| HS Code | 183788 |
| Product Name | Kuraray K-II WQ941 |
| Polymer | Water-soluble polyvinyl alcohol (PVA) |
| Fiber Form | Staple fiber |
| Dissolution Temperature | 95°C in water |
| Water Solubility | Completely soluble in water at 95°C |
| Tenacity | 8.8 cN/dtex |
| Elongation At Break | 7% |
| Youngs Modulus | 230 cN/dtex |
| Fineness | 1.4 dtex |
| Cut Length | 38 mm |
| Density | 1.26 g/cm³ |
| Color | White |
As an accredited Kuraray K-II WQ941-Water Soluble PVA Fiber (Dissolves at 95°C) factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | Available in 20 kg sealed moisture-proof bags. Water-soluble PVA fiber dissolves at 95°C; keep dry until use. |
| Container Loading (20′ FCL) | 20′ FCL: palletized cartons of Kuraray K-II WQ941 water-soluble PVA fiber securely loaded, ventilated, and container-sealed for transport. |
| Shipping | Ship Kuraray K-II WQ941 Water-Soluble PVA Fiber in sealed, moisture-resistant packaging to prevent premature dissolution. Avoid humid environments and direct water contact. Store dry at ambient temperature. Standard ground freight is suitable; no special hazmat classification required. Ensure containers remain intact during transit. |
| Storage | Store in a dry, cool, well-ventilated area away from direct sunlight, moisture, and temperatures exceeding 95°C. Keep sealed in original packaging or a tightly closed container to prevent humidity absorption. Avoid contact with water, solvents, and ignition sources. Maintain clean, dry conditions to preserve fiber integrity and dissolution performance. |
| Shelf Life | Shelf life is typically 2 years if stored sealed, cool, and dry, protected from moisture and direct sunlight. |
In wet-laid nonwoven production for embroidery stabilisers and soluble packaging webs, WQ941 is metered into the furnish as a polyvinyl alcohol fibre whose structural integrity is retained through sheet forming, pressing, and drying phases, then released only when the finished web is subjected to a sustained 95°C aqueous bath. The key process boundary is the differential between the fibre’s dissolution onset and the thermal profile of through-air or can drying; dryer shade temperatures above 85–90°C may initiate surface gelatinisation and cause fibre-to-fabric adhesion on the drying wire. The furnish is typically composed of 70–90 wt% wood pulp or cellulosic furnish and 10–30 wt% WQ941 cut length 3–6 mm, with the PVA portion adjusted upward when the final web must retain tensile strength during tensioned embroidery machine operation. Compliance for the nonwoven segment references ISO 9073-2:2018 for thickness, ISO 9073-3:2023 for breaking force, ISO 9073-6:2018 for absorbency time, and EDANA/INDA NWSP 010.4.R0 for basis weight. EU marketability requires REACH pre-registration or registration for polyvinyl alcohol fibre based on the parent polymer; food-contact soluble sachet applications fall under FDA 21 CFR 177.1670 and EU Regulation (EU) No 10/2011 when the PVA composition meets the specific migration limits for vinyl acetate monomer and acetaldehyde. Processing on an inclined-wire former is preferred over vertical gap formers because the high-water-retention PVA fibre increases sheet closure time and requires enhanced dewatering vacuum in the suction boxes; vacuum levels of −25 to −40 kPa are commonly maintained in the low-vacuum boxes, while the dandy roll must be run at low nip pressure to prevent fibre crushing. After forming, drying is staged with first-stage can temperatures of ≤70°C, second-stage 80–85°C, and a final stage not exceeding 88°C, because the dissolution onset is time-temperature dependent and the residence time on the final dryer group is the main factor controlling premature solubility. Terminal products include embroidery backing rolls of 35–80 g/m², water-soluble sachet webs for hardware packaging, and dissolving interliners for technical textiles.
