| HS Code | 592960 |
| Appearance | White milky liquid |
| Solid Content | 50 ± 2% |
| Viscosity | 8000 - 12000 mPa·s |
| Ph | 4.0 - 6.0 |
| Density | 1.05 - 1.10 g/cm³ |
| Average Particle Size | 0.5 - 1.5 μm |
| Glass Transition Temperature | 15 - 20 °C |
| Minimum Film Forming Temperature | 8 - 12 °C |
| Residual Monomer Content | ≤ 0.5% |
| Mechanical Stability | Good |
| Storage Stability | 6 months at 5 - 35 °C |
As an accredited BT-01 PVAc Emulsion factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | BT-01 PVAc Emulsion is packaged in 25 kg net sealed plastic drums, labeled with product details and safety information. |
| Container Loading (20′ FCL) | 20′ FCL loading of BT-01 PVAc Emulsion in drums/IBCs, secured and palletized, ensuring safe transport and stability. |
| Shipping | BT-01 PVAc Emulsion ships in sealed, corrosion-resistant drums or IBCs to prevent leakage and contamination. Transport in ventilated, dry containers, avoiding extreme temperatures and direct sunlight. Handle with care, keep upright, and follow standard chemical safety protocols to ensure stable, safe delivery. |
| Storage | Store BT-01 PVAc Emulsion in a cool, dry, well-ventilated area away from direct sunlight, heat sources, and open flames. Keep containers tightly sealed when not in use. Maintain storage temperature between 5°C and 35°C to prevent freezing or coagulation. Avoid exposure to moisture and contamination. Follow shelf-life guidelines, and use clean equipment when dispensing. |
| Shelf Life | Shelf life is 12 months from manufacture date when stored sealed at 5–35°C, protected from freezing. |
For interior solid-wood edge lamination on single-sided clamp carriers and multi-daylight hydraulic presses, the bond-line performance of BT-01 PVAc Emulsion in beech, oak, and pine assemblies is governed less by static viscosity than by the rate at which water leaves the glueline under compression. The adhesion mechanism is a coalescence-driven particle entanglement process: the aqueous dispersion must lose sufficient water into the wood capillary network before the polyvinyl acetate particles can fuse into a continuous film, so mean wood moisture content is maintained between 8% and 12% before spreading, with a shop-floor upper boundary of 14% because higher free water delays coalescence and produces starved bond lines on planed surfaces. For interior structural and semi-structural joinery, a single-side spread of 120 g/m² to 180 g/m² is used on planed softwood, while 150 g/m² to 180 g/m² is typical on medium-density hardwood where capillary absorption is less uniform; the wet adhesive is assembled within an open time of 5 min to 10 min at 20 °C and 60% relative humidity, while line temperatures above 28 °C lower the working open time to 3 min to 5 min and promote skin formation on transfer rollers, causing intermittent starved joints on later clamp positions. Clamp pressure is set between 0.6 N/mm² and 1.0 N/mm² for softwood and 0.8 N/mm² to 1.2 N/mm² for hardwood; excessive compression reduces the residual glueline below 0.10 mm, which is the minimum film thickness needed to maintain cohesive failure under tensile loading. Cold press time at 20 °C ranges from 20 min to 45 min for 22 mm face-glued staves, whereas high-frequency edge-gluing presses reach handling strength in 2 min to 4 min, but the stack must be conditioned for 24 h at 20 °C and 50% relative humidity before sanding or machining because the film continues to consolidate and microfracture appears at the glue line when mechanical stress is applied immediately after press release. Compliance for non-humid interior applications is assessed under EN 204:2016, class D2; upgraded D3 classification is achieved only when a crosslinking hardener is metered into the emulsion at 3 wt% to 5 wt% by total liquid weight immediately before use, and the mixed system is consumed within the stated pot life to avoid viscosity rebound and press contamination. Lap-shear strength is evaluated according to EN 205:2016 on beech test specimens, and batch-to-batch variation on high-speed clamp carriers is observed when returned reservoir adhesive exceeds 15,000 mPa·s at 25 °C due to evaporation; this is corrected with demineralized water at not more than 2 wt% of the returned volume because dilution below 48% solids collapses wet bond strength and extends clamp-open time unpredictably. Terminal finished product types include edge-glued panels for tabletops, solid wood drawer fronts, stair treads, finger-jointed mouldings, door stiles and rails, and multi-stave bench tops. The operational boundary includes avoiding ambient relative humidity above 65% for open assembly lines because water loss slows and the adhesive remains aggressively tacky on the wood surface; at the opposite extreme, relative humidity below 30% accelerates skinning and requires reducing the open time target to the lower end of the stated range.
