| HS Code | 409407 |
| Base Polymer | Polyvinyl acetate (PVAc) |
| Modification | Acrylic copolymer |
| Water Resistance | Improved, suitable for humid and damp conditions |
| Glass Transition Temperature | Approximately 0 to 10°C |
| Minimum Film Forming Temperature | Around 5°C |
| Adhesion | Excellent to wood, paper, and porous substrates |
| Flexibility | Enhanced flexibility due to acrylic modification |
| Drying Time | Tack-free in 15 to 30 minutes; full cure in 24 hours |
| Voc Content | Low, less than 50 g/L |
| Ph | 4.5 to 6.5 |
| Density | Approximately 1.05 to 1.10 g/cm³ |
| Freeze Thaw Stability | Stable with proper storage; avoid repeated freeze-thaw cycles |
| Tensile Strength | Typically greater than 10 MPa for cast film |
| Elongation At Break | Moderate, ranging from 100% to 300% |
| Coalescing Ability | Good film formation without high solvent demand |
As an accredited Water-Resistant Acrylic-Modified PVAc factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | Supplied in 25 kg HDPE drums with secure, airtight lids, ensuring safe handling and moisture-resistant storage. |
| Container Loading (20′ FCL) | 20′ FCL loaded with Water-Resistant Acrylic-Modified PVAc in sealed drums/IBCs, secured and blocked to prevent shifting during transit. |
| Shipping | Ship Water-Resistant Acrylic-Modified PVAc in sealed drums or totes, protected from moisture and extreme temperatures. Use proper labeling and secure palletization. This product is typically non-hazardous, but avoid leaks and consult SDS for specific transport regulations. Ensure ventilation during loading and compatibility with shipping materials to maintain product integrity. |
| Storage | Store Water-Resistant Acrylic-Modified PVAc in a cool, dry, well-ventilated area away from direct sunlight and heat sources. Keep containers tightly sealed when not in use to prevent skinning or contamination. Protect from freezing and temperatures above 90°F (32°C). Ensure adequate ventilation to avoid vapor accumulation. Follow all label and SDS instructions. |
| Shelf Life | Shelf life is typically 12 months from manufacture when stored sealed, cool, and dry, avoiding freezing. |
The distinction between EN 204:2016 durability classes D3 and D4 in non-structural wood adhesives is governed by how the acrylic copolymer phase shifts the glass transition and interacts with an aliphatic isocyanate hardener. A water-resistant acrylic-modified PVAc dispersion formulated at 48–55 wt% solids and an acrylic modification level of 15–25 wt% of total binder solids typically exhibits a Brookfield viscosity of 8,000–18,000 mPa·s at 20 rpm and 25 °C under ISO 2555. If the acrylic phase glass transition temperature is below −10 °C, as determined by differential scanning calorimetry under ISO 11357-2, wet shear strength after water contact remains insufficient for D4 service because the film softens and creeps under load. If the acrylic phase glass transition is raised above 15 °C, open time collapses below 5 min and edge-starved joints appear on high-absorption beech and birch substrates. On production spreader lines, the adhesive is applied at 120–180 g/m² with a polyurethane grooved roller or toothed spreader. Open time at 35 °C and 40% relative humidity is typically 6–9 min, while closed assembly time should not exceed 12 min to avoid skinning. Press pressure between 0.7–1.2 N/mm² for 20–40 min at 18–22 °C fixes the joint before moisture loss creates a weak interphase. The role of the acrylic component becomes more critical when an aliphatic polyisocyanate hardener is added at 3–5 wt% of dispersion mass. Below 3 wt%, crosslink density remains insufficient to resist delamination after cyclic damp exposure. Above 5 wt%, pot life falls below 30 min and the cured film embrittles, leading to brittle failure at oak annual-ring boundaries. Storage stability data from mixer tanks show that pH drift from 4.0 to below 3.2 accelerates hardener reaction with water, generating carbon dioxide and foam in pMDI-containing systems. The workable boundary is therefore narrow: pH 3.5–5.0 under ISO 976, viscosity 8,000–18,000 mPa·s, and wood moisture content between 8% and 12% on the dry basis. Moisture above 12% delays fibre saturation and produces a starved bondline, while moisture below 8% reduces adhesive penetration and yields chalky joint edges after planing. Published data for exact wet shear values across every hardwood species is limited; D3/D4 classification under EN 204:2016 requires passing the relevant water immersion and re-drying sequences, and the acrylic modification level must be validated for each filler and hardener combination rather than transferred from beech to meranti or teak without re-testing.
