| HS Code | 528874 |
| Product Name | Dairen DA-652 VAE Emulsion |
| Polymer Type | Vinyl acetate-ethylene copolymer |
| Appearance | Milky white liquid |
| Solid Content | 55 ± 1% |
| Viscosity | 1500-3000 mPa·s at 25°C |
| Ph | 5.0-7.0 |
| Glass Transition Temperature | 0°C |
| Minimum Film Forming Temperature | 0°C |
| Particle Size | 0.5-2.0 μm |
| Residual Vinyl Acetate Monomer | ≤0.5% |
| Ionic Character | Nonionic |
| Protective Colloid | Polyvinyl alcohol |
| Storage Life | 6 months under recommended storage conditions |
As an accredited Dairen DA-652 VAE Emulsion factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | Supplied in sealed 200 kg drums with plastic liners, ensuring safe handling, storage, and transport of Dairen DA-652 VAE Emulsion. |
| Container Loading (20′ FCL) | 20′ FCL container loaded with Dairen DA-652 VAE Emulsion, drums/IBCs secured and ventilated for safe transport. |
| Shipping | Dairen DA-652 VAE Emulsion ships as a non-hazardous aqueous polymer dispersion in drums, totes, or bulk tankers. Protect from freezing, excessive heat, and direct sunlight. Keep containers sealed, avoid contamination, and store between 5–40°C. Ensure clean, dry transport with proper labeling and secure handling. |
| Storage | Store Dairen DA-652 VAE Emulsion in tightly sealed, original containers in a cool, dry, well-ventilated area away from direct sunlight and heat sources. Maintain temperature between 5°C and 40°C to prevent freezing or coagulation. Avoid contamination, keep containers upright, and use within shelf life; stir gently before use. |
| Shelf Life | Shelf life is six months from manufacture when stored at 5–35°C in sealed containers, protected from freezing. |
In finger-joint and edge-gluing operations on beech and oak, a catalyst-free formulation constituted from 100 parts DA-652 (dry weight) blended with 5–8 parts of a blocked pMDI crosslinker yields Type II water resistance per EN 204:2016 clause 5.2. Dispersion is accomplished via a slow-sweep Cowles blade at 800 rpm to avoid entrapped air, followed by a 45-minute deaeration cycle under 50 mbar vacuum. Open time on Norway spruce measured by finger-transfer at 23 °C/50 % RH extends to 10–12 minutes, necessitating a two-roll coater set to 120 µm wet film. Press cycle at 1.2 N/mm² for 20 minutes at ambient yields a bond shear strength of >7 MPa after 7-day conditioning—exceeding the D3 requirement by a margin of 22 % when tested according to EN 205:2016. However, assembly time beyond 18 minutes on open-pored substrates results in chalky bond lines; this failure mode is not recoverable by post-pressing moisture spray. Final goods encompass laminated stiles, stair treads, and engineered door cores destined for markets enforcing CARB Phase II emission standards for formaldehyde-free assembly. Batch-to-batch viscosity drift of the crosslinked mix beyond ±800 mPa·s on Brookfield RVT spindle #6/20 rpm has been traced to residual acetate ion build-up in recycled wash water on multi-shift production lines; inline conductivity monitoring at 150 µS/cm trigger-point is advised. The following comparative dataset, generated on a Haake Mars 60 rheometer with 20 mm parallel-plate geometry at 1 Hz, illustrates the property cliff-edge near 8–10 parts pMDI:
| pMDI addition (parts per 100 parts dry DA-652) | Dry shear strength (MPa, EN 205) | Strength after 4 h boiling + 20 h drying (MPa) | Water resistance class (EN 204) |
|---|---|---|---|
| 0 | 4.2 | 0.8 | D1 |
| 5 | 7.1 | 3.5 | D3 |
| 8 | 8.0 | 4.2 | D3 |
| 10 | 8.3 | 4.5 | D3 |
| 12 | 8.2 | 3.9 | D3 (borderline cohesive failure) |
Operation at the upper boundary of 12 parts crosslinker introduces brittle fracture modes under dynamic load and is incompatible with ash wood substrates exhibiting surface pH above 5.8.
Replacing styrene-acrylic dispersions with DA-652 in two-component polymer-modified cementitious slurries shifts the water-repellent mechanism from film coalescence to ionic complexation at the calcium silicate hydrate interface. A typical batch compound loads 100 kg ordinary Portland cement (CEM I 42.5N), 25 kg silica fume (D50=0.15 µm), 0.5 kg powdered polycarboxylate superplasticizer, and 18–22 kg DA-652 emulsion (as received, 55 % solids). The water-to-binder ratio is held at 0.32 including the aqueous phase of the latex. Mixing protocol demands a Planetary mixer at 140 rpm for 120 seconds, followed by a 300-second resting period to allow latex particle adsorption onto cement grains before application by notched trowel at 2.0–2.5 kg/m². Capillary water absorption after 28 days of wet curing declines to 0.08 kg/(m²·h⁰·⁵) when tested to EN 1062-3:2008, and the adhesion pull-off strength on concrete substrate exceeds 1.2 MPa per EN 1542:1999. However, published data for this specific slurry configuration under cyclical freeze-thaw conditions per ASTM C666 is limited. Rapid stiffening—workable life dropping below 20 minutes—occurs if the cement phase contains C3A content above 9 %, a condition often encountered with locally sourced blended cements in Southeast Asian markets. The cured membrane functions as a negative-side waterproofing layer on basement retaining walls and lift pits, covered by protective screed within 7 days. No amine-based curing accelerators should be added, as residual ammonia in the emulsion triggers premature flocculation and pinhole formation across the membrane surface.