In flat lamination of decorative wood veneer to MDF or particleboard, BT-01 PVAc Emulsion applied through a roller coater exhibits a process failure boundary that is more sensitive to veneer moisture than to press pressure. The wet adhesive application is maintained at 70 g/m² to 100 g/m² on the panel core for veneer and 60 g/m² to 80 g/m² for decorative paper overlay; the coater is run at 20 m/min to 30 m/min line speed with a nip gap set to deposit a uniform film without flooding the sheet edges. When the veneer moisture content exceeds 12%, the hot-press cycle converts retained water to steam at the adhesive interface, producing localized blow points and shifting the fracture path from cohesive within the PVAc film to adhesive at the wood interface; when moisture falls below 6%, the dry veneer withdraws water from the emulsion so rapidly that particle coalescence is incomplete before final compression, and the bond fails along low-porosity latewood zones. Cold pressing is performed at 0.5 N/mm² to 0.8 N/mm² for 20 min to 30 min, while heated platen pressing at 70 °C to 90 °C reduces the cycle to 3 min to 5 min; the higher temperature is limited to moisture-controlled panels to prevent steam blows. Compliance for surface soundness and adhesion of the finished laminated panel is checked under EN 311:2005, with additional internal quality control based on panel cross-cut adhesion after 24 h conditioning at 20 °C and 65% relative humidity. The production process includes glue spreading, panel layup, multi-daylight pressing, and post-press conditioning before finish sanding; failure modes observed on production lines include edge starvation when rolls are set too dry, adhesive strike-through on veneer thinner than 0.5 mm, and telegraphing when excess adhesive accumulates around dust particles on the core surface. Terminal finished product types include lacquered MDF tabletops, interior door skins, wardrobe side panels, and veneered furniture fronts. The operational limit is that BT-01 PVAc Emulsion remains a water-sensitive film; components exposed to continuous high humidity or direct liquid water without a topcoat require an upgraded crosslinked system or a different adhesive chemistry.
High-speed folding carton side-seam lines using disc-roller application subject BT-01 PVAc Emulsion to shear rates above 10,000 s⁻¹ during transfer from the metering disc to the carton seam, and the formulation must retain viscosity stability under that shear to prevent misting and web contamination. The adhesive is metered through a shallow plate trough with a partially immersed rotating disc, then applied to one seam flap at 4 g/m² to 6 g/m² wet weight before the blank is folded and compressed; compression belts provide 0.5 s to 1.0 s of dwell at speeds from 150 m/min to 250 m/min. On high-speed lines, water loss from the open trough raises the adhesive viscosity across a shift from 2,000 mPa·s to 4,000 mPa·s at 25 °C; production activity documents a correction limit of demineralized water addition not exceeding 1 wt% of the reservoir volume because higher dilution reduces tack development and causes seam pop-open during the folding station. Compliance for dry food and non-food carton side seams is reviewed under FDA 21 CFR §175.105 where the dried adhesive is used as an indirect food-contact substance behind a functional barrier or where it does not directly contact food; under REACH Regulation (EC) No 1907/2006, the emulsion is assessed for SVHC content at the 0.1% w/w notification threshold; and under EU Directive 94/62/EC, the combined heavy-metal migration of the finished package is controlled at the 100 mg/kg packaging limit. Downstream converting processes include side-seam gluing on folder-gluers, compression belt setting, crash-lock and straight-line carton erection, and final die-cut carton stripping. Terminal finished product types include detergent and cosmetic folding cartons, pharmaceutical secondary packaging, record jackets, and slip sheets. The operational boundary is low-temperature brittleness: the unplasticized PVAc film becomes brittle below 5 °C, so freezer carton or refrigerated packaging lines exceeding that thermal load require plasticized emulsion or a barrier cover.