For humid retail and cold-chain folding-carton bonding, the adhesive is slot-die or disc-roller applied at 20–50 g/m² to clay-coated board with basis weight 300–450 g/m². Formulation solids are typically held at 45–52 wt% to balance wet tack and fibre penetration. Brookfield viscosity, measured by ISO 2555 at 20 rpm and 25 °C, ranges from 1,200–3,000 mPa·s. A lower viscosity, below 1,000 mPa·s, causes strike-through on recycled board with high ash content and destroys the surface sizing layer, while a higher viscosity above 3,500 mPa·s produces skip coating on high-speed carton lines running above 250 m/min. The acrylic phase is responsible for maintaining bond integrity when sealed cartons are held at 4 °C for 24 h and then exposed to 85% relative humidity at 30 °C. Peel separation under ASTM F904 should remain above 2.5 N/15 mm on polyethylene-laminated board, with cohesive fibre tear rather than adhesive delamination. For indirect food contact, the dry adhesive film must meet the component requirements of FDA 21 CFR 176.170 when the carton contacts aqueous or fatty foods, and the formulation should additionally conform to FDA 21 CFR 175.105. In the European market, the finished article falls under Regulation (EC) No 1935/2004, with the adhesive validated through migration testing on the final board construction rather than on free films. If a compostable claim is required under EN 13432, the adhesive content must be assessed for disintegration after 12 weeks in controlled aerobic composting. Because acrylic-modified PVAc is not inherently biodegradable at the rate of thermoplastic starch or cellulose-based binders, the formulation cannot exceed a minor constituent threshold without compromising the ≥90% disintegration criterion. On the packaging line, pH is maintained between 3.5–5.0 under ISO 976 to prevent corrosion of stainless steel slot-die parts and to avoid coagulation when the dispersion is cleaned with cationic polymer flocculants. Formaldehyde-releasing preservatives are incompatible with low-odour carton applications, and residual acrylic monomer must be controlled below the relevant food-contact migration limits rather than below generic industrial emission thresholds.
| Regulatory/technical parameter | Standard or regulation | Boundary |
|---|---|---|
| Indirect food-contact adhesive | FDA 21 CFR 175.105 | Component formulation or migration limit |
| Paper and board contacting aqueous/fatty foods | FDA 21 CFR 176.170 | Component limit |
| EU food-contact framework | Regulation (EC) No 1935/2004 | No transfer of constituents in quantities endangering human health |
| Compostable packaging disintegration | EN 13432 | ≥90% disintegration after 12 weeks |
| pH | ISO 976 | 3.5–5.0 |
| Viscosity | ISO 2555 | 1,200–3,000 mPa·s |
In rotary-screen pigment printing of cotton and polyester-blend knits, acrylic-modified PVAc functions as a formaldehyde-free, APEO-free binder with water resistance after repeated domestic washing. The printed fabric is cured at 150–160 °C for 2–3 min. Residence time below 90 s leaves the binder film thermoplastic and produces wet crockfastness below 3 on the grey scale under ISO 105-X12. High acrylic fractions, above 30 wt% of total binder solids, reduce stiffening at seam lines but increase film thermoplasticity and blocking during sun drying. The formulation boundary for a rotary line is therefore set by dry and wet crockfastness, not by colour strength alone. A print paste containing 12–18 wt% binder solids, 0.5–1.0 wt% ammonium polyacrylate thickener, and a melamine-formaldehyde or blocked isocyanate crosslinker at 0.3–0.6 wt% on binder solids produces a dry crock rating of 4 and a wet crock rating of 3–4 according to ISO 105-X12. Wash fastness is evaluated under ISO 105-C06 at 60 °C with 4 g/L ECE reference detergent. Colour change exceeding 4 on the grey scale after five cycles indicates incomplete film coalescence or excessive surfactant migration. The use of amine-based crosslinkers, such as certain aziridine hardeners, is incompatible with this dispersion because the acidic pH of 4.0–5.0 causes premature coagulation and screen blocking. Similarly, cationic fixatives added after printing can precipitate anionic binder particles and reduce wet crockfastness by creating a discontinuous film. On production-scale printing tables, viscosity drift from 8,000 to 14,000 mPa·s at 20 rpm is tolerated before screen penetration becomes uneven. Viscosity below 6,000 mPa·s causes flushing and loss of fine-line definition. Field observations from multi-head rotary machines show that binder film builds up on nickel screens when the extraction system fails to control humidity above 65%, forcing shutdown for solvent cleaning every 4–6 h instead of the planned 8 h. The binder should therefore be specified with mechanical stability exceeding 30 min under a high-speed mixer at 3,000 rpm without coagulum formation, measured by screening through a 40 μm sieve. Published data for this exact binder composition on viscose-dominated knits is limited, so each rotary screen profile must be validated against ISO 105-X12 wet crock after the exact curing tunnel profile used in production.
