Fineness | 1.7 dtex (typical) |
| Cut Length | 3 mm to 12 mm (typical) |
| Color | White |
| Odor | Odorless |
| Specific Gravity | Approximately 1.26-1.30 |
| Tensile Strength | Approximately 8-10 cN/dtex |
| Elongation At Break | Approximately 15-25% |
As an accredited Kuraray K-II WN241-Low-Temperature Water Soluble PVA Fiber (Dissolves at 20C) factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | Available in 20 kg sealed bags: Kuraray K-II WN241 low-temperature water-soluble PVA fiber, dissolving at 20°C, ready for use. |
| Container Loading (20′ FCL) | 20′ FCL loading of Kuraray K-II WN241 PVA fiber: moisture-proof, dry集装箱, secure palletized units, safe handling for low-temperature water-soluble product. |
| Shipping | Ship as non-hazardous dry fiber in sealed moisture-barrier packaging. Protect from humidity, rain, condensation, and direct water contact, since it dissolves at 20°C. Keep cool, dry, and ventilated. Avoid compression or abrasion during transit. Label “Keep Dry” and store away from liquids. |
| Storage | Store in a cool, dry, well-ventilated area, away from moisture, humidity, water sources, and direct sunlight. Keep container tightly sealed when not in use to prevent dissolution or clumping. Avoid exposure to temperatures exceeding 20°C without controlled conditions. Protect from physical damage and separate from incompatible materials or ignition sources. |
| Shelf Life | Store in a cool, dry place away from moisture. Shelf life is typically two years from date of manufacture. |
Wetlaid nonwoven lines that convert K-II WN241 into cold-water-dispersible hygiene substrates operate within a narrow whitewater-temperature envelope because the fiber begins losing structural integrity at 20°C. In mill practice, the dry-furnish addition ratio generally ranges from 5 wt% to 20 wt% of total fiber mass, depending on the required balance between converting strength and dispersibility. Loadings below 10 wt% yield handle and wet tensile derived chiefly from cellulose, while loadings above 15 wt% shorten slosh-box disintegration time but may increase headbox foaming if surfactant levels are not adjusted. Compliance for finished flushable nonwovens in the EU and North America is typically assessed against EDANA/INDA GD4 guidance using methods FG501.2, FG502.2, FG503.2, and FG504.1, with supplemental physical testing per ISO 9073-3:2019 for wet and dry tensile and ISO 9073-6:2017 for absorbent capacity.
On a commercial angled-wire wetlaid former, the furnish is prepared at a headbox consistency of 0.2–0.5% with a pH of 6.0–8.0. The K-II WN241 cut length of 6 mm is dispersed with a low-dose anionic polyacrylamide retention aid and a nonionic defoamer; vacuum suction boxes are modulated to 1.5–3.0 kPa to avoid premature fiber loss. Hydroentangling manifolds are generally operated below 18°C because pump enthalpy and jet strip friction can raise whitewater temperature by 2–4°C over a six-hour campaign. If the water temperature exceeds 20°C, partially dissolved PVA forms a colloidal film on the wire and causes streaking, higher drainage resistance, and off-spec basis weight variation. Drying is carried out on through-air or flatbed through-air dryers with zone temperatures between 110°C and 140°C; the dry fiber remains stable because dissolution requires free water, but residual moisture at the dry end above 12% can initiate surface tackiness during roll winding. Terminal products include dispersible cleaning cloths, adult hygiene wipes, and personal care wipe substrate that must retain wet tensile during storage and disintegrate after flushing.
| Test protocol | Scope | Application on dispersible wipe substrate |
|---|---|---|
| EDANA/INDA GD4 FG501.2 | Slosh-box disintegration | Finished roll immersion under controlled water turbulence |
| EDANA/INDA GD4 FG502.2 | Household drain-line transport | Column or pipe-flow clearance after flush release |
| ISO 9073-3:2019 | Wet/dry tensile strength | Wet tensile after 5 min soak and dry tensile at roll slitting |
| ISO 9073-6:2017 | Liquid absorption capacity | Absorbency of finished nonwoven before converting |
| ISO 5269-2:2004 | Laboratory sheet formation | Furnish optimization for fiber retention and formation |
At loadings above 20 wt%, sheet densification from PVA film formation can reduce liquid strike-through time and create surface slickness; manufacturers should validate slosh-box and household drain-line protocols on every roll because basis weight and binder distribution vary with whitewater loop solids. Storage of fiber bales requires conditioned warehousing at 45–60% RH and below 35°C; fiber exposed to humidity above 70% RH can partially plasticize and generate bale splitting or blocking.