| Regulatory/standard reference | Applicable condition | Threshold or test method |
|---|---|---|
| FDA 21 CFR §175.105 | Side-seam adhesive for folding cartons not in direct food contact | Indirect food additive; dried adhesive behind functional barrier |
| REACH Regulation (EC) No 1907/2006 Annex XVII | SVHC evaluation of BT-01 PVAc Emulsion | SVHC > 0.1% w/w |
| EU Directive 94/62/EC | Heavy metals in finished paper/board packaging | Sum of Pb, Cd, Hg, Cr(VI) ≤ 100 mg/kg |
In convolute and spiral tube winding for paper cores with inner diameters from 25 mm to 152 mm, BT-01 PVAc Emulsion functions as a starch-compatible wet laminate binder applied between kraft plies before the winding mandrel compresses the plies into a cylindrical structure. The wet adhesive addition ratio is maintained at 20 g/m² to 30 g/m² per glue line for kraft grades ranging from 200 g/m² to 250 g/m²; lighter tissue plies take the lower end of the range because excess water leads to wrinkles and paper tear at the mandrel. Spiral winder speed is set at 30 m/min to 60 m/min for standard core sizes, with a winding angle between 20° and 30° from the core axis; belt pressure at the mandrel is adjusted to avoid adhesive squeeze-out at the cut-off station. The adhesive is pumped from a holding tank to a pan applicator with doctor roll metering; machine operators monitor viscosity at 4,000 mPa·s to 6,000 mPa·s at 25 °C because lower viscosity causes strike-through into porous core paper, while higher viscosity reduces transfer and creates dry lap joints. Compliance for the finished core as packaging or carrier material is checked under EU Directive 94/62/EC for the sum of lead, cadmium, mercury, and hexavalent chromium not exceeding 100 mg/kg, and under REACH Annex XVII restriction entries applicable to substances in finished articles. Downstream production includes paper unwind, adhesive application, spiral winding, in-line cutting, drying, and end-finishing; dried cores are conditioned for 24 h to 48 h at 20 °C and 50% relative humidity before dimensional inspection. Terminal finished product types include adhesive tape cores, label cores, PET film cores, nonwoven roll cores, and protective film cores. The operational boundary is moisture sensitivity: PVAc homopolymer loses bond strength above 70% relative humidity during storage, and cores with exposed cut edges may delaminate if water-soaked or stored in uncontrolled warehouses; for outdoor or wet-use cores, a crosslinked PVAc or synthetic emulsion is substituted.
Formulators replacing vinyl acetate-ethylene binders in interior matt wall paints encounter a different scrub resistance and dry film condition profile with BT-01 PVAc Emulsion, primarily because the higher glass transition temperature of the vinyl acetate homopolymer raises early block resistance but narrows low-temperature film coalescence. The emulsion is added to the letdown stage after the pigment slurry is dispersed; a high-speed disperser with a Cowles blade at 18 m/s to 20 m/s peripheral speed is used for the pigment grind, and the PVAc binder is introduced under reduced agitation to limit shear-induced destabilization. The addition ratio in a flat interior wall paint is 12 wt% to 18 wt% of the total wet formulation for a 55% solids vinyl acetate homopolymer emulsion, which corresponds to 6.6 wt% to 9.9 wt% dry polymer binder on total paint; the pigment volume concentration is maintained between 45% and 60% because below this range the dried film becomes too glossy for contract matt products, and above this range scrub resistance falls below practical thresholds. Compliance with low-VOC requirements is anchored to EU Directive 2004/42/EC, Annex IIA, category (a), with a 30 g/L limit for ready-to-use water-based interior matt paints; scrub resistance is evaluated under ASTM D2486 using the weighted abrasion test, while dry film porosity and hiding are adjusted by formulation and checked by contrast ratio method ISO 2814. The downstream manufacturing process includes slurry pre-gel, pigment dispersion, letdown, viscosity adjustment with polyurethane or cellulose thickener, and final filtration through a 150 µm bag filter; batch-to-batch variance is observed when the emulsion is added too early to the disperser because the high shear and local temperature above 40 °C can reduce particle stability and produce microgel in the paint. The minimum film formation temperature of an uncoalesced PVAc homopolymer typically lies between 16 °C and 20 °C; below 10 °C application temperature, coalescent at 2 wt% to 4 wt% based on dry binder is required, and film formation remains unreliable below 5 °C without heated substrate or forced ventilation. Terminal finished product types include interior contract matt wall paint, ceiling white, low-VOC interior emulsion, and tintable base paints for pastel shades. The operational boundary includes an alkaline substrate limitation: PVAc films hydrolyze slowly on surfaces with pH above 10, so fresh cementitious render and lime plaster must be carbonated or sealed before application.
