| HS Code | 486713 |
| Productname | Celvolit 1466 VAE Emulsion |
| Chemicaltype | Vinyl Acetate Ethylene Copolymer Emulsion |
| Appearance | Milky white liquid |
| Solidcontent | 55 wt% |
| Viscosity | 3000 mPa·s at 25°C |
| Ph | 5.0 |
| Density | 1.06 g/cm³ at 25°C |
| Glasstransitiontemperature | 0°C |
| Minimumfilmformingtemperature | 0°C |
| Particlesize | 0.5–1.0 μm |
| Surfacetension | 30 mN/m |
| Residualmonomer | <0.1 wt% |
As an accredited Celvolit 1466 VAE Emulsion factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | Supplied in 1,000 kg IBC totes or 200 kg drums, tightly sealed to maintain emulsion stability and prevent contamination. |
| Container Loading (20′ FCL) | 20′ FCL container loading: Celvolit 1466 VAE Emulsion packed in sealed drums/IBCs, secured, labeled, and documented for safe transport. |
| Shipping | Celvolit 1466 VAE Emulsion is shipped in drums, totes, or bulk tankers. Protect from freezing and excessive heat; ideal transport temperatures are 5–35°C. Ensure containers are sealed and upright in ventilated, dry conditions. Not classified as dangerous goods, but avoid spills and contact with incompatible materials. |
| Storage | Store Celvolit 1466 VAE Emulsion in original, tightly sealed containers in a cool, dry, well-ventilated area away from direct sunlight and incompatible materials. Maintain temperatures between 5°C and 40°C; do not allow freezing. Keep containers upright to prevent leakage. Use within recommended shelf life and stir gently before use if separation occurs. |
| Shelf Life | Shelf life is typically 6 months from date of manufacture when stored properly, avoiding freezing and excessive heat. |
Celvolit 1466 is a carboxylated vinyl acetate-ethylene (VAE) copolymer emulsion stabilized with a polyvinyl alcohol protective colloid system. Its glass transition temperature (Tg) registers at 0°C, minimum film formation temperature (MFFT) at < 1°C, and the solids content is maintained at 55 ± 1%. The particle surface charge density introduced by carboxylation governs colloidal stability under high-shear mechanical stress and provides reactive sites for crosslinking with polyvalent metal cations or multifunctional aziridines. These parameters define a processing window suited to adhesion to low-surface-energy substrates and fiber bonding where room-temperature flexibility is non-negotiable.
Adhesive formulation with thermoplastic starches, polyvinyl alcohol extenders, or boric acid-complexed systems is well-documented in published literature; however, Celvolit 1466 diverges from conventional VAE grades in its response to acidic catalytic environments. At pH values below 3.8, the carboxyl groups protonate, causing a controlled destabilization that can be exploited for chemically triggered deposition onto cellulosic fibers but which presents a pot-life risk in closed-loop circulation systems. Published data for equilibrium surface tension at the carboxyl-protonation inflection point is limited. Processing plant operators have documented foam persistence anomalies when the emulsion is introduced into circulatory piping with flow velocities exceeding 1.5 m/s, attributed to PVOH desorption at pump impeller shear zones and subsequent free-surfactant migration to air-liquid interfaces.
Industry Compliance Standards: Food contact adhesives within the European Union must satisfy the Framework Regulation (EC) No 1935/2004 and, for paper and board applications, the German BfR Recommendation XXXVI on paper and board for food contact. In the United States, 21 CFR 176.170 (Components of paper and paperboard in contact with aqueous and fatty foods) and 176.180 (Components of paper and paperboard in contact with dry food) govern permissible extractives limits. The specific migration limit for vinyl acetate monomer, set at 12 mg/kg food simulant under Regulation (EU) No 10/2011 Annex I, requires gas chromatographic verification per EN 13130-8. EN 13432 and ASTM D6400-23 provide the frameworks for industrial compostability claims when Celvolit 1466 is blended with biodegradable polymer coatings.
