| HS Code | 305597 |
| Product Name | Kuraray VPB105-1 PVA Binder Fiber for Paper Making (Dissolves at 70°C) |
| Base Material | Polyvinyl alcohol (PVA) |
| Fiber Form | Short-cut staple fiber for wet-laid papermaking |
| Dissolution Temperature | 70°C in water |
| Solubility Behavior | Insoluble in cold water and organic solvents; fully dissolves in hot water at 70°C |
| Typical Fineness | 1.1 dtex (customizable from 1.0 to 2.0 dtex) |
| Typical Cut Length | 3 mm to 6 mm depending on papermaking requirements |
| Specific Gravity | Approximately 1.26–1.30 g/cm³ |
| Mechanical Properties | Tensile strength about 5 cN/dtex; elongation roughly 15–20% as PVA staple |
| Binding Mechanism | After dissolution in the wet web at 70°C, the PVA film forms upon drying, creating strong bonds with cellulose fibers |
As an accredited Kuraray VPB105-1-PVA Binder Fiber for Paper Making (Dissolves at 70°C) factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | Supplied in 20 kg moisture-protective, polyethylene-lined paper bags with clear labeling for safe handling and storage. |
| Container Loading (20′ FCL) | Load 20′ FCL with palletized, wrapped PVA binder fiber bales, blocked to prevent shifting, keeping dry and away from heat/moisture. |
| Shipping | Ship Kuraray VPB105-1-PVA Binder Fiber in sealed, moisture-proof packaging to prevent premature dissolution or clumping. Store away from heat sources and humidity; transport at ambient temperature, below 70°C. Avoid extreme pressure, sharp objects, and wet conditions. No special hazard classification expected for standard dry handling. |
| Storage | Store in a cool, dry, well-ventilated area, away from moisture, direct sunlight, and heat sources. Keep the original container tightly sealed to prevent humidity absorption and premature dissolution. Avoid contact with water or temperatures above 70°C. Ensure good housekeeping and protect from physical damage. |
| Shelf Life | Shelf life is typically two years when stored in a cool, dry place away from moisture and direct sunlight. |
Kuraray VPB105-1 is a polyvinyl alcohol binder fiber for wet-laid papermaking in which the bonding function is thermally triggered at 70°C. The fiber remains discrete during pulping, refining, and sheet formation; only after the web reaches the dissolution threshold in the dryer does it mobilise as a binder film. This separation of formation and bonding controls the grade-specific process limits described below.
In wet-laid filter media for HVAC panels and engine intake elements, the furnish is prepared from softwood kraft pulp, polyethylene terephthalate staple fiber, and Kuraray VPB105-1 at an addition level of 6–14 wt% based on dry solids. The binder fiber is cut to 3–6 mm so that its length approximates the number-weighted mean fiber length of the refined pulp. If the cut length exceeds 8 mm, production-scale inclined-wire formers show rope formation in the headbox and uneven basis weight across the cross direction. Stock temperature is held at 30–45°C; the dissolution temperature of 70°C is therefore not reached until the sheet enters the first through-air drying zone. Addition below 5 wt% produces a measurable loss of dry tensile index in a 60 g/m² sheet when tested according to ISO 1924-2:2008, while addition above 16 wt% causes PVA film bridges over pores and reduces air permeability below the target band for fine particulate filtration. The permeability is screened with ISO 5636-5:2013; thickness and tensile energy absorption follow ISO 534:2011 and ISO 1924-2:2008. On high-speed pleating lines, internal bond failure at the pleat apex is the dominant defect. That failure is reduced when the sheet is dried with a first-zone air temperature of 75–90°C and a dwell time of 5–15 s, which permits the PVA fiber to dissolve and form a film around fiber intersections. If the first zone remains below 70°C, the binder remains fibrous and internal bond measured by a Scott bond tester remains unchanged from the control.
The finished media are subsequently converted into cabin air filters evaluated under ISO 16890:2016 and engine intake elements tested using ISO 5011:2014; the binder system must not contribute extractables that increase engine intake fouling. Wet-end pH is maintained between 6.5 and 8.0, because alkaline pH above 9.0 causes premature swelling of the PVA fiber and deposit formation on forming fabrics. The first dryer section must exceed 70°C quickly enough to activate the binder, but rapid steam generation within the sheet must be avoided by controlling the initial air dew point. End products include pleated HVAC panel filters, cabin air cartridges, and heavy-duty engine intake panels, where the PVA binder contributes to pleat stiffness and dust-loading stability rather than filtration efficiency itself.