In infection-control laundry logistics, K-II WN241 is converted into nonwoven bag materials that must maintain mechanical integrity during soiled-linen handling and then dissolve without residue in the wash cycle. Addition ratios in drylaid or wetlaid bag webs typically fall between 20 wt% and 40 wt% of total web mass; the upper limit is constrained by seam strength and cost, while the lower limit is driven by the need to prevent open seams when a bag is lifted by a 25 kg wet load. The relevant compliance framework includes EN 14065:2016 for risk analysis and bioburden control in laundry-processed textiles and ISO 15797:2018 for industrial wash testing, with seam tensile measured under ISO 9073-3:2019. Most institutional laundry machines operate at 20–25°C for the first rinse; therefore a bag must start dispersing at 20°C or below, not merely after a heated wash stage.
Production typically uses a carded nonwoven line with K-II WN241 cut length of 12 mm for dry strength and a meltable PVA or water-soluble adhesive seam tape for ultrasonic or thermal seam closure. Web formation is followed by compacting calender rolls set to 60–80°C and 80–120 N/mm² nip pressure to reduce loft and prevent tearing during filling; basis weight is commonly 30–50 g/m². During bag filling, the seam must resist tensile failure from wet linen at ≥20 N/50 mm, but the same seam must disappear in cold water. Process validation uses a standard front-loading washer at 20°C, with a wash load of 20–30 kg, water volume of 100–150 L, and agitation for 5–10 min; the bag is visually inspected for residual film on the drum perforations, and wash water is tested for PVA concentration. Terminal products include soluble bags for hospital bed linens, isolation gown collection bags, and transit packaging for infectious textiles that is placed directly into the washer drum.
An operational boundary exists in the presence of borate ions in the detergent or fabric conditioner; borate crosslinks PVA and can delay or prevent bag dissolution at 20°C. Therefore facility validation must include the actual laundry chemical dosing profile. If the washhouse uses ozone or high-pH peroxide stages after the initial rinse, any PVA residue should be cleared before those stages because partially swollen PVA can re-adhere to textiles and create stiff spots. Published data for bag disintegration across all washer brands is limited; converters should run a washer-specific qualification protocol under EN 14065:2016 before changing suppliers or bag basis weight.
For cold-water removable embroidery backings produced as monocomponent PVA webs, K-II WN241 occupies the entire fiber fraction or nearly all of the web because the backing must vanish without leaving a residue on heat-sensitive face fabrics. A monocomponent wetlaid or carded web of 100 wt% K-II WN241 with a cut length of 6–8 mm is typical for lightweight backings below 40 g/m²; blended versions containing 10–20 wt% of a higher-dissolution-temperature PVA grade are used to raise stiffness for dense stitch counts on automated multi-head embroidery machines. Compliance for skin-contact finished garments is generally handled through OEKO-TEX Standard 100 product class II calibration, while wash cycles for assessing removal are specified under ISO 6330:2012 with a wash temperature not exceeding 25°C.
Production machinery consists of a carding line or inclined-wire wetlaid former, followed by light calendering at 70–90°C and 40–60 N/mm² nip pressure to consolidate the web without creating a dense film that slows dissolution. The sheet is slit to hoop sizes for standard embroidery frames; stitch densities above 20,000 stitches/m² require a higher basis weight or blended PVA to resist needle deflection. After embroidery, the fabric panel is passed through a spray-rinse or drum rinse station with water at 20–25°C and a flow rate of 8–12 L/min per hoop width; static soak tanks below 15°C can extend dissolution times beyond 3 min and leave gel residue in satin stitch channels. Terminal products include backing for lace appliqué, badge embroidery, embroidered emblems, and delicate silk or wool garment panels where a hot-water soluble backer would cause thermal damage.