In thread-sewn hardcover book production, BT-01 PVAc Emulsion is applied as a cold adhesive to the spine after sewing to fix the thread, fill shoulder voids, and anchor the backlining cloth or nonwoven to the folded signatures. The adhesive is applied through a mechanically heated glue-off roller at 25 °C to 35 °C with a wet film thickness of 0.3 mm to 0.5 mm; the corresponding application rate is 200 g/m² to 300 g/m² on the spine area, depending on paper caliper and spine roughness. Downstream production includes sewing, glue-off, backlining, rounding and backing, case-making, casing-in, and joint pressing; the joint nipping pressure is set at 20 kN to 30 kN during casing-in for standard A4 to crown quarto casebound books, and the adhesive remains repositionable for 1 min to 2 min before initial tack locks the backlining in place. There is no harmonized EU standard specifically governing PVAc bookbinding adhesives; chemical compliance is managed under REACH Regulation (EC) No 1907/2006 registration and safety data sheet obligations, while paper permanence standards such as ANSI/NISO Z39.48-1992 do not evaluate adhesive film stability. Published data for BT-01 in adhesive-bound book block flex fatigue is limited, so binderies requiring archival guarantee or aggressive flex-cycle performance conduct internal cold-crack and page-pull testing before production qualification. Terminal finished product types include hardcover trade editions, annual reports, library-bound books, school textbooks, and casebound laminated covers. The operational boundary is grain direction: when the backlining cloth is applied against the spine grain or the adhesive film exceeds 0.5 mm wet thickness, the dried film can crack during rounding and backing, causing hinge weakness and endpaper splitting at the joint.
On gypsum plaster, aerated concrete, and sand-cement render, BT-01 PVAc Emulsion is diluted with water to produce a penetrating pore-sealing primer that reduces the absorbency of the substrate before water-based topcoats. The dilution ratio is 1:2 to 1:4 by volume emulsion to water, depending on surface porosity; highly absorbent gypsum skim coat takes the lower ratio, while dense sand-cement render takes the higher dilution to prevent glossy film build. The diluted primer is applied at 10 m²/L to 15 m²/L per coat by airless spray with a 0.6 mm to 1.0 mm tip or by short-nap roller, and the recoat interval at 20 °C and 55% relative humidity is 1 h to 2 h; topcoating is delayed to at least 4 h after the final primer coat to allow the water from the emulsion to escape and the film to consolidate. The production process includes surface dust removal, crack filling, spot priming, full-surface primer application, drying, and sanding before the decorative topcoat; on high-production interior renovation lines, forced air ventilation at 0.5 m/s across the surface reduces the recoat interval to the lower end of the stated range. There is no product-specific harmonized EU standard for PVAc plaster sealers; workplace and environmental compliance is managed under REACH Regulation (EC) No 1907/2006, and the liquid sealer is formulated to remain below the 30 g/L VOC threshold for water-based interior coatings under EU Directive 2004/42/EC when applied by roller or spray. Terminal finished product types include primed plasterboard, sealed gypsum plaster, primed aerated concrete, and renovation substrates under interior emulsion paints. The operational boundary includes damp and alkaline surfaces: the primer must not be applied to substrates with rising damp or surfaces with pH above 10 because continuous moisture and alkali accelerate hydrolysis of the PVAc film, leading to topcoat peeling and primer softening.
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BT-01 PVAc Emulsion is a polyvinyl alcohol-stabilised homopolymer polyvinyl acetate dispersion supplied as a white, medium-viscosity liquid with a nominal non-volatile content of 55 ± 1 % by ISO 3251. The emulsion is specified for porous assembly applications where rigid bond lines and fast wet tack are required. The stabilisation package is based on hydrolysed polyvinyl alcohol rather than low-molecular-weight surfactants, which increases shear resistance and reduces foam generation in high-speed transfer systems. The pH at 25 °C is maintained in the 4.0–5.0 band (ISO 976), and the density at 25 °C is 1.07–1.10 g/cm³ (ISO 2811-1). The minimum film formation temperature is 3 °C (ISO 2115), allowing unplasticised film formation above 5 °C in thin layers. Batch-to-batch rheology is influenced by the hydrolysis degree and molecular weight of the polyvinyl alcohol fraction; production-scale reaction records with 88 % hydrolysed polyvinyl alcohol at 3–5 % of monomer charge show a bimodal particle-size distribution in which the coarse fraction contributes wet tack and the fine fraction controls coalescence. The emulsion is supplied without added plasticiser, allowing formulators to select a coalescent according to end-use restrictions.
| Property | Nominal value | Test method |
| Appearance | White viscous liquid | Visual |
| Non-volatile content | 55 ± 1 % | ISO 3251 |
| Brookfield viscosity, RVT, Spindle 6, 20 rpm, 25 °C | 12,000–16,000 mPa·s | ISO 2555 |
| pH at 25 °C | 4.0–5.0 | ISO 976 |
| Density at 25 °C | 1.07–1.10 g/cm³ | ISO 2811-1 |
| Minimum film formation temperature | 3 °C | ISO 2115 |
| Average particle size by laser diffraction | 0.8–2.0 µm | ISO 13320 |
| Residual vinyl acetate monomer | ≤ 0.1 % | ISO 13741-1 |
Reference values only; the certificate of analysis controls batch-specific acceptance.