Addition of WQ941 to specialty paper furnish occurs at 1–5 wt% on dry furnish, most frequently via the machine chest or fan pump inlet to minimize fibre breakage from prolonged centrifugal pump shear. The fibre functions initially as a synthetic carrier fibre that increases wet-web tensile during transfer from the forming wire to the press section, but its solubility at 95°C allows near-complete removal in subsequent aqueous coating or impregnation steps when the papermaker seeks a highly porous, short-fibre sheet with reduced synthetic residue. This is particularly relevant in low-grammage condenser paper, teabag tissue, and release base papers where the presence of insoluble synthetic fibre would degrade die-cut edge cleanliness or off-taste migration. The addition ratio must remain below 5 wt% because higher loadings create stiff fibre bundles at the slice jet and reduce formation index on the machine direction. The grade is evaluated against ISO 5269-2:2004 for Rapid Köthen handsheets, ISO 1924-2:2008 for tensile properties at constant rate of elongation, ISO 536:2019 for grammage, and TAPPI T 412 cp-12 for moisture. Papers intended for indirect food contact are evaluated under FDA 21 CFR 176.170 and BfR Recommendation XXXVI for paper and board; dissolution residue testing is performed using a series of 95°C water extractions followed by gravimetric analysis according to ISO 1762:2019 for residue on ignition. On the paper machine, the stock pH is maintained between 5.5 and 7.5 because strongly alkaline conditions can accelerate PVA fibre swelling and cause press roll picking. Headbox consistency of 0.8–1.2 wt% and slice jet-to-wire speed ratio of 1.00–1.03 are typical for short synthetic fibre stock to avoid fibre flocculation. The press section is operated at a linear pressure of 50–80 kN/m in the first press and 90–120 kN/m in the second press; excessive press impulse causes fibre flattening and lowers the final extraction porosity after the dissolution step. Drying is staged at 60–70°C in the main section, then 80–88°C in the final cylinders, with lower final moisture targets of <8% to reduce microbial issues and to preserve fibre dissolution characteristics. Terminal products include heat-sealable teabag tissue, security paper with time-consuming fibre-to-fibre bonding, and release base papers where residual PVA below 0.5 wt% is required.
WQ941 is converted into water-soluble sewing thread by ring spinning from 100 wt% PVA staple with a fibre length of 51 mm and a linear density of 1.1–1.7 dtex, typically to a final yarn count of Ne 20/1 to Ne 40/1. For temporary twistless roving or support yarn blended with cotton, the WQ941 content is 5–20 wt% to limit fibre loss during pre-dissolution processing. The thread is used as basting yarn in garment assembly, as temporary stitching in sock toe closure, and as separation yarn in jacquard weaving. The critical processing boundary is the hygroscopic swelling of PVA yarn in high-humidity sewing rooms; at relative humidity above 65%, yarn tensile strength declines and needle breakage increases, so the thread must be conditioned at 20±2°C and 55±5% RH for at least 24 h before use. In garment dyeing or finishing, the thread is removed by immersion in an aqueous bath held at 95°C for 15–30 min under agitation; the bath must contain sufficient overflow to flush dissolved PVA polymer from the fabric surface, because re-deposition during cooling forms a clear film on polyester or cotton dyed substrates and reduces apparent colour yield. Yarn tensile testing follows ISO 2062:2009 with a gauge length of 500 mm and a constant rate of extension of 500 mm/min. Colour fastness to washing is evaluated under ISO 105-C06:2010 using test condition D3S, which provides a 70°C washing environment that must not dissolve the thread during normal wet processing. Oeko-Tex Standard 100 Annex 4 certification applies to the converted yarn. For apparel sold to EU markets, REACH Annex XVII restrictions on vinyl acetate monomer and formaldehyde content in polyvinyl alcohol are relevant; finished yarns are tested by EN ISO 14184-1:2011 for free formaldehyde and by EN 71-3:2019 for extractable elements when intended for children’s garments. Spinning uses a roller drafting system with apron spacing of 2.0–2.5 mm and spindle speed of 8,000–10,000 rpm. Twisting is performed on a two-for-one twister with 600–800 tpm for yarns destined for chain stitching. The temporary support yarn is typically inserted as a plating yarn or as a separate stitch row without stitching tension above 18–22 cN because higher tension causes premature PVA fibre fibrillation and thread breakage at the needle. Terminal products include basting thread for tailor’s chalk seams, toe-closure thread in hosiery, and separable knitting yarn for fully fashioned garments; after the dissolution step, the final garment must be rinsed at 60°C to remove residual PVA film, followed by cold water rinse to prevent gelatinous deposits on drain screens.