The critical processing boundary is residual PVA after rinse; a hand-feel test under ISO 6330:2012 is not sufficient for white or pastel fabrics, so a near-UV inspection stage may be added to detect translucent PVA film under a 365 nm lamp. Avoid combining K-II WN241 backings with cationic softeners or reactive alkaline pre-treatments before dissolution because cationic species can form insoluble complexes on the fiber surface. If the embroidery is to be treated with a durable water-repellent finish, the backing should be removed before finishing rather than after, because fluorocarbon or silicone films block water ingress and inhibit dissolution.
When a hollow tubular woven structure requires a temporary weft that vanishes without heat, K-II WN241 is often used as a 100 wt% water-soluble spun or filament yarn in counts ranging from 20 tex to 40 tex. For core-spun or plied constructions in which the PVA yarn is intended to supply temporary bulk, the PVA fraction is usually 30–50 wt% of total yarn mass, with the remainder being cotton, viscose, polyester, or nylon. The governing yarn tensile standard is ISO 2062:2009; mill release specifications commonly require a conditioned tenacity of 5–8 cN/tex and elongation at break of 10–18% at 65% RH.
Production flow uses ring spinning or rotor spinning on conventional cotton or wool spinning frames; the PVA staple is pre-conditioned to 50–60% RH because at moisture above 12%, fiber-fiber cohesion increases and ends-down rates rise. In weaving, the PVA yarn is inserted as a temporary weft on rapier or projectile looms at tensions between 15 cN and 25 cN; single-yarn lubrication with a nonionic antistat is required to reduce abrasion at reed impact. After fabric formation, the greige fabric is passed through a cold-water wash at 20–25°C for 2–5 min, optionally with a nonionic non-foaming wetting agent at 0.2–0.5 g/L; mechanical squeeze rolls remove dissolved PVA before drying. The process is validated by weighing a marked tracer yarn before and after washing, with residual mass below 2% of original PVA mass as a typical release criterion. Terminal products include hollow tubular tapes for medical bandages, spacer fabrics with internal channels, drop-stitch textile preforms, and openwork geotextiles.
The operational boundary is that K-II WN241 yarn loses tenacity above 70% RH, so high-humidity weaving rooms in coastal mills should install dehumidification. In addition, PVA yarn cannot be used with starch sizes that require hot water removal because the PVA itself solubilizes during desizing, changing fabric geometry before the warp size is fully removed. Published data for PVA yarn residual mass after cold-water extraction across all loom types is limited; therefore initial production trials should isolate the PVA yarn from permanent yarns to quantify dissolution efficiency under the exact wash-box configuration.
Historically, water-dispersible paper grades relied on carboxymethyl cellulose or water-soluble binders, but K-II WN241 provides a dry fibrous network that has enough tensile strength for converting and disappears under cold water. In specialty paper furnishes, the addition ratio is 1–5 wt% of total dry furnish when the fiber is used as a temporary strength aid during formation and drying; in water-dispersible label or security paper, the loading may reach 5–15 wt% to force sheet disassembly on soaking. The relevant physical test methods are ISO 1924-2:2008 for tensile properties, ISO 535:2023 for Cobb water absorbency, and TAPPI T 494 om-22 for wet tensile retention. If the paper is intended for indirect food contact, compliance may also require FDA 21 CFR 176.170 or EU EC 1935/2004 migration documentation, depending on the converter's regulatory route.
On a Fourdrinier paper machine, K-II WN241 cut to 6 mm is added to the pulper after refining to avoid excessive fiber damage; headbox consistency is maintained at 0.3–0.6%, and the pH is controlled between 6.0 and 7.5. Wet pressing is run at 80–100 kN/m linear pressure, and drying cylinders are set below 130°C to avoid melting or yellowing the PVA fibers. Because PVA fibers become sticky at high moisture, a dryer-section moisture profile below 8% at the reel is required to prevent sheet breaks at calender stacks. The finished paper may be surface sized with a water-soluble grade of PVA to balance ink receptivity; however, permanent wet-strength additives such as melamine-formaldehyde or polyamidoamine-epichlorohydrin resins are incompatible with the water-dispersible requirement. Terminal products include water-soluble labels, dissolvable security papers, temporary document substrates, and cold-water-delaminated release bases for printed transfer systems.