Abrasive backing paper formed on a cylinder or Fourdrinier machine requires high internal bond before it is saturated with phenol-formaldehyde resole resin, because the wet resin bath swells the sheet and exposes loose fiber ends. VPB105-1 is added at 4–10 wt% to bleached softwood kraft containing minimal fines; the furnish is refined to a freeness of 25–40 °SR to keep the sheet open while the dissolved PVA provides surface consolidation. The first dryer section is operated at cylinder surface temperatures of 75–95°C, which triggers fiber dissolution and spreads the PVA as a film at cellulose intersections. The base sheet entering the saturator has a moisture content of 3–7%; if the moisture is above 9%, the binder film rehydrates and surface picking occurs during kiss coating. The resole resin add-on is controlled by a metering rod system at 150–300 g/m² wet deposit. Tensile energy absorption is measured by ISO 1924-2:2008; Cobb water absorption by ISO 535:2014 determines whether the PVA film has closed the surface excessively.
On abrasive disc punching lines, edge tear and notch sensitivity are the limiting production defects. The final abrasive sheets are coated with alumina or silicon carbide grit and cured at 120–140°C. Processing above 180°C is avoided because discolouration of the PVA film appears and adhesion of the printed backing becomes uneven. Published data for this specific resin-polymer interphase is limited, so each saturating resin grade requires a mill trial to verify anchoring. The converting operation uses high-speed slitting at 150–300 m/min, where edge dust from an under-bonded backing has been observed to contaminate the resin-coating section. The end product is a dimensionally stable abrasive backing for discs, belts, and sheets used in metal finishing; the PVA binder remains in the base paper and is subsequently locked under the phenolic resin layer.
Wet-laid separator base sheets for valve-regulated lead-acid batteries are composed of glass microfibers with average diameters from 0.5 µm to 4.0 µm and polyester or polypropylene scrim fibers. These furnishes have low initial wet and dry tensile because glass fiber does not fibrillate or form hydrogen bonds. VPB105-1 is introduced at 5–9 wt% so that it can dissolve at 70°C and create a binding phase without the high drying temperatures that would soften the synthetic scrim. Through-air drying at 80–105°C activates the binder while maintaining sheet temperature below the melting onset of the polypropylene component. The key process conflict is that the same binder film can block the tortuous pore network if overdosed. Porosity is screened by ISO 5636-5:2013 and by in-plane wicking tests required by separator OEM specifications. Dimensional stability after acid immersion is governed by internal protocols because no single ISO test covers all separator grades.
In production, the most frequent failure is brittle snap-off at the C-folder crease, which occurs when the PVA addition is below 4 wt% or when the drying profile fails to reach 70°C across the full width of the web. A wet-end pH above 9.0 accelerates swelling of the PVA fiber and should be avoided. Because glass fiber stock has low fines retention, the dissolved PVA also assists in anchoring short fiber fractions during the first dryer pass. The end product is a stiff separator base that is subsequently corrugated, buffered, and assembled into battery plates. The binder must not introduce chlorides or transition-metal contaminants that would affect gas recombination in the final cell.
The compliance matrix below condenses the main processing and test boundaries across the above sectors.
| Application segment | Primary standard or protocol | Critical process limit | End product |
|---|---|---|---|
| Wet-laid filter media | ISO 16890:2016, ISO 5011:2014, ISO 1924-2:2008 | First-zone air 75–90°C; stock <70°C | HVAC panels, engine intake elements |
| Abrasive backing paper | ISO 1924-2:2008, ISO 535:2014 | Saturator moisture 3–7%; cure 120–140°C | Abrasive discs and sheets |
| Glass microfiber separator | ISO 5636-5:2013, OEM acid immersion protocols | Through-air 80–105°C; wet-end pH 7–9 | VRLA separator base |
| Decorative laminate paper | ISO 8791-2:2013, ISO 2471:2008, EN 438 | First drying 70–85°C; wet strength resin 0.5–1.5 wt% | Low-pressure melamine laminate surfaces |
| Infusion sachet paper | 21 CFR 176.170, EC 1935/2004, ASTM F88/F88M-23 | Seal jaw 150–190°C; wet strength resin 0.7–1.2 wt% | Tea and coffee sachets |
| Repulpable label and wrapper | ISO 1924-2:2008, internal repulpability screen protocol | Storage RH <70%; drying 75–90°C | Water-dispersible labels, repulpable wrappers |
In melamine-faced decorative paper production, picking during gravure or ink-jet coating exposes fiber voids after impregnation with melamine-formaldehyde resin. The furnish is prepared from eucalyptus kraft pulp, high-opacity titanium dioxide, and VPB105-1 at 3–8 wt% on dry fiber. The PVA fiber remains undissolved during refining at 35–45°C and is distributed with the stock through a pressure screen. The first dryer section is set to 70–85°C, which dissolves the fiber and creates a consolidated surface layer. Without a wet-strength additive, the binder film is hygroscopic and loses strength when the base paper is immersed in aqueous melamine resin at 30–50 wt% solids. A polyamide-epichlorohydrin resin is therefore added at 0.5–1.5 wt% dry pulp to maintain tension through the impregnation bath. Surface roughness is evaluated by ISO 8791-2:2013, opacity by ISO 2471:2008, and sheet pH by ISO 6588-1:2020.