Formulation Addition Ratios: As a primary adhesion layer in paper-to-paper or paper-to-biopolymer film laminations, Celvolit 1466 is typically applied at 100% of the wet adhesive weight, reduced to 80-95% when co-formulated with acetyl tributyl citrate plasticizer at 3-7 wt% of total emulsion mass to depress heat-seal initiation temperature. In repulpable adhesive formulations tested under TAPPI UM 213, inclusion of polyvinyl alcohol (degree of hydrolysis 88%, 4% aqueous viscosity 5-6 mPa·s) at 10-20 phr has been specified to maintain fiber-recovery yields above 85%. Pre-neutralization with sodium bicarbonate to a pH of 6.0-6.5 is mandatory when incorporating boric acid crosslinker at 0.5-1.5 phr to prevent premature boron-ester gelation with the PVOH stabilizer.
Downstream Manufacturing Process: Application proceeds via engraved roller coating (line speeds 150-300 m/min) or slot-die coating (wet film thickness 20-80 µm) onto one substrate web. The coated web transits an IR drying tunnel with air temperatures staged from 80°C to 120°C; dew-point monitoring of exhaust air at -5°C prevents PVOH-skin-over formation that would otherwise trap residual moisture and cause blistering at the heat-seal nip. Dried coated reels are slit and rewound, then transferred to form-fill-seal lines where the adhesive is reactivated at 70-85°C under jaw pressure of 3-5 bar for a dwell time of 0.3-0.8 seconds. Equipment documentation from horizontal flow-wrapper OEMs confirms that jaw-surface PTFE coating eliminates adhesive build-up and enables continuous operation exceeding 120,000 cycles between cleaning intervals.
Terminal Product Types: Cold-seal-compatible sandwich wraps for confectionery bars, heat-sealable inner bags for dry breakfast cereals, compostable single-serve sachets constructed from cellulose/polyhydroxyalkanoate laminates, and moisture-barrier paper envelopes for powdered beverage formulations requiring oxygen transmission rates below 10 cm³/m²·day (tested at 23°C, 50% RH per ASTM F1927).
Industry Compliance Standards: Nonwoven binders intended for absorbent hygiene products are subject to the voluntary Guideline for the Safety Assessment of Hygiene Absorbent Products issued by the European Disposables and Nonwovens Association (EDANA), alongside the OEKO-TEX Standard 100, product class I, for articles in prolonged direct skin contact. ISO 9073-3 specifies the trapezoid tear method for nonwoven tensile evaluation. Binders for flushable dispersible nonwovens are assessed under the fourth edition of the INDA/GD4 Flushability Guidance Document, which prescribes slosh-box disintegration testing and municipal sewerline transport modeling. Low formaldehyde content, confirmed via the Japanese Ordinance 112 acetylacetone method with a reporting limit of < 16 mg/kg, is a prerequisite for Asia-Pacific hygiene converters.
Formulation Addition Ratios: For air-laid cellulose cores in baby diapers and adult incontinence pads, Celvolit 1466 is spray-applied at dry add-on weights of 8-15% relative to fiber mass. Wet-laid nonwoven processes incorporating synthetic fibers (PET, bicomponent PET/PE) at 15-30% blend ratios operate with binder addition levels of 18-25%. In contrast, fully cellulosic wet-laid wipes intended for dispersibility require higher binder loading at 25-35% dry add-on, the elevated quantity compensating for the deliberate weakening induced by salt-sensitive groups when the wipe contacts tap water. When formulated with citric acid catalyst at 0.3-0.8% on emulsion solids and cured at 130-150°C, Celvolit 1466 self-crosslinks through esterification of carboxyl moieties with the PVOH hydroxyl network, raising the wet tensile index from approximately 2.5 Nm/g to 6.0 Nm/g as measured per ISO 1924-2.