At impregnation speeds of 80–120 m/min for hydroentangled cellulose-polyester wipe substrates, the binder bath is maintained at 8–12 wt% solids and a viscosity of 200–600 mPa·s under ISO 2555 at 60 rpm. Unlike coating applications, saturation requires the dispersion to penetrate the fibre network before surface drying. The acrylic-modified PVAc must be diluted with deionized water to a surface tension of 38–42 mN/m using 0.2–0.5 wt% nonionic wetting agent. High foam generation above 150 mL in a dynamic foam test indicates residual defoamer failure and leads to pinholes in the binder film. Binder add-on is controlled at 12–18 wt% dry-on-dry. Below 12 wt%, wet tensile strength under ISO 9073-3 falls below the level required for stacked wet-wipe storage. Above 18 wt%, the sheet becomes papery and loses softness. The acrylic modification specifically delays fibre-to-fibre release in wet storage, but it does not confer antimicrobial action; preservation remains a separate biocidal system. Drying is performed in a steam-can or through-air dryer with a peak web temperature of 110–130 °C. Residual moisture above 4% after curing causes blocking in roll winding, while overdrying above 150 °C embrittles the acrylic phase and leads to lint generation in high-speed converting. The binder is incompatible with elevated levels of boric acid crosslinker above 1.0 wt% because the acidic dispersion precipitates at pH below 3.5 and forms needle-like deposits on the saturator pan. In production, the substrate must be preconditioned to 55–65% relative humidity before saturation. Dry fibre below 40% relative humidity absorbs water too rapidly and causes binder migration to the surface, resulting in a weak core and delamination during wet use. Compliance for cosmetic wet wipes is assessed under the manufacturer’s toxicological risk assessment rather than a single harmonised standard, but the binder must satisfy the finished article’s specific formaldehyde release limit when tested by AATCC 112. Published data for specific microbial challenge testing is limited, but the dispersion itself must meet the relevant purity criteria for the final cosmetic article.
Replacement of a styrene-acrylic latex by acrylic-modified PVAc in interior wall coatings is technically feasible only when the formulation compensates for higher water sensitivity and lower alkali resistance. At 60–75% PVC on an interior matt formulation with a volume solids content of 30–35%, the binder demand is typically 12–16 wt% on total paint. The resulting Stormer viscosity is set at 90–110 KU under ASTM D562, with an ICI high-shear viscosity of 1.2–1.8 P at 25 °C. Film formation at 10 °C requires a minimum film formation temperature below 8 °C measured by ISO 2115. The acrylic modification enables this without high coalescent demand, but the paint still requires 1–2 wt% coalescent on binder solids to prevent early cracking under 40% relative humidity. Wet scrub resistance is evaluated according to ISO 11998 or ASTM D2486. Formulations based on acrylic-modified PVAc typically pass Class 2 under ISO 11998, but Class 1 performance is not consistently reached unless the acrylic content is above 25 wt% of total binder solids. In practice, a dry-film thickness of 50–60 μm over a sealed gypsum substrate is required to measure meaningful scrub data; thinner films fail prematurely by erosion at the gypsum interface. The substitution is most vulnerable on alkaline substrates, where pH above 10 from new plaster can hydrolyse the PVAc segments. A primer with a pH-buffering function or the addition of 0.5–1.0 wt% sodium nitrite is used to suppress flash rusting on metal corner beads but does not fully protect the binder from alkali. Wet adhesion to chalky surfaces is checked by ASTM D3359 Method B. A rating below 3B after 24 h water soak indicates that the formulation has insufficient acrylic content or coalescent distribution. Volatile organic compound content is determined by ISO 11890-2 or EPA Method 24. Typical formulations stay below 30 g/L VOC if ammonia-free neutralizers are used. Storage stability in a finished paint requires freeze-thaw resistance across 3 cycles of −5 °C to 25 °C. Without 2–5 wt% propylene glycol on paint mass, the dispersion coagulates and cannot be restirred. The main processing boundary is pH: the paint must be maintained between 8.5–9.5 after letdown because the binder is supplied at pH 3.5–5.0 and will precipitate if concentrated ammonium hydroxide is added too rapidly. Published data comparing scrub resistance across every tint base is limited, so tinted formulations containing iron oxides or phthalocyanine dispersions require separate testing for ASTM D2486 scrub loss and ASTM D3359 wet adhesion before full commercialisation.