Contaminated linen isolation in healthcare and cleanroom operations uses water-soluble PVA nonwoven fabricated from 80–100 wt% WQ941 fibre and 0–20 wt% low-melting synthetic binder fibre, with a basis weight of 25–50 g/m². The bag must retain tear resistance at ambient temperature and humidity while exposed to wet soiled textiles, then dissolve when the washing machine reaches 95°C in the sluice cycle. This is a sharp performance cliff: if the wash programme plateaus at 85–90°C for more than 10 min, the fibre may soften but not fully disperse, leading to pump impeller fouling and residual film on linen. The nonwoven is produced by carding the fibre blend, cross-lapping to 2–4 layers, and hydroentangling at 80–120 bar water jet pressure; seam construction uses heat sealing or PVA stitch yarn instead of polyester thread, because any insoluble seam thread will block the washing machine drain. Compliance is anchored to ISO 16604:2004 for resistance to penetration by blood-borne pathogens for protective clothing, EN ISO 9073-2:2018 for thickness, ISO 9073-3:2023 for breaking strength, and EN 14065:2016 for laundry contamination control. Bags used for medical waste are assessed under ISO 15223-1:2021 for symbol marking, and the dissolved PVA concentration in the wastewater is managed according to the plant’s biological oxygen demand permit limits because PVA has a slow biodegradation rate in conventional activated sludge compared to cellulosic fibres. Carding is run at 40–55°C and 45–55% RH to prevent static charging; the fibre has a crimp frequency of 11–15 crimps per 25 mm which is sufficient to maintain web cohesion without additional finish. Hydroentangling pressure above 120 bar can cause local fibre fibrillation but does not impair dissolution. Terminal products include single-chamber sluice bags, double-ply transport sacks for infectious linen, and gusseted bags for surgical drapes with capacities from 10 L to 60 L; maximum load is limited to 10 kg because wet laundry above that mass can exceed the wet tensile strength of the PVA web before washing.
WQ941 staple is introduced into composite preform manufacture at 2–8 wt% of the reinforcing fibre mass as a temporary binder fibre that permits net-shape layup of carbon or glass fibre tapes prior to resin infusion. The fibre remains dimensionally stable during ambient-temperature vacuum bagging and low-temperature cure cycles up to 80°C, but dissolves when the cured laminate is held in a 95°C water bath for 60–120 min, creating internal voids or hollow channels where the PVA fibre had been placed. Published data for this specific configuration is limited; however, the general principle follows from the fibre’s solubility profile and laboratory extraction coupons rather than from production-scale aerospace qualification programmes. The main process conflict is that the PVA fibre softens near 80–85°C, so autoclave cycles or resin systems with exothermic peaks above that temperature can cause premature fibre collapse, closing the hollow channel before extraction. Tooling must therefore be designed with a controlled exotherm profile; thermocouple data from the laminate show that the peak exotherm should not exceed 78°C if the PVA fibre is to retain its geometry. The addition ratio is limited to 8 wt% because higher loadings create continuous PVA networks that are slow to extract and can leave residue at the void boundary; residual PVA is measured by ISO 1762:2019 ash residue after soaking at 95°C for standard duration. For the composite sector, mechanical testing of the fibre-containing laminate before extraction follows ASTM D3039/D3039M-17 for tensile properties and ASTM D2344/D2344M-22 for short-beam shear. The PVA fibre itself is evaluated by ISO 2062:2009 for tensile elongation and ISO 306:2022 for Vicat softening. REACH compliance is required for the European market; polyvinyl alcohol is generally considered non-hazardous, but the vinyl acetate monomer content must remain below the residual limit defined in the substance registration dossier rather than under a harmonised Annex XVII entry. For aerospace or automotive qualification, the resin system must be shown to be compatible with PVA extraction water; the extract solution is tested for pH and total organic carbon before discharge. Terminal products include prototype hollow composite ducts, intake manifolds, and non-structural sacrificial core sections where the channel geometry is defined by the PVA fibre placement rather than by a removable metal mandrel.