Downstream Manufacturing Process: In air-laid formation, opened fluff pulp is gravimetrically dosed into a forming head and entrained in an air stream oriented perpendicular to a moving wire; Celvolit 1466, diluted to 10-15% solids, is sprayed through hydraulic atomizing nozzles (orifice diameter 0.3-0.5 mm, operating pressure 20-40 bar) vertically into the fiber curtain. The formed web enters a through-air bonding oven where oil-fired heat exchangers deliver air at 140-165°C for 15-45 seconds, sufficient to remove water and initiate crosslinking without scorching cellulose—a thermal-fusing threshold monitored by IR pyrometers scanning at 1 Hz. At the winder, inline beta-gauge sensors (Kr-85 sources) measure basis weight to a tolerance of ± 2 gsm, and the feedback loop adjusts pump stroke on the binder dosing unit to maintain add-on consistency. Production-scale experience records that relative humidity in the forming area exceeding 65% causes fiber clumping that manifests as periodic tensile-strength dips at the finished-roll core.
Terminal Product Types: Air-laid acquisition distribution layers (ADL) rated for fluid-strike-through time below 2.0 s (EDANA NWSP 070.3.R0), wet-laid flushable moist toilet tissue that passes the INDA GD4 slosh-box test with > 95% disintegration within 30 minutes, and thermally bonded nonwoven carrier sheets for transdermal drug delivery patches (loaded with lidocaine or fentanyl in rate-limiting silicone or polyisobutylene matrices).
Industry Compliance Standards: Printing inks and overprint varnishes conforming to the Nestlé Guidance Note on Packaging Inks when evaluated via the EuPIA Exclusion List for Photoinitiators and the Swiss Ordinance 817.023.21 Annex 10 requirements for printing inks on food-contact materials. Volatile organic compound content must remain below 5% by weight as enumerated by US EPA Method 24. The Cradle to Cradle Certified Material Health assessment at the Platinum level is pursued by several European flexible-packaging converters for water-based primer systems. Surface energy of the primed substrate, determined using calibrated dyne pens per ASTM D2578, needs to achieve 48-52 dynes/cm to ensure ink wetting without reticulation.
Formulation Addition Ratios: Priming lacquers based on Celvolit 1466 are compounded at 45-70 wt% of the total wet formulation, with the balance comprising deionized water (15-30 wt%), isopropanol as coalescent and defoamer vehicle (5-10 wt%), and a high-density polyethylene wax slip agent dispersion (2-5 wt% on dry weight, particle size D50 < 10 µm). Addition of a polyfunctional aziridine crosslinker (trimethylolpropane tris(2-methyl-1-aziridinepropionate)) at 0.5-1.2 wt% of total formula reduces the number of double rubs to failure (methyl ethyl ketone, ASTM D5402) from < 20 to > 100 after 48-hour room-temperature cure. Rheological modification with hydrophobically modified alkali-swellable emulsion (HASE) thickeners, targeting a Brookfield viscosity of 200-500 mPa·s at 20 rpm (spindle #3), prevents Ribbing instabilities in the coating nip at press speeds above 250 m/min.
Downstream Manufacturing Process: The primer is pumped to a chambered doctor-blade system (anilox roll: 120-160 L/cm, hexagonal cell geometry, theoretical cell volume 11-15 cm³/m²) on a central-impression flexographic press. Directly after primer transfer, the web transits an interstation hot-air drying hood delivering impingement velocity of 25-35 m/s and air temperature of 70-90°C for a residence time of 0.5-1.2 seconds; web surface temperature exiting the hood must not exceed 45°C to avoid blocking of the corona-treated BOPP or LDPE web during subsequent in-line printing. Converting operations report a persistent defect known as “ghosting” when anilox-to-plate squeeze pressure deviates by more than 0.05 mm, resolved by closed-loop hydraulic impression setting with displacement transducers reading to ± 0.01 mm.