During thread-sewn casing-in at 30–50 cases/min, the rounding and backing adhesive must build fast green strength without penetrating the 70–90 g/m² cotton mull and 100–130 g/m² kraft liner. The adhesive is applied with a disc roller at 60–100 g/m², with a Brookfield viscosity of 2,000–3,500 mPa·s at 6 rpm and 25 °C under ISO 2555. This low-shear viscosity keeps the bead open at the crown and hinge areas while preventing strike-through into the text block. A solids content of 47–53 wt% provides the necessary tack on laminated case covers, but solids above 55 wt% produce case warp in high-humidity binding rooms. The acrylic modification reduces cold-flow during camel-back rounding, which is necessary when the block is rounded with heating irons at 65–80 °C. Pure PVAc at these temperatures softens and allows the sections to shift. After casing-in, the book is stacked under 2–5 kPa pressure for 2–6 h; early reopening force must be low enough to correct hinge alignment. The bonded book is then conditioned at 23 °C and 50% relative humidity for 24 h before trimming. Tensile strength of the hinge after ageing is checked by ISO 1924-2. A drop below 40% of initial tensile strength after 90 °C dry ageing for 7 days indicates that the acrylic phase has lost plasticiser or the PVAc segments have crosslinked prematurely. The adhesive must remain water-resoluble for book repair and recycling, but the acrylic phase should not form grit or skin in the glue pot during breaks longer than 30 min. pH is held between 4.0–5.5. The adhesive is incompatible with stearate-coated felt pads because the metal soap reacts with acid groups and forms a slip layer that reduces mull adhesion. On high-speed lines, the main failure mode is fibre tear on the mull surface after the book is opened. If the tear pattern shifts to the interface between adhesive and coated case stock, the acrylic modification level must be raised within the 10–20 wt% range until fibre failure returns. Published data for this specific application is limited, so a mill trial on the actual mull weave and case cover coating remains mandatory before changing the adhesive solids or acrylic level.
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Water-resistant acrylic-modified poly(vinyl acetate) dispersion, grade WR-PVAc 2040/D4, is supplied as a one-part aqueous dispersion of a vinyl acetate–acrylic ester copolymer stabilised with a polyvinyl alcohol protective colloid. The formulation is intended for wood assembly, edge gluing, veneer lamination, window scantlings, door cores, and furniture joints that require EN 204 D4 classification. Solids content by ISO 3251 is 49–51%; Brookfield RVT viscosity at 23 °C using spindle 6 at 20 min⁻¹ is 14,000–18,000 mPa·s; pH by ISO 976 is 3.2–4.8. Minimum film-forming temperature by ISO 2115 is 3–5 °C, and density at 20 °C is 1.06–1.10 g/cm³. The copolymer contains 18–25 wt% acrylic ester on dry solids; free films immersed 24 h at 23 °C under ISO 62 absorb 12–16% water, compared with 25–32% for a homopolymer PVAc D2 dispersion of equivalent solids. The product is filled into 1,000 L IBCs or 200 L drums and must be stored at 5–30 °C; exposure below 0 °C causes irreversible coagulation.