Bulk handling trials on continuous coaters indicate that the emulsion is shear thinning under transfer conditions. The low-shear Brookfield value measured at 20 rpm cannot be extrapolated to doctor blade or roller application conditions. At 25 °C, a cone-and-plate shear sweep from 1 s⁻¹ to 1,000 s⁻¹ typically shows a viscosity reduction from approximately 14,000 mPa·s to 1,000–1,500 mPa·s; published data for this specific configuration is limited, and line trials should confirm the final coating window. Freeze–thaw resistance is not a design property: storage below 0 °C can cause irreversible syneresis and grit formation. In heated or insulated storage, the product should be held between 5 °C and 35 °C. Transfer pumps should be sized for start-up viscosity of at least 20,000 mPa·s and operated below the cavitation limit. Rotary lobe pumps with wide clearances are preferred over narrow-clearance gear pumps because mechanical shear can heat the emulsion above 40 °C and create coagulum on seal faces. Extended storage beyond 6 months can shift viscosity upward by 5–10 %; periodic ISO 2555 checks are required before release to production.
Microbial contamination in open recirculation systems is a known batch failure mode. After wet storage in uncovered troughs for more than 72 h, bacterial counts measured by dip slides can exceed 105 CFU/mL and reduce pH below 3.5. A preservative approved for polymer dispersions should be added before extended campaign runs; the emulsion is not supplied as sterile.
BT-01 is used in water-resistant wood assembly adhesives meeting EN 204 D2 and, when formulated with crosslinkers, EN 204 D3 classification. On beech and oak with moisture content 8–12 %, a spread rate of 150–200 g/m² and a press cycle of 20–40 min at 0.7–1.4 MPa are typical. Lap-shear strength after 7 days at 23 °C and 50 % RH is measured by ASTM D905; published values for PVAc homopolymer wood adhesives of this solids level are commonly 12–16 MPa, but formulated batches must be verified against the specific substrate and press cycle. On birch, clamping before handling is commonly 15–20 min at 20 °C; on oak, open assembly should be limited to 5 min because acidic extractives can destabilise the wet film. Wet tack and open time are adjusted by water or plasticiser addition; water dilution above 5 % by weight lowers viscosity disproportionately and can extend open time beyond 10–15 min on absorbent board.
On high-speed paper bag converting lines running at 150–300 bags/min, BT-01 is applied by ribbed roller at 25–40 g/m². Open time of 8–15 s at 25 °C and 55 % RH allows side-seam bonding before the web enters compression drums. Compared with starch-based adhesives at similar solids, BT-01 produces a harder finished bond but requires drying tunnel temperatures above 70 °C to prevent blocking at stack compression. The shear stability of the polyvinyl alcohol-stabilised emulsion reduces stringing and misting at high roll speeds; however, machine operators should not exceed 100 m/min on narrow-web bag machines without verifying that the ribbed roller speed does not entrain air into the adhesive film.
Calcium carbonate filler levels between 5 wt% and 25 wt% based on wet emulsion are feasible only with controlled addition into an anchor-agitated vessel at 20–30 rpm. Addition above 15 wt% can produce a viscosity climb from 16,000 mPa·s to 80,000–120,000 mPa·s within 10 min if the mixture pH falls below 3.8; pre-neutralisation of the filler slurry with sodium bicarbonate to pH 6.5–7.5 is required. The polyvinyl alcohol stabilisation allows higher filler uptake than typical surfactant-stabilised grades before phase separation. Filled batches should be screened through 125 µm mesh before roller coating to remove agglomerates. A high-shear disperser at 1,000 rpm for 15–20 min is appropriate; air entrainment should be minimised because foam breaks slowly in polyvinyl alcohol-stabilised emulsions. On edge-coating lines with engraved rollers, filled BT-01 should be maintained below 35 °C to prevent viscosity increase from flash drying at the roller ends.