Terminal Product Types: Surface-printed frozen vegetable pouches using reverse-printed PET/PE laminates, shrink-sleeve labels for PET bottles where the primer ensures adhesion through the hot-caustic shrink tunnel, and paper-based ice-cream cone overwraps requiring frost resistance at -25°C without ink delamination.
Carpet backings represent a distinct end-use class where VAE emulsion binders entirely dominate the late-phase consolidation of tufted constructions. Celvolit 1466 is introduced into precoat and lamination coating operations that secure face yarn to the primary backing and subsequently laminate the secondary backing fabric to the precoated tufted structure. The carboxylated functionality of the emulsion has been correlated with improved filler loading capacity—calcium carbonate at 200-450 parts per hundred parts of emulsion solids is documented without catastrophic viscosity break—because the particle surface charge facilitates electrostatic stabilization of the dense filler-binder interfacial region that would otherwise shear-thin irreversibly under high-speed blade coating.
Industry Compliance Standards: The Carpet and Rug Institute (CRI) Green Label Plus program (Carpet Testing Program v.3.2) sets total VOC emission limits at < 0.5 mg/m³ after 14 days per chamber testing per ASTM D5116-17 using small environmental chamber methodology. The European voluntary scheme GUT (Gemeinschaft Umweltfreundlicher Teppichboden) establishes additional limits for 4-phenylcyclohexene and vinyl acetate as individually listed substances. Fire behavior classification under EN 13501-1 is achieved by formulating Celvolit 1466 with aluminum trihydrate (ATH, median particle size 15-25 µm) as a blend component; the critical radiant flux per ASTM E648 (flooring radiant panel test) must exceed 0.45 W/cm² for Class I institutional carpet designation.
Formulation Addition Ratios: In precoat compounding, Celvolit 1466 constitutes the sole latex binder, loaded into a high-speed disperser (Cowles blade, tip speed 18-25 m/s) with calcium carbonate filler at a dry-weight ratio of 1:2.5 to 1:4.0. For lamination compounds, a secondary low-Tg styrene-butadiene latex may be blended at a VAE-to-SBR dry-weight ratio of 70:30 to extend open time; the formulation is thickened with sodium polyacrylate (molecular weight 3,000-5,000 g/mol) to a target viscosity of 8,000-14,000 mPa·s (Brookfield #5, 20 rpm). Ammonia solution (28% assay) is drip-fed at 0.1-0.3% to adjust compound pH to 9.0-9.5, stabilizing the carboxylate form of the binder.
Downstream Manufacturing Process: Tufted greige carpet is unwound into a coating range where the precoat compound is applied by a lick-roll applicator rotating in a pan and metered by an adjustable doctor blade set to a gap of 0.5-1.2 mm. The precoated carpet immediately enters a tenter-frame drying oven divided into three thermal zones: Zone 1 at 100-120°C (surface water removal), Zone 2 at 130-150°C (coalescence and film formation), Zone 3 at 110-130°C (cure completion without thermal yellowing). Oven residence time ranges from 4-8 minutes. Secondary-backing lamination involves spreading the filled compound onto the precoat layer and marrying the secondary fabric (typically woven polypropylene or jute) via nip-roll lamination at a pressure of 2-4 kg/cm of roll width. In-line moisture analyzers using near-infrared reflectance at 1,940 nm verify residual moisture below 0.8% downstream of the final oven zone before the carpet is accumulated on a J-box accumulator and fed to the inspection and cut-to-length station.
Terminal Product Types: Broadloom contract carpet for hospitality settings (corridor class, minimum face weight 450 g/m²), 6-foot-width modular carpet tiles with bitumen-modified secondary backing for raised-access-floor office environments, and automotive cut-pile floor mats where the carboxylated VAE precoat withstands repetitive trunk-compartment thermal cycling from -20 to +80°C without cohesive failure or odor release.