In direct comparison with hot-melt EVA edge adhesives, the acrylic-modified PVAc does not require melt application at 160–200 °C and remains water-cleanable before cure. Green strength is lower, however; stackable handling after cold pressing is reached in 20–30 min, whereas EVA hot melts develop handling strength in seconds but exhibit higher creep above 60 °C. Against one-component polyurethane wood adhesives, the PVAc dispersion is lower-cost, non-foaming in thick films, and easier to clean, but it is restricted to permeable wood and cellulosic substrates because water must escape through the substrate during film formation. The grade can be formulated to support indirect food-contact compliance under FDA 21 CFR 175.105 and EU 10/2011, provided full cure and migration testing on the finished laminate are completed.
The dispersion is low-formaldehyde; free formaldehyde content by the acetylacetone method is below 5 mg/kg, which is below the detection threshold of BS EN 717-1 for interior air. This property is relevant for furniture and children’s products where indoor emission limits apply.
Wet shear retention on beech is limited by access of water to the polyvinyl alcohol phase, by plasticisation of the acrylic copolymer, and by shallow penetration into dense summerwood. On planed beech strips conditioned to 9–11% moisture content, a toothed roller coater applied 100–120 g/m². Dry tensile shear to EN 205 was 10.5–12.5 N/mm² with wood failure above 60%. After the EN 204 D3 conditioning sequence of 4 days in cold water at 20 °C and 7 days redrying, wet shear remained 2.2–2.8 N/mm², with failure localised at the adhesive–wood interface on summerwood.
The acrylic ester comonomer reduces hydrolytic susceptibility because the ester side groups shield acetate carbonyl sites from acid-catalysed hydrolysis. A homopolymer PVAc of similar solids can fall below 1.0 N/mm² under the same D3 cycle and fails the D4 boil/water sequence. The remaining water-sensitive component is the protective colloid; increasing press pressure above 0.7 MPa forces the dispersion deeper into vessels and reduces the continuous colloid film thickness, improving wet shear. At wood moisture content above 12%, however, capillary dilution lowers local viscosity and can starve the interface under pressure; the failure is fibre tear on softer earlywood and interfacial separation on denser latewood.
On hard maple, wet shear after D3 is lower by 0.4–0.6 N/mm² than on beech because the dense pore network reduces mechanical anchoring. Increasing coat weight to 130–150 g/m² and extending open time to 8–10 min recovers approximately 80% of the beech value. This behaviour is consistent with a penetration-controlled adhesion mechanism rather than a purely chemical bond mechanism.
In a high-frequency edge-gluing line operating at 27.12 MHz with a 12 kW generator and 1.8 m platens, the ionic mobility of the dispersion accelerates energy uptake at the glue line. For 22 mm pine staves, pressing time was reduced from 18–22 min in a cold press to 90–120 s at 0.6 MPa. After 24 h conditioning at 23 °C/50% RH, lap-shear strength by EN 205 was 8.4–9.2 N/mm² with wood failure above 70%. Panels produced under these conditions showed total creep of 1.2–1.8 mm over a 100 mm gauge length after 24 h at 50 °C under 0.1 N/mm² dead load; a plasticised homopolymer PVAc D3 control exhibited 2.4–3.0 mm. The reduced creep is relevant to tabletop and bench-top joints where seasonal movement is visible as seam slippage.
For dense tropical hardwoods such as iroko and meranti, moisture content above 10% and oil content above 1.5% by Soxhlet extraction can inhibit adhesion. Wiping with acetone immediately before spreading improves wet shear by 15–20% on iroko; press time must be extended to 30–40 min at 0.8 MPa because low vessel permeability delays water escape. On a production edge-gluer processing 18 mm meranti staves, batch rejection due to starved glue lines was traced to sanding dust with mean particle size below 80 µm; dust extraction at the coater reduced open-time variability and restored wet shear above 2.0 N/mm².
Bonding of oily teak requires solvent wiping with acetone at 80–100 mL/m²; without wiping, wet shear after D3 fell below 1.2 N/mm² on a production lot, whereas wiped panels reached 2.0–2.4 N/mm². Oil migration to the surface retards wetting, measured by contact angle reduction from 74° to 38° on a goniometer after wiping.
The dispersion is shear-stable under low-shear transfer pumps; however, gear pumps with clearances below 0.2 mm generate local temperatures above 40 °C and viscosity drift of 15–20% within 2 h of recirculation. On a 2.2 m wide roller-coating line with web speed 0.5 m/s, a diaphragm pump with return-line pressure limited to 0.1 MPa maintained coat weight at 85–95 g/m² for an 8 h shift without foaming. Substituting a piston pump caused air entrainment and reduced edge-zone coat weight to 62–68 g/m², producing wet shear below 1.0 N/mm² after D3 conditioning.