The process conflict in this application is refining energy. If the PVA fibers are over-refined, they fibrillate and entangle with cellulose fines, which delays disintegration and creates a slimy broke when re-pulped. Mill studies recommend adding PVA after refining and limiting subsequent agitation to 15–20 min in the machine chest. If the paper contains furnish from recycled fibers with high ash content, the PVA loading should be shifted toward the upper limit of 5–15 wt% because ash weakens the dry web and may require more binder to survive slitter operations.
Soil-contact seed carriers built around K-II WN241 use the 20°C dissolution threshold as the agronomic trigger for seed release when irrigation or soil moisture reaches the root zone. In wetlaid seed tapes, the K-II fiber loading is typically 10–25 wt% of the carrier furnish, with cellulose powder or tissue-grade pulp supplying the remainder; higher loadings above 25 wt% can reduce soil oxygen exchange after dispersal. Environmental safety testing follows OECD 208:2006 for seedling emergence and early growth and ISO 11269-2:2012 for higher plant response, while the PVA polymer must be registered under REACH EC 1907/2006 with appropriate biodegradation data from OECD 301B or 302A if required by the importing jurisdiction.
The carrier is formed on a wetlaid inclined wire machine at basis weights between 20 g/m² and 40 g/m²; seeds are deposited between two wet-formed sheets and pressed with a low-nip calender at 50–70°C. Slitting to row widths of 2–5 cm is conducted with optical registration to avoid cutting the seed pockets. In the field, the tape is placed in the furrow at 10–25 mm depth and covered; irrigation water at or above 20°C dissolves the fiber and releases the seed within minutes, while cooler water below 15°C softens but does not fully dissolve the matrix, which can delay emergence by 1–3 days in cold soils. Terminal products include vegetable seed tapes for leafy greens, carrot and radish strips, herb garden mats, and turf repair carriers.
The agronomic boundary is soil pH below 4.0 or above 9.0, where PVA dissolution kinetics may shift and require a higher proportion of cellulosic fibers to prevent film-forming residues. Seed treatments containing high doses of ionic micronutrients, especially borates, should be avoided in the carrier layer because borate crosslinks PVA and can retard release. Published field data for K-II WN241-specific seed carriers is limited; therefore greenhouse emergence trials under OECD 208:2006 should precede full-field use in each target soil type.
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Kuraray K-II WN241 is a low-temperature water-soluble polyvinyl alcohol staple fibre designated for dissolution at 20 °C. The grade belongs to the K-II series, in which the polyvinyl alcohol backbone is fibre-formed and processed to retain sufficient amorphous character for solvation in ambient water. Lot-specific documentation for WN241 typically includes linear density, cut length, dry tenacity, elongation at break, dissolution onset temperature, finish content, and visible residue limits; because numerical values vary with cut length and downstream conversion, the manufacturer’s certificate of analysis is the controlling specification. Single-fibre tensile evaluation is normally conducted under ISO 5079:2020. Fibre linear density can be measured under ISO 1973:2021, and bulk density can be reported under ISO 1183-1:2019, with polyvinyl alcohol fibre density generally in the range 1.26 g/cm³ to 1.30 g/cm³. The defining distinction from conventional K-II grades is that the deliberate dissolution step requires only cold water at 20 °C rather than heated tanks, steam tunnels, or high-temperature rinse stages. That behaviour shifts the critical control point from wash-water energy input to the prevention of uncontrolled moisture contact during storage, air conveying, and wet-laid forming.
The dissolution mechanism is physical solvation of the fibre matrix rather than chemical degradation. At 20 °C, water molecules penetrate the amorphous regions, disrupt interchain hydrogen bonding, and progressively disentangle the crystalline domains. Because the process is temperature-dependent, stock water only a few degrees above the dissolution onset can initiate fibre surface solvation before the intended bonding or removal stage. This is the principal operational conflict in wet-laid applications: cold-water solubility provides low-energy removal but reduces the thermal window for forming and pressing. Process water should therefore be maintained below 18 °C in furnish lines where the fibre must remain intact until drying. Once the web reaches the dryer section, the dissolution temperature is not a boundary in dry air; however, condensation on machine frames, felt edges, or suction boxes can generate local wetting. Production-scale experience on Fourdrinier and inclined wire equipment indicates that stock temperature, felt moisture, and white-water solids must be monitored as a single control loop when WN241 is used as a temporary binder.