Industry Compliance Standards: Glass-fiber scrim products for external thermal insulation composite systems (ETICS) are governed by EAD 040083-00-0404 when placed in the European market, with alkali resistance tested per ETAG 004, Section 5.5.4.2, involving immersion in 5% NaOH solution at 23°C for 28 days and residual tensile strength retention of at least 50%. For flat-roofing polyester-reinforced underlayment, EN 13707 specifies the mechanical requirements, including nail tear resistance per EN 12310-1. The finished composite fabric is typically classified per EN 13501-1 for reaction to fire; Euroclass E or higher is demanded. Binder content is verified via loss-on-ignition testing at 625°C per ISO 1887.
Formulation Addition Ratios: Celvolit 1466 is applied at a dry-add-on target of 12-22 g/m² onto a woven or laid-scrim substrate, equating to approximately 8-18% of the finished composite mass. Crosslinking is induced with ammonium zirconium carbonate (AZC, 20% ZrO₂ content) at 1.5-3.0% on emulsion solids; this metal-chelation mechanism is more effective in carboxylated emulsions than in non-functionalized analogs, with wet tensile retention after 24-hour water immersion at 23°C increasing from a baseline of 40-50% to 70-85% at the optimal AZC dose. Where flame retardancy is required, ammonium polyphosphate (phase II, degree of polymerization > 1,000) is dispersed into the binder bath at 10-20 phr, and the dispersion is stabilized with a non-ionic surfactant at 0.2% on the APP weight to prevent re-agglomeration in the dip tank.
Downstream Manufacturing Process: A continuous web of reinforcement fibers—either stitch-bonded filament yarns (warp-knit, gage 5-7 needles/inch) or a cross-laid scrim assembled from rovings—is led over a series of idler rolls into an immersion dip tank where Celvolit 1466 compound, maintained at 30-40°C and continuously recirculated through a magnetic filter, coats the yarn intersections. Surplus compound is removed by a pair of pneumatic squeeze rolls (Shore A 60-70, nip pressure 0.3-0.5 MPa). The saturated scrim then enters a multi-pass dryer; in a tenter configuration with pin-chain transport, nozzles above and below the web deliver air at 150-175°C for a dwell time of 1.5-3.0 minutes. The exit window, constrained by the glass transition of the binder and the oxidation threshold of the PET or glass yarn, necessitates that web surface temperature not exceed 165°C. Production operators have documented that trace carryover of spin-finish lubricants from untreated glass roving into the aqueous binder bath causes cratering in the dried film, remedied by in-line plasma pre-treatment of the glass fabric at 500 W·min/m² prior to the dip tank.
Terminal Product Types: Alkali-resistant reinforcing mesh (mesh size 5 x 5 mm to 10 x 10 mm) for cementitious base coats in ETICS facades, flat-roofing polyester carrier fleece coated for torch-on membrane dimensional stability, and self-adhesive waterproofing carrier grids used in below-grade foundation waterproofing composite sheets.