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Kuraray K-II WQ941 is a water-soluble polyvinyl alcohol staple fiber specified for high-temperature dissolution at 95°C in water. The product belongs to the K-II family of polyvinyl alcohol fibers, CAS 9002-89-5, manufactured by wet spinning and drawing into a controlled crystalline structure that restricts solubility below the thermal threshold. It is normally supplied as cut staple in lengths of 4 mm or 6 mm and linear densities from 1.4 dtex to 1.7 dtex, with exact values reported on the lot certificate of analysis. The fiber remains intact in aqueous processing below approximately 80°C and dissolves only after sufficient residence at or above 95°C. This property creates a processing window for wet-laid nonwovens, papermaking, and other converters that require a temporary fiber phase.
Compared with warm-water PVA grades that dissolve at 70–80°C and cold-water grades that dissolve below 60°C, WQ941 tolerates higher wet-end temperatures, heated dryer cans, and hot-water showers without premature fiber loss. Standard non-water-soluble Kuralon polyvinyl alcohol fiber is used as a permanent reinforcing phase and does not dissolve. The K-II WQ941 grade is therefore selected when the process stream runs above 50°C but extraction can be performed with boiling or near-boiling water. Published grade-specific data for all water-soluble K-II subgrades is limited; grade selection should be confirmed by controlled bath testing under the target temperature-time profile.
On a pilot Fourdrinier wet-laid line with headbox stock temperature controlled at 45–55°C, WQ941 can be blended with cellulose, glass, or synthetic staple at addition levels from 2 wt% to 10 wt% without measurable dissolution. The slurry can be held in pulpers and machine chests for 20–40 min without headbox consistency drift or increased filtrate chemical oxygen demand. Anionic or nonionic retention aids are preferred; strongly cationic polyelectrolytes may bridge the partially hydrolyzed fiber surface and reduce dispersion quality. Vacuum dewatering and wet pressing at linear loads up to 80 kN/m do not harm the fiber geometry because the web temperature remains below the thermal threshold. On multicylinder dryer cans, surface temperatures may reach 120°C, but the fiber remains intact because web moisture content drops quickly and dry heat does not solvate the polyvinyl alcohol phase. Extraction is then conducted in a separate bath or shower at 95–98°C with residence time from 30 s to 5 min, depending on basis weight, water turnover, and mechanical turbulence.
High-shear dispersion should be limited to the minimum energy required to separate fiber bundles. Excessive refining at high temperature fibrillates the fiber surface and increases the surface area, which can make the apparent dissolution onset appear below the nominal 95°C threshold. The stock should not be recirculated through centrifugal cleaners for more than 15 min at temperatures above 60°C unless the system is designed to handle dissolved polymer accumulation.