The primary storage limit is condensation. At 20 °C and 65 % relative humidity, the dew point is approximately 14 °C. If bale or carton surfaces are stored in a warehouse where night-time air temperature falls below that dew point, surface condensation can initiate partial dissolution even though the bulk fibre appears dry. Polyvinyl alcohol fibres typically show moisture regain in the range 3 % to 5 % at 20 °C and 65 % relative humidity; WN241’s low dissolution onset lowers the practical humidity threshold. Sealed packaging with desiccant inserts, storage at relative humidity below 60 %, and avoidance of dew-point cycling are therefore required before fibre is delivered to the opening line.
In pneumatic conveying, compressed air with a pressure dew point above 10 °C is a known incompatibility. Moisture in the conveying stream can condense in bends or on cooler fibre surfaces, causing fibre clumping, build-up on card clothing, and variable feed to the web former. Air handling for WN241 should use desiccant dryers or refrigerated dryers with pressure dew point below 4 °C when ambient intake air exceeds 20 °C and 50 % relative humidity. Opening and blending equipment should be enclosed and supplied with dehumidified air to prevent hygroscopic uptake during extended stops. If pre-drying is required, it should be performed with dehumidified air whose wet-bulb temperature remains below the fibre’s dissolution onset when residual moisture is present; published data for this specific configuration is limited, and lot-specific storage and handling instructions should be applied to automatic bale openers, weigh-pan blenders, and card feed chutes.
In aqueous furnish systems, borate-based wet-strength additives and boric acid/borax buffer systems are documented gelation agents for polyvinyl alcohol. Addition of WN241 to a fibre slurry containing borate ion can produce gel networks that raise viscosity and reduce dewatering. Compatibility jar testing should be conducted at the intended stock temperature and pH before full-scale introduction.
In wet-laid nonwoven and specialty paper operations, K-II WN241 is metered into the furnish as a temporary binder or spacer fibre at addition levels specific to the substrate and target dry strength. When the fibre dissolves at 20 °C, the polymer transfers to the aqueous phase and can deposit on cellulosic fibres during drying, forming interfibre bonds without a heated dissolution step. The dosage range must be controlled because excess dissolved polyvinyl alcohol raises white-water viscosity, reduces drainage at the forming section, and contributes to felt filling on downstream presses. Bench-scale drainage tests using a Schopper-Riegler apparatus under ISO 5267-1 or a dynamic drainage jar can establish the maximum addition level before freeness drops below the machine requirement. On a Fourdrinier line, stock temperature above 18 °C reduces the dry fibre fraction before the couch roll; control is commonly maintained by chilled water makeup or plate heat exchangers on the white-water silo. If the forming fabric receives warm stock above 20 °C, dissolved fibre may penetrate the wire, accumulate on suction boxes, and cause streaking in the wet web.
The use of WN241 in hydroentangled nonwovens as a removable support fibre follows a different risk profile. In this configuration, the fibre may be present in a carded web, and low-temperature dissolution allows support removal after hydroentangling without exposing the structure to elevated water temperature. However, the hydroentanglement water system itself must operate below 20 °C when fibre integrity is required; if recirculated water rises above the dissolution onset, fibre loss in the filter and water treatment loop increases. Dissolved polyvinyl alcohol in process water can raise chemical oxygen demand load, which must be managed in the plant’s effluent treatment system. A closed-loop filtration system with dissolved air flotation or ultrafiltration is typically used when high addition levels are specified.