| Crosslinker Type | Addition Level (wt% on solids) | Wet Tensile Retention After 24h H₂O Soak (%)ISO 1924-2 | Gel Fraction After 2h MEK Soxhlet (%) | Observations |
|---|---|---|---|---|
| Unmodified control | 0 | 42-48 | 15-22 | Cohesive failure at fiber crossover points; acceptable only for temporary protective veil applications with < 7-day service life. |
| Ammonium zirconium carbonate (AZC) | 2.0 | 72-80 | 58-67 | Optimum zirconium-carboxylate coordination density; marginal improvement beyond 3.0% dose, and excess AZC at >5.0% causes compound viscosity to double within 4-hour pot life. |
| Trimethylolpropane tris(2-methyl-1-aziridinepropionate) | 0.8 | 78-88 | 65-75 | Superior wet strength but 8-hour pot life drop when compound pH drifts below 8.0; forced ventilation of dryer exhaust required to keep aziridine-derived vapor below occupational exposure limit of 0.5 mg/m³ per NIOSH. |
| Glyoxal (40% aqueous) | 3.0 | 55-63 | 38-45 | Yellowing upon storage at >40°C limits application to dark-pigmented systems only; avoided in white ETICS mesh. |
The adoption of Celvolit 1466 as a co-binder in cementitious thin-bed tile adhesives and self-leveling underlayments exploits the emulsion's capacity to coalesce within the high-pH pore solution of hydrating Portland cement. Standard emulsion modifications for mortar involve the simultaneous management of defoaming, workability retention, and early-strength development. In thin-bed adhesive formulation, the water carried by the VAE emulsion contributes to the total mixing water; the effective water-to-cement ratio (w/c) must be corrected accordingly. At Celvolit 1466 addition levels of 3-7% polymer solids on cement mass, the increase in open time—tested per EN 1346 by measuring tensile adhesion strength of tiles applied after a 30-minute maturing interval—is attributed to the coalesced polymer film reducing evaporative water loss from the mortar surface, not to chemical retardation of cement hydration, as calorimetric isothermal studies (TAM Air, 23°C) show less than 20 minutes shift in the main silicate hydration peak at the stated dosage range.
Industry Compliance Standards: Cementitious tile adhesives are classified under EN 12004; polymer-modified dispersion adhesives fall into the D classification, while cementitious adhesives with polymer modification exceeding 2.5% dry polymer on dry mix remain C1 (normal) or C2 (improved) with additional characteristics designated by suffixes: T (reduced slip), E (extended open time), S1 (deformability ≥ 2.5 mm transverse deformation per EN 12002), S2 (deformability ≥ 5.0 mm). LEED v4.1 low-emitting materials credit requires VOC content compliance per California Department of Public Health (CDPH) Standard Method v1.2. China's GB 18583-2008 mandates a free formaldehyde limit of < 0.5 g/kg and total VOCs below 50 g/L in adhesive products for indoor decorating and refurbishing.
Formulation Addition Ratios: In a standard dry-mix C2TES1 thin-bed formulation, Celvolit 1466 is introduced as a liquid admixture at the job site rather than as redispersible powder. The liquid addition rate to dry mortar is 15-25 parts emulsion per 100 parts dry mix by weight; this delivers 8-14 parts of polymer solids. When converting from a powder-based formulation reference, the liquid water content of the emulsion (approximately 45%) displaces 7-11 parts of batch water. Cellulose ether (hydroxypropyl methylcellulose, viscosity 40,000-60,000 mPa·s at 2% aqueous solution) at 0.3-0.5% on dry mix weight provides the base rheology, with a polycarboxylate ether superplasticizer at 0.1-0.3% compensating for the slight slump increase introduced by the PVOH stabilizer. A mineral-oil-based powder defoamer at 0.1-0.2% is mandatory to suppress air entrainment beyond 5% air content (tested per ASTM C185 with the modification that the emulsion is substituted for an equivalent volume of water).
Downstream Manufacturing Process: Tile adhesive compound is mixed at the construction site using a low-speed paddle mixer (300-450 rpm) for 90 seconds with pre-weighed emulsion, followed by a 3-minute maturing period and a final 30-second re-mix. The adhesive is trowel-applied with a notched trowel (notch dimensions 6 x 6 x 6 mm for standard ceramic tiles, 10 x 10 x 10 mm for large-format porcelain exceeding 0.36 m² per tile). The installed tile is bedded with firm pressure and lateral movement; pull-off testing per EN 1348 after 28 days of standard climate storage (23°C, 50% RH) typically yields adhesion strengths of 1.5-2.5 MPa, with failure mode predominantly cohesive within the adhesive rather than adhesive at the tile interface. Extended open time exceeding 30 minutes is critically sensitive to ambient conditions; air movement above 0.5 m/s or substrate temperatures above 35°C reduce the skinning-over time to under 15 minutes, and site reports document that re-trowelling a skinned adhesive bed without removing and replacing the material results in near-zero adhesion.