Compared with surfactant-stabilised homopolymer PVAc dispersions at equivalent solids, BT-01 exhibits higher low-shear viscosity, stronger shear thinning, reduced foam generation, and a larger particle-size distribution. The polyvinyl alcohol colloid layer reduces over-penetration into absorbent paper and improves wet tack in wood assembly, but it is more sensitive to low-pH fillers and to freeze–thaw cycling. For non-porous film-to-film packaging, a vinyl acetate-ethylene copolymer or a finer-particle-size plasticised PVAc is normally required; BT-01 does not provide adequate adhesion to untreated polyethylene or polyester films. The comparison table below summarises the primary handling differences.
| Parameter | BT-01 PVAc Emulsion | Surfactant-stabilised PVAc homopolymer | Test or condition |
| Stabiliser chemistry | Polyvinyl alcohol, 88 % hydrolysis grade | Mixed anionic/nonionic surfactants | Infrared spectroscopy |
| Low-shear viscosity at 25 °C | 12,000–16,000 mPa·s | 3,000–8,000 mPa·s | ISO 2555, 20 rpm |
| Shear thinning index, 1/100 s⁻¹ | 8–12 | 2–4 | Cone-and-plate sweep |
| T-peel on corona-treated polyethylene, 24 h | ≤ 0.5 N/mm | 0.3–0.8 N/mm | Line test |
| Filler tolerance before phase separation | 20–30 % | 10–15 % | Calcium carbonate addition |
Published data for the specific film-lamination configuration of BT-01 is limited; the peel values above are representative of unformulated homopolymer PVAc grades and must be remeasured on the intended film surface.
Plasticiser compatibility is limited to ester types with solubility parameters close to the polyvinyl acetate matrix. Triacetin at 5–12 wt% lowers the minimum film formation temperature below 0 °C but reduces heat resistance. Dibutyl phthalate usage is constrained by REACH authorisation and should not exceed 5 wt% in articles intended for children. Film formation at 5 °C and 65 % RH proceeds without added coalescent only when the wet film is thin and air movement is continuous. Water resistance after film formation is classified by EN 204 sequential treatments; unmodified BT-01 film shows moderate swelling and should not be specified for full exterior or marine exposure. If EN 204 D3 classification is required, a blocked isocyanate or aluminium chloride crosslinker at 0.5–2.0 wt% is added immediately before use, and the pot life of such mixes is commonly 2–6 h. Amine-based additives should not be combined with the aluminium chloride system because premature coagulation can occur. Uncrosslinked films are rigid and show low elongation at break; tensile strength of cast films is typically 8–12 MPa by ISO 527, but this value is not directly transferable to porous bond lines.
Regulatory documentation for BT-01 includes EU REACH registration for polyvinyl acetate monomers as applicable. The dried adhesive film may be evaluated under FDA 21 CFR 175.105 for food-contact adhesives and under 21 CFR 176.170 or 21 CFR 176.180 for paper and paperboard components if the formulated end product complies with the specified extractives and migration test methods. Published data for this specific configuration is limited; compliance must be established on the final article, not on the raw emulsion alone. Residual vinyl acetate monomer is controlled to ≤ 0.1 % by ISO 13741-1, and formaldehyde is not expected above 10 ppm in the wet product when tested by EN 1243.
Machine cleanup in continuous laminating lines requires water before film coalescence. Dried film is not redispersible and must be removed by hot alkaline cleaning at 50–60 °C or by solvent wiping with ethyl acetate; solvent wiping should be restricted to stainless-steel surfaces and conducted with local exhaust ventilation. Production-scale lines have shown that intermittent shutdowns longer than 30 min cause dry edge deposits on roller ends, increasing web tension by 10–15 % on paperboard laminators. Scrapers and washdown stations should be actuated before each pause, particularly when processing filled formulations. If the machine remains idle with wet adhesive on the roller train, pH drift below 3.5 can corrode unplated steel surfaces and destabilise the next batch through back-contamination.
BT-01 is also applied in spiral paper tube winding on machines running at 30–80 m/min. Application weight is 20–40 g/m² with a contact nip pressure of 0.2–0.5 MPa. The shear stability of the polyvinyl alcohol-stabilised emulsion reduces stringing and misting at high roll speeds. Comparative line trials with surfactant-stabilised homopolymer grades have shown lower misting but longer drying time when BT-01 is used at the same solids content; the drying time is approximately 10–20 % longer than low-solids grades, and infra-red preheating should be adjusted upward by 10–15 °C to maintain tunnel exit moisture below 8 %. On recycled board substrates, moisture pickup above 8 % at the exit can cause tube wall softening and dimensional instability in the final core.