The impregnated decor sheet is pressed onto medium-density fiberboard or particleboard with overlay films under EN 438 conditions. Production experience shows that overdrying above 120°C before impregnation reduces resin absorption and creates dry-edge coating defects. The final component is a low-pressure laminate surface used in furniture and interior cladding; the PVA binder is locked inside the cured resin matrix and does not function as a surface barrier. The main operational boundary is reverse-side curl. This defect appears when the base paper moisture after drying is below 2%, because the PVA film contracts during subsequent rehumidification and alters the fiber orientation memory of the sheet.
Heat-sealable infusion sachet paper operates under conflicting requirements: the sheet must retain sufficient porosity for flavor release, seal on high-speed fill-and-seal lines, and resist fiber tear during a short immersion in hot water. VPB105-1 is used at 3–7 wt% in the base sheet, where it dissolves at 70°C during drying and contributes to the uniform densification of the seal layer. Because the binder remains water-sensitive, the converting formulation includes a polyamide-epichlorohydrin wet-strength resin at 0.7–1.2 wt% dry pulp; this resin provides the required retention of tensile strength during steeping above 90°C. The paper is formed on a twin-wire former at 40–60 g/m² basis weight and dried in a first phase at 75–85°C to activate the PVA binder, followed by a second phase below 110°C to cure the wet-strength resin. Heat-seal strength is tested according to ASTM F88/F88M-23 with jaw temperatures between 150°C and 190°C and dwell times of 20–80 ms.
Air permeance is controlled by ISO 5636-3:2013; wet burst after immersion is checked by ISO 2758:2014. Compliance for food contact is assessed under 21 CFR 176.170 and EC 1935/2004; the supplier documentation must demonstrate that the PVA grade does not dislodge particles into the infusion. The end products are tea and coffee sachet papers for single-serve converting lines, where seal defects are the main cause of line stoppage. Because the binder film rehydrates in the cup, this grade is not suitable for extended boiling exposure, multi-use bags, or high-fat contents that require barrier functions beyond the wet-laid substrate.
Water-dispersible paper labels and repulpable packaging grades use VPB105-1 as a temporary binder that returns to solution under warm water, thereby aiding fiber recovery and liner separation. The furnish is composed of bleached hardwood kraft with VPB105-1 at 10–20 wt%; the high addition level provides dry tensile for die cutting and flexographic printing. The sheet is formed on a standard Fourdrinier with couch vacuum adjusted so that the fiber is not washed out; first dryer cans are held at 75–90°C to trigger dissolution. At RH above 70%, the PVA film absorbs moisture and the sheet exhibits dimensional movement; rolls must be wrapped in moisture-resistant packaging and stored below 30°C. Repulpability is monitored by the mill's screen yield protocol: after a warm-water disintegrator cycle at 70°C, screen yield below 90% indicates insufficient dispersion and requires a higher dryer temperature or a lower addition rate. Dry tensile is measured by ISO 1924-2:2008; print surface strength is tested by an IGT pick test using ISO 3783:2014. The end product is a water-dispersible label or wrapper for reusable containers; it is not suitable for wet-grip packaging because the binder rehydrates and the paper loses structural strength in contact with water.
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Kuraray VPB105-1-PVA Binder Fiber for Paper Making (Dissolves at 70 °C) is a polyvinyl alcohol binder fiber supplied for papermaking furnishes in which the binder must remain a discrete staple fiber through stock preparation and sheet forming, then dissolve at a defined aqueous temperature of 70 °C. The grade is added as a dry furnish component, not as a pre-dissolved PVOH solution. Polyvinyl alcohol in fiber form has a density near 1.26–1.30 g/cm³; this range is consistent with published PVOH solid-state data and is relevant to stock-settling and retention calculations. Because the product is a fiber, its retention on the forming fabric depends on mechanical entanglement and sheet formation, not on adsorption of a dissolved polymer chain. Batch-specific fiber length, linear density, moisture, and ash values appear on the Kuraray certificate of analysis. Users should verify those values before setting refiner clearances and screen-slot dimensions.