Terminal Product Types: Polymer-modified thin-bed mortar for porcelain stoneware tiles in underfloor-heating compatible installations (thermal cycling per ISO 13007-4, 20 cycles between +20°C and +50°C), liquid-applied waterproofing membrane underlayments comprising a primer coat of Celvolit 1466 diluted 2:1 with water prior to a reinforcing fleece embedment, and self-leveling floor screed compounds designed for pump application at flow distances up to 15 meters where the VAE emulsion modifies the Young's modulus to accommodate 0.3-0.5 mm shrinkage without delamination from the concrete substrate.
Industry Compliance Standards: Adhesives for furniture edgebanding are evaluated under the ANSI/BIFMA M7.1-2011 test method for formaldehyde and VOC emissions from office furniture systems, with an acceptance criterion of < 50 ppb formaldehyde in chamber air after 7 days. The European standard EN 204, classification D3 (frequent short-term exposure to running or condensed water), is the minimum performance requirement for kitchen and bathroom furniture joints. The Japanese Agricultural Standard JAS 233:2008 specifies the boiling-water soak-delamination test for laminated wood products, where edgeband-peel force after soak must exceed 40 N/25 mm of band width. TSCA Title VI compliance is obligatory for formaldehyde-emitting composite wood products sold in the United States, though VAE emulsions contribute negligible free formaldehyde.
Formulation Addition Ratios: The edgeband pre-coating lacquer comprises Celvolit 1466 at 85-95 wt% with an anti-blocking additive dispersion—typically a high-density oxidized polyethylene homopolymer wax (acid number 15-25 mg KOH/g, melting point 130-140°C)—at 3-8 wt% of the dry film. The formulation may include a fugitive base (ammonia, adjusted to pH 9.0-9.5) to maintain the carboxyl groups in their ionized, non-reactive form during storage and coating, thereby preventing premature surface crosslinking. The pre-coating weight applied to the reverse side of the edgeband (ABS, PVC, or veneer) is 30-60 g/m² dry film, delivered as a 40-50% solids formulation via gravure roller.
Downstream Manufacturing Process: Celvolit 1466 is coated onto the edgeband at a dedicated converting operation. The edgeband is unwound (tension 20-35 N for a 23 mm-wide, 1 mm-thick ABS band) and passed through a two-roll gravure station; after metering, the web transits a hot-air drying tunnel at 60-80°C to remove water and ammonia, leaving the carboxylic acid functionality in a latent reactive state. The coated and re-wound edgeband is shipped to the furniture manufacturer, where it is fed through an edgebanding machine. At the point of application, a hot-air blower or infrared heater (wavelength 2.5-3.5 µm) reactivates the dry adhesive film to a surface temperature of 70-90°C, at which point the carboxyl groups and the PVOH undergo rapid tack development. The heated band is pressed onto the MDF edge by a series of pressure rollers (sequential pressure profile: roller 1 at 0.5 MPa, roller 2 at 1.2 MPa, roller 3 at 0.8 MPa) over a pressing zone of approximately 600 mm, corresponding to a dwell time of 1.0-2.5 seconds at typical feed speeds of 12-20 m/min. The reactivation method is sensitive to heat-input consistency: fluctuations exceeding ± 5°C at the band surface produce alternating over-bonding and under-bonding zones detected by an inline peel-force tribometer set to reject at < 35 N/25 mm. Transfer of the dry VAE layer onto the pressure rollers—commonly termed “roll-wrap”—is prevented by PTFE-impregnated roller covers with a surface roughness Ra below 0.8 µm and by limiting the cumulative machine runtime between roller cleaning cycles to 8 hours.