| Fiber class | Nominal dissolution temperature | Wet-end survival envelope | Typical function | Extraction condition |
|---|---|---|---|---|
| Kuraray K-II WQ941 | 95°C | Aqueous exposure up to 80°C for short residence; dry heat to 120°C | Sacrificial binder, pore former, template fiber | Hot water at 95–98°C with agitation |
| Warm-water water-soluble PVA grade | 70–80°C | Aqueous exposure up to approximately 50°C | Temporary binder where extraction heat is limited | Hot water at 70–80°C |
| Cold-water water-soluble PVA grade | <60°C | Ambient only | Rapid release, embroidery backing, low-temperature dissolution | Water at 20–40°C |
| Standard Kuralon PVA fiber | Insoluble | No dissolution limit | Permanent reinforcement, structural nonwoven bonding | Not applicable |
After the sheet has been resin-bonded, thermally bonded, or hydroentangled, the sacrificial PVA phase is removed to create a controlled void network. Extraction should be arranged countercurrently to prevent redeposition of dissolved PVA as the bath cools. Bath PVA concentration can be monitored by total organic carbon analysis or by a colorimetric boric acid-iodine complex method, with the method selected according to the site discharge permit. The extraction step is often the rate-limiting operation on converting lines because low bath agitation or insufficient overflow can leave residual PVA that reduces final porosity and air permeability.
As a dissolved species, PVA raises chemical oxygen demand in the extraction bath. For a hypothetical line producing 10,000 m²/day of 50 g/m² web with 5 wt% WQ941, the input fiber mass is approximately 25 kg/day. The extraction bath overflow and any downstream biological treatment must be sized for this organic load; otherwise bath viscosity increases and washing efficiency falls.
In hydroentanglement with water-jet manifolds operating at 80–90°C, WQ941 provides temporary support to the fiber web only if the cumulative time-temperature exposure remains below the dissolution induction period. The control variable is the integral of jet temperature and residence time across all manifolds, recirculation loops, and wash boxes. At 85°C, partial surface dissolution may begin after several minutes, forming a PVA-rich boundary layer that raises recirculated water viscosity and can deposit on perforated drums. Lower-temperature water-soluble PVA grades would not survive this operation because their dissolution onset lies within the jet temperature band. To avoid defects, the water system should be operated with overflow bleed to limit dissolved solids, and the fiber should be validated in pilot trials with the specific jet pressure, drum speed, and manifold configuration. After entanglement, the web transfers to an extraction bath at 95–98°C where the fiber dissolves and is removed through overflow.
Removable PVA fiber forms have also been used in composite preforms to create microchannels or void networks after matrix cure. WQ941 can be laid into a carbon or glass preform, subjected to resin infusion, and extracted after cure with heated water. The process requires the cured matrix to be sufficiently open to water transport and dimensionally stable at the extraction temperature. Anhydride-cured epoxy systems with glass transition temperatures above 110°C are generally more suitable than flexible or low-Tg matrices. Published data for this specific configuration is limited, and cure exotherms above 180°C may alter PVA crystallinity and reduce the subsequent dissolution rate.
Borate ions form reversible covalent complexes with vicinal diol units on the PVA chain and can gel the fiber surface or the extraction bath. Borax-containing retention aids, starch additives, or process water with elevated boron are incompatible unless the ratio and pH have been validated. Gelation can occur at low borate concentrations, particularly at alkaline pH and higher molecular weight. Processing pH is typically maintained between 4 and 9; outside this band the acetate functionality and surface charge shift, altering dispersion stability and dissolution behavior. Polyvalent cations such as Fe3+ and Al3+ should be controlled because they can bridge carboxylate/acetate sites and induce agglomeration. Storage is recommended below 65% relative humidity at 20–25°C. The fiber is hygroscopic, with moisture regain at 65% RH of approximately 4–5%. Material that has absorbed excess moisture should be dried at 105°C to constant mass before blending to avoid bridging in screw feeders and nonuniform dispersion.
Bales are typically supplied as compressed sheet-wrapped units in the range of 100–200 kg, sealed in moisture-barrier film. The bales should be conditioned in the production hall for 24 h before opening to prevent condensation on the fiber surface. Once opened, the fiber should be consumed within the shift schedule specified by the facility because moisture uptake can alter electrostatic behavior and make web formation less uniform.