Pilot evaluations typically use laboratory sheets formed according to ISO 5269-2:2004 to compare VPB105-1 addition levels against a control furnish. The addition level cannot be transferred directly from handsheet data to production because pilot drying conditions often differ from full-scale contact or through-air dryers. Handsheet dryers may reach 70 °C more rapidly than a heavy commercial sheet, so the observed bonding benefit may overstate the production response. Conversely, paper machine dryers with high evaporative load may under-develop the binder if steam pressure is limited. Any dose-response screening should therefore include tensile index according to ISO 1924-2:2008 and internal bond strength according to TAPPI T 569 after controlled drying, not solely after ambient air drying.
Premature dissolution is governed primarily by stock water temperature and residence time below the forming wire. At wet-end temperatures below 50 °C, VPB105-1 remains largely undissolved; if the stock reaches 70 °C in a pulper, machine chest, or broke system, the fiber can soften and produce tacky PVOH domains. A temperature-controlled approach below 60 °C is therefore recommended for mills that operate closed white-water loops with elevated process-water temperatures. Sustained exposure near the dissolution point should be avoided, especially in hot repulping of broke that has already passed through the dryer. Partially hydrated PVOH can coat deflaker plates, pressure-screen baskets, and forming fabric surfaces. Thermocouple data from the machine-chest discharge and headbox manifold provide the required verification.
Mechanical refining of VPB105-1 is not recommended as a primary action because it reduces fiber length and may generate PVA fines that escape into white water. On a disc refiner with standard cast alloy plates, the fiber is exposed to high shear and localized heating that can soften the material at loads below fiber damage thresholds for cellulosic fiber. Where refining is unavoidable, addition at the post-refiner chest is preferable to addition at the pulper. Pressure screens should be monitored for plugging when slot widths are below 0.2 mm; if rejects rise, stock dilution and higher screen rotor speed may be required.
Dry VPB105-1 addition eliminates the viscosity increase, cooking step, and foaming often associated with high-molecular-weight PVOH solution make-down. On the paper machine, the dry fiber can be fed by a loss-in-weight screw feeder into the pulper or post-refiner chest. Retention before the dryer is mechanical rather than adsorption-driven; in high-speed gap formers, formation, retention, and drainage must be balanced against fiber length and cut length distribution. Aqueous PVOH solution is subject to unretained-polymer losses that increase chemical oxygen demand in the white water, whereas retained VPB105-1 remains in the sheet until thermal activation. However, the dry-fiber route shifts bond development to the dryer section, so the wet-web tensile response is governed by refining and wet-end starch rather than thermal binder activation.
Thermal activation is not achieved when the web surface temperature alone reaches 70 °C; the entire z-directional cross-section must exceed the threshold for uniform binder dissolution. On multi-cylinder contact dryers, shell temperatures of 90–110 °C are common, but web core temperature depends on basis weight, incoming moisture, machine speed, and condensate removal. Through-air dryers provide direct hot-air penetration and can reach the dissolution threshold more uniformly in high-bulk grades, but at higher energy demand. Infrared dryers or air caps can accelerate surface heating in the initial dryer sections.
To verify bonding development, internal bond strength should be tested according to TAPPI T 569 or tensile index according to ISO 1924-2:2008 after dryer-section changes. If the sheet remains below 70 °C through the core, VPB105-1 remains partially in fiber form and the expected PVA film-bridge contribution is reduced. Wet-lap or heavy caliper boards are particularly sensitive because conductive heat transfer through the wet web is slower than in tissue or lightweight paper grades. Machine speed trials should record steam pressure, dryer surface temperature, sheet surface temperature, and final internal bond values before changing addition level.