Terminal Product Types: PVC and ABS edgebanded office desktops resistant to peeling at the front-edge point-load zones, high-gloss kitchen cabinet doors where the pre-coated band is reactivated and immediately over-painted with a water-based pigmented topcoat after edge trimming, and veneer-edgebanded interior door leaves graded for fire resistance per EN 1634-1 where the adhesive must maintain integrity at the door-lip during a 30-minute cellulose-fire test.
| Application Segment | Relevant Standard or Code | Parameter Measured | Typical Target Value |
|---|---|---|---|
| Paper/Film Heat-Seal Adhesive | EN 13432 / ASTM D6400-23 | Disintegration (compostability) | ≥ 90% disintegration after 12 weeks |
| Paper/Film Heat-Seal Adhesive | 21 CFR 176.170 | Chloroform-soluble extractives | Adheres to compositional limits for paper and paperboard components |
| Nonwoven Binder (Hygiene) | OEKO-TEX Standard 100, Class I | Formaldehyde (acetylacetone method) | < 16 mg/kg |
| Nonwoven Binder (Flushable) | INDA/EDANA GD4, 4th Ed. | Slosh-box disintegration | > 95% passage through 12.5 mm sieve at 30 min |
| Flexographic Primer | Swiss Ordinance 817.023.21 Annex 10 | Photoinitiator migration | ND (< 10 ppb) for unlisted substances |
| Carpet Backing | CRI Green Label Plus v3.2 | Total VOCs (14-day chamber) | < 0.5 mg/m³ |
| Carpet Backing | ASTM E648 | Critical radiant flux | ≥ 0.45 W/cm² (Class I) |
| Glass/PET Reinforcing Scrim | ETAG 004 Section 5.5.4.2 | Tensile strength retention after alkali immersion | ≥ 50% residual at 28 days |
| Cementitious Tile Adhesive | EN 12004 / EN 12002 | Transverse deformation (S1/S2) | S1: ≥ 2.5 mm; S2: ≥ 5.0 mm |
| Cementitious Tile Adhesive | GB 18583-2008 | Free formaldehyde | < 0.5 g/kg |
| Profile-Wrapping Edgeband | ANSI/BIFMA M7.1-2011 | Chamber formaldehyde concentration | < 50 ppb at 7 days |
| Profile-Wrapping Edgeband | JAS 233:2008 | Boil-soak delamination peel force | > 40 N/25 mm |
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| Parameter | Celvolit 1466 (VAE) | PVAc Homopolymer | Acrylic (BA/MMA) | Test Standard |
|---|---|---|---|---|
| Solids content (%) | 55 | 50–52 | 50–55 | ISO 3251 |
| MFFT (°C) | < 1 | 15–18 | 14–20 (without coalescent) | ASTM D2354 |
| Elongation at break (%) | > 600 | 200–300 (plasticized) | 300–500 | ISO 527-2 |
| Water absorption (24 h, %) | 8–12 | 25–35 | 15–25 | ISO 62 |
| Required plasticizer for ambient film form. | None | 8–15 wt% on solids | 0–12 wt% on solids | — |
| Carpet tuft lock (N, nominal) | 45–55 | 30–40 (brittle fracture) | 40–50 | ASTM D1335 |
| Regulation / Standard | Clause / Requirement | Applicability to Celvolit 1466 |
|---|---|---|
| FDA 21 CFR 175.105 | Adhesives for indirect food contact (dry food/dry contact) | Compliant when formulated without unauthorized biocides |
| FDA 21 CFR 176.170 | Components of paper and paperboard in contact with aqueous and fatty foods | Subject to extraction limits; suitable under specific conditions |
| EU Regulation 1907/2006 (REACH) | Substances of very high concern | None intentionally added; SVHC < 0.1% |
| EU 2004/42/EC (VOC Solvents Emissions) | Decorative coatings and vehicle refinishing products | VOC < 1 g/L (Method 24) as supplied |
| GB/T 30795-2014 | Adhesives for food packaging composite film | Migration test applicable at end-article stage |
| DIN EN 204 Durability Class D3 | Non-structural wood adhesives for interior use, occasional wet exposure | Pass at > 7 N/mm² after 4-day conditioning cycle |