Water-soluble PVA fiber grades generally exhibit lower dry tenacity than non-water-soluble Kuralon reinforcement grades because the reduced crystallinity required for solubility also reduces load-bearing capacity. Supplier literature for water-soluble PVA staple commonly reports dry tenacity in the range of 3 cN/dtex to 5 cN/dtex and elongation at break of 15–25%, but these values are grade-dependent and should be taken from the certificate of analysis. The fiber should not be exposed to prolonged dry heat above 160°C, because discoloration and embrittlement may occur before any dissolution-related failure. For operations involving through-air dryers or infrared panels, the web surface temperature should be checked with an infrared pyrometer rather than inferred from the air setpoint.
Fiber diameter can be estimated from linear density and PVA density. At 1.4 dtex and a polyvinyl alcohol density near 1.28 g/cm³, the nominal filament diameter is approximately 12 μm. This geometry is useful in filtration media because the extracted pore width is initially defined by the fiber diameter. However, wet pressing and drying collapse and consolidate the web, so final pore size must be measured by capillary flow porometry such as ASTM F316 rather than inferred from fiber diameter alone.
No. Alkaline conditions can accelerate surface swelling and dissolution of water-soluble PVA, particularly at temperatures above 60°C. Cementitious boards, mortar reinforcement, and structural fiber-cement applications require non-water-soluble Kuralon or another high-tenacity PVA fiber. WQ941 is intended for neutral to mildly acidic process waters; if the process stream contains sodium hydroxide or other alkalinity above pH 9, a laboratory immersion test is required before production. The high-pH aqueous phase in cement pore water can also react with acetate and hydroxyl functionality, making the fiber unsuitable for permanent alkaline service.
| Parameter | Standard or method | Notes |
|---|---|---|
| Linear density | ISO 1973:2021, ASTM D1577 | Reported on certificate of analysis as dtex |
| Cut length | ISO 6989 | Staple length distribution; sieve method |
| Single-fiber tensile properties | ISO 5079:2020, ASTM D3822/D3822M-14 | Dry tenacity and elongation at break; water-soluble grades may require low-strain-rate control |
| Dissolution temperature | Internal controlled-bath method | No harmonized ISO/ASTM method; report temperature-time profile |
| Moisture regain | ISO 6741-1 | Equilibrium at standard atmosphere |
| Ash content | ISO 3451-4 | Residue after combustion; used to monitor spin-finish content |
| Biodegradability | OECD 301B, ISO 14851 | Polyvinyl alcohol is biodegradable under aerobic aqueous conditions; confirm specific grade |
| Food-contact status | 21 CFR 176.170, 21 CFR 176.180, EU Regulation 1935/2004 | End-use confirmation is required; PVA may be permitted for specific paper/paperboard applications |
| REACH registration | EC 1907/2006 | Polyvinyl alcohol is a registered polymer; verify SVHC status with supplier certification |
Retention of water-soluble PVA fiber is influenced by cut length and the presence of surface finish. Long 6 mm fibers provide greater wet-web tensile strength but increase the risk of wrapping around rolls or forming fabric contamination. Short 4 mm fibers disperse more easily in low-consistency headbox stock. The choice should be matched to the forming section configuration and the target sheet basis weight. At basis weights below 30 g/m², the shorter cut length is preferred to reduce pinholing. Sheet air permeance after extraction can be characterized by ISO 5636-3 for paper and board or ISO 9073-15 for nonwovens.
For food-contact or medical packaging applications, the converter must not assume that the dissolution temperature establishes suitability. The extracted PVA is normally removed from the finished web; residual PVA content should be quantified by extraction followed by total organic carbon analysis or a validated colorimetric procedure. If residual PVA remains in an article intended for skin contact, the finished article must meet the relevant migration limits under the applicable jurisdiction. Textile embroidery backing and support yarns represent an additional use class, but WQ941 is appropriate only when the downstream washing process is conducted at or above 95°C. Many textile finishing operations run at 60–80°C; in those conditions a lower-temperature water-soluble grade is more appropriate because WQ941 would leave undissolved residue. The high dissolution temperature becomes a process defect if the substrate cannot tolerate boiling-water baths without dimensional change.