Compared with starch, VPB105-1 does not introduce the same biochemical oxygen demand when retained, but dry PVA fiber must undergo thermal dissolution before it develops its final binding structure. Starch and PVOH solution wet-end binders develop hydrogen bonding as water is removed, without a phase-change dissolution step in the dryer. Compared with bicomponent thermoplastic binder fibers, such as polyethylene/polypropylene sheath-core grades, VPB105-1 does not leave a discrete hydrophobic synthetic domain in the finished sheet. The PVA phase is water-soluble at its activation temperature, which supports repulpability but also means the dry bond is water-sensitive unless protected by wet-strength resins, internal sizing, or coating. Wet tensile strength after immersion can be evaluated according to TAPPI T 456 or ISO 3781:2011.
| Variable | VPB105-1 dry PVA fiber | Aqueous PVOH solution | Starch binder |
|---|---|---|---|
| Addition point | Pulper or post-refiner chest | Metered thin stock or size press | Jet cooker or size press |
| Stock viscosity impact | Low at ambient wet-end temperatures | May increase headbox viscosity | Variable with cook quality |
| Bond development stage | Thermal dissolution at 70 °C in dryer | Water removal and hydrogen bonding | Water removal and hydrogen bonding |
| White-water loading | Polymer loss limited if fiber retained | Unretained PVOH raises COD | Unretained starch raises BOD |
| Finished-sheet water sensitivity | Water-sensitive unless protected | Water-sensitive unless insolubilized | Water-sensitive unless insolubilized |
The cut length and linear density of VPB105-1 should be selected for the forming geometry, headbox consistency, and drainage capacity of the target machine. Longer cut lengths improve mechanical retention but can create formation defects on high-speed fourdrinier wires; shorter lengths reduce formation risk but may pass through the forming fabric with fines. PVOH density near 1.26–1.30 g/cm³ reduces settling compared with denser synthetic fibers. Ignition residue is measured according to ISO 1762:2019 at 525 °C to verify that the PVA fiber does not raise furnish ash beyond the grade specification. Because PVOH is largely organic, it is consumed during ignition; only inorganic residues from the fiber or additives remain. The ash balance should be checked when VPB105-1 is combined with filler grades that contain calcium carbonate or kaolin.
For food-contact paper and paperboard, the specific VPB105-1 grade must be reviewed against the supplier regulatory statement and the intended food type. Polyvinyl alcohol may be used in paper and paperboard intended for food contact under the relevant national and regional frameworks, including FDA 21 CFR 176.170 for U.S. conditions of use and BfR Recommendation XXXVI for European paper and board. The user must confirm migration status, temperature of use, and any food-type restrictions with Kuraray regulatory documentation. For European workplace and supply-chain compliance, the current safety data sheet and REACH Regulation (EC) No 1907/2006 registration should be checked.
VPB105-1 occupies a 70 °C dissolution class. Lower-temperature PVA binder fibers may dissolve at 60 °C or below, reducing dryer demand but increasing the risk of premature dissolution in warm wet-end loops. Higher-temperature PVA binder fibers may require a larger dryer heat load and longer residence. Selection of the 70 °C grade is generally appropriate when the wet-end temperature remains below 60 °C and the dryer section can reliably raise the whole sheet to 70 °C. In tissue and towel machines with high-speed through-air dryers, the threshold can be achieved rapidly; on heavily loaded paperboard machines with thick calipers, the z-directional heat transfer must be confirmed. Published data for specific production-scale configurations of VPB105-1 is limited; pilot trials on a pilot paper machine are required to determine the actual dose-response.
Borate-containing wet-end additives should be avoided with VPB105-1 because borate ions form reversible PVOH–borate gel networks that can increase viscosity, reduce solubility, and create insoluble deposits. If borate is present in felt-cleaning chemicals or mill water treatment, the degree of interaction should be evaluated in laboratory stock-jar tests before production use. The fiber should be stored in dry conditions; PVOH is hygroscopic, and at relative humidity above 60 %, pre-drying or sealed storage is required to prevent surface tackiness and feeding issues in loss-in-weight equipment.
| Standard/Regulation | Designation | Application to VPB105-1 |
|---|---|---|
| ISO 5269-2:2004 | Preparation of laboratory sheets for physical testing | Basis for evaluating VPB105-1 addition level on handsheet tensile and formation |
| ISO 1924-2:2008 | Tensile properties of paper and paperboard at constant rate of elongation | Dry tensile index after thermal activation |
| ISO 1762:2019 | Determination of residue on ignition at 525 °C | Ash verification in filler-loaded furnishes |
| TAPPI T 569 | Internal bond strength of paper | Z-direction bond development after drying |
| TAPPI T 456 | Wet tensile strength after water immersion | Water sensitivity of PVA-bonded sheet |
| FDA 21 CFR 176.170 | Components of paper and paperboard in contact with aqueous and fatty foods | Regulatory review for food-contact end uses |