Coalescence at board surface temperatures of 12–14 °C is delayed; open time extends beyond 15 min, and delayed clamping can produce dry bond. Above 30 °C and 35% relative humidity, open time falls to 3–4 min, requiring press closure within 90 s after lay-up. These values were recorded on a 600 mm wide coater and a plant-scale cold press with 0.8 MPa capacity. pH drift above 5.5 due to accidental mixing with alkaline cleaning agents destabilises the colloid and produces grit; screen filtration to 125 µm is recommended before spray application.
Storage in open containers under factory conditions raises surface skin formation. Containers left open for 4 h at 30 °C developed a skin layer that blocked 125 µm filters and increased pump suction pressure by 0.03 MPa. Covered containers with nitrogen blanket are unnecessary below 30 °C, but moisture loss from open tanks beyond 2% of batch weight shifts viscosity upward by 10–15%.
For hot-press lamination of 0.6 mm oak veneer to 18 mm MDF at platen temperature 70 °C, the adhesive was applied at 60–80 g/m² and the lay-up entered the press within 45 s. At 0.8 MPa, pressing time to handling strength was 3–4 min; edge skin-over was not observed. When open time was extended to 3 min in a separate trial, the dried film formed a barrier layer that prevented mechanical interlocking with the veneer, and peel strength measured after 24 h at 23 °C fell from 1.8 N/mm to 0.9 N/mm by EN 311. This defines a critical process window of ≤90 s between adhesive application and press closure at platen temperatures above 60 °C.
Capillary penetration into 0.6 mm sliced oak is not the limiting factor; the limiting factor is film coalescence at the exposed surface. Pre-wetting the veneer with water to raise moisture content from 6% to 8% extended open time by 30–45 s but introduced steam blisters at the panel centre when press temperature exceeded 75 °C. This failure mode was eliminated by reducing platen temperature to 65 °C and increasing press time to 5 min.
Foaming in hot-press application was observed when line speed exceeded 0.8 m/s; the film split at the transfer roll produced micro-bubbles that appeared as pinholes in the dried adhesive line. Reducing line speed to 0.5 m/s and using a doctor blade gap of 150 µm eliminated the defect.
The values below are representative for beech assemblies prepared at 0.8 MPa with 100 g/m² coat weight and conditioned for 7 days at 23 °C/50% RH before testing. Published data for one-component polyurethane wood adhesives include a broad range; the figures shown represent the lower quartile of manufacturer technical data for wood bonding grades.
| Property | WR-PVAc 2040/D4 | General-purpose PVAc D2 | One-component polyurethane D4 |
|---|---|---|---|
| Solids content per ISO 3251 (%) | 49–51 | 45–55 | 100 |
| Viscosity at 23 °C (mPa·s) | 14,000–18,000 | 8,000–15,000 | 10,000–20,000 |
| Minimum film-forming temperature (°C) | 3–5 | 12–18 | <0 |
| Durability classification | EN 204 D4 | EN 204 D2 | EN 204 D4 |
| Dry shear on beech by EN 205 (N/mm²) | 10.5–12.5 | 9.0–11.0 | 8.0–12.0 |
| Wet shear after EN 204 D3 (N/mm²) | 2.2–2.8 | <1.0 | 3.0–5.0 |
| 24 h water absorption of free film by ISO 62 (%) | 12–16 | 25–32 | 2–8 |
| Creep after 24 h at 50 °C (mm) | 1.2–1.8 | 3.5–5.0 | 0.5–1.0 |
| Relative adhesive cost per 1,000 kg (index) | 1.0 | 0.7 | 2.2 |
For painted exterior joinery, the product is suitable only where the cured adhesive line is covered by a coating system with dry film thickness above 120 µm and the joint is not exposed to standing water. In an unprotected northern European weathering test on beech lap joints, wet shear fell below 1.5 N/mm² after 12 months of direct rain exposure; this confirms the operational boundary of EN 204 D4 as a frequent water-contact classification rather than an immersion-grade adhesive. The dispersion is incompatible with amine-containing additives, which raise pH above 6.0 and destabilise the protective colloid, causing grit formation and screen blockage in spray nozzles.