In embroidery base materials, water-soluble sewing threads, and temporary separation yarns, the replacement of hot-water removal with 20 °C dissolution is applied where the surrounding fibre, coating, or membrane cannot withstand thermal stress. Polyester and polypropylene substrates that are dimensionally stable below 60 °C may be processed without the dryer temperature ramp or extended autoclave cycle used for higher-temperature PVA fibre grades. The removal step requires mechanical agitation and sufficient water exchange; stagnant cold water will reach saturation with dissolved polymer and slow further dissolution. For a woven or nonwoven structure containing WN241, the dissolution time is controlled by fibre accessibility, water flow, and dissolved polymer concentration rather than by water temperature alone. Laboratory verification should use a flow-through immersion cell or cascading rinse bath with water at 20 °C, a liquor ratio of at least 100:1, and a defined agitation rate. Residual fibre inspection after washing should be performed optically at 10x magnification to detect short fibre remnants trapped at yarn intersections. Fabric tensile properties can be evaluated under ISO 13934-1:2013, and dimensional stability can be measured under ISO 6330:2021 where the supporting textile is intended to survive the wash cycle.
Compared with standard K-II grades that require warmer water, WN241 reduces the probability of thermal shrinkage in the surrounding textile structure, but it narrows the humid storage tolerance as already described. In blended yarn applications, the fibre should not be exposed to steam setting, autoclave conditioning, or hot water dyeing before the intended removal stage. Even brief contact with steam above 20 °C can cause surface tack and filament bonding. For this reason, yarn slashing and preparation must use dry or ambient conditions; splitting guides and tension rollers should be kept free of condensation. The difference between WN241 and conventional PVA fibres is therefore not limited to dissolution temperature; it is a process boundary that constrains every aqueous step upstream of the final wash.
Incoming inspection of K-II WN241 should verify dissolution onset at 20 °C, fibre length distribution, finish content, and visible gel particles. Because the product is low-temperature soluble, sample conditioning must occur in a desiccated environment; otherwise moisture gain during weighing distorts fibre property measurements. Tensile tests under ISO 5079:2020 should be performed on fibres conditioned for 24 h at 20 °C and 65 % relative humidity only if the dissolution onset is not exceeded; the standard conditioning atmosphere is at the boundary of the product’s solubility, so sample handling time should be limited. The dissolution test method is typically a gravimetric or optical residue method in which a known fibre mass is immersed in demineralized water at 20 °C under controlled agitation; complete dissolution is recorded when residue falls below a specified percentage. Published data for this specific configuration is limited, and the manufacturer’s certificate should define the acceptance threshold.
Regulatory documentation for the fibre typically covers REACH Regulation (EC) No 1907/2006, Directive 2011/65/EU (RoHS), and site-level management standards. Table 1 summarises the standard document set requested for industrial qualification.
| Compliance domain | Designation | Documentation requested |
|---|---|---|
| Quality management | ISO 9001:2015 | Production site certificate and batch traceability |
| Environmental management | ISO 14001:2015 | Site certificate or audit report |
| Chemical registration | REACH Regulation (EC) No 1907/2006 | Safety data sheet and substance registration number |
| Hazardous substances | Directive 2011/65/EU | RoHS declaration for restricted substances |
Table 2 positions WN241 among water-soluble PVA fibre classes by dissolution onset and operational constraint. The comparison is based on general K-II temperature classes, not alternative lot-specific grades; the user should verify the exact grade code and dissolution temperature on the certificate of analysis.
| Fibre class | Dissolution onset | Removal environment | Main process boundary |
|---|---|---|---|
| K-II WN241 | 20 °C | Ambient water, no heated wash | Condensation and stock temperature below 18 °C |
| Higher-temperature K-II classes | Warm-water and hot-water ranges | Heated wash tanks or steam chambers | Energy input and residence time at temperature |
| Conventional non-water-soluble PVA grades | Not applicable | Not removable by aqueous dissolution | Permanent reinforcing function |
The operational boundary where WN241 is inappropriate is any process that exposes the fibre to free moisture above 20 °C before the intended dissolution point. This includes high-humidity ambient storage, warm white-water loops, steam-assisted web forming, and hot calendering with moisture present. The product should not be combined with borate-based additives or hot melt extrusion where pre-swelling or gelation can occur before controlled removal. When these constraints cannot be maintained, a higher-temperature water-soluble PVA fibre or a non-soluble structural fibre should be selected. Published data for WN241-specific denier and cut length is limited; qualification must include pilot trials on the intended production line to determine addition level, drainage impact, and removal efficiency before conversion to full-scale manufacture.