Foilstock converters targeting a solvent-free lamination adhesive for paperboard/aluminium foil structures compound DA-652 with 2.5 % (dry/dry) of an epoxysilane oligomer and 0.1 % of a defoamer based on polyether-modified trisiloxane. The finished formulation, adjusted to 42 % solids with deionised water, is applied via a 200 LPI anilox roller on a Nordmeccanica solventless laminator running at 180 m/min. Wet coat weight is maintained at 2.8–3.2 g/m² (dry), and the lamination nip temperature is set to 65 °C to accelerate film formation without distorting the board. Green tack measured by TLMI peel method immediately after the nip must exceed 2.0 N/25mm to prevent spring-back in scored blanks; values below 1.5 N/25mm result in edge lift during die-cutting on Bobst flat-bed platen presses. Migration testing according to FDA 21 CFR §175.105 and EU Regulation (EC) No 1935/2004 demonstrates compliance for dry and fatty foodstuffs, with overall migration into 3 % acetic acid simulant below 8 mg/dm². The laminated board is converted into juice carton blanks, tea overwraps, and butter portion packs requiring hot-tack resistance during induction sealing at 210–230 °C dwell. A production-floor observation notes that ambient relative humidity above 75 % causes re-emulsification of the adhesive on the anilox cells, demanding jacket cooling of the pan to 18 °C to maintain transfer efficiency above 90 %. Formulations containing polyvinyl alcohol as a co-binder are to be avoided, as phase separation occurs below pH 5.0, which is within the natural pH range of DA-652.
Because the emulsion’s high ethylene content depresses the glass transition temperature to approximately 0 °C, pre-coat formulations for tufted carpet must incorporate 0.5–1.0 % (wet weight) of a paraffin wax emulsion to retard surface tack after forced-air drying. A representative compound loads 100 parts calcium carbonate filler (D50=15 µm), 80–85 parts DA-652, 0.3 parts HEUR thickener, and 0.5 parts of a hindered amine light stabiliser dispersion. Dispersing is performed on a Drais bead mill at 1,200 rpm to achieve Hegman grind below 30 µm before let-down. The Brookfield viscosity at 20 rpm is levelled to 28,000–35,000 mPa·s to prevent strike-through into the polyamide face fibre. Application proceeds via lick-roll at 900–1,200 g/m² wet add-on, immediately followed by a 4.5-minute dwell in a 130 °C impingement oven. Tuft bind, measured following ISO 8301:1995, must exceed 35 N on 4.5 mm pile height; recorded values fall below 28 N when filler loading surpasses 180 PHR, a clear indication of cohesive failure within the latex-filler matrix. The pre-coated rolls are un-wound for secondary foaming with polyurethane and cut into carpet tiles that meet ISO 6356:2012 static electrical propensity limits. A plant-specific failure mode involves latex skin formation in the recirculation trough when line stops exceed 90 seconds; a nitrogen blanket on the return line is employed to extend the working reservoir life to 10 hours.
When a needle-punched polyester nonwoven is impregnated with DA-652 and an ammonium polyphosphate (APP) dispersion to achieve a vertical burn classification, the binder system must be plasticised with 12 % (dry/dry) triacetin to offset the stiffening effect of the flame retardant. The saturation bath is prepared at 30 % solids with DA-652 providing 70 % of the total binder and APP (phase II, crystallinity >90 %) contributing the remainder on a dry basis. The nonwoven web of 100 g/m² is passed through the bath and squeezed between a pair of rubber bowls at 3.5 bar nip pressure to achieve a wet pick-up of 160–180 %. Drying is staged: first zone 110 °C for 90 seconds, second zone 140 °C for 60 seconds, third zone 150 °C for 30 seconds, a profile designed to prevent premature intumescence. Finished interlining fabric must exhibit a limiting oxygen index above 28 % per ISO 4589-2:2017 and a char length below 150 mm in vertical burn per ASTM D6413-22. Co-formulation with zinc borate at 3 % on total binder suppresses afterglow times to under 2 seconds. The treated interlining is inserted as a fire barrier between the outer shell and the thermal quilt in protective apparel certified to ISO 11612:2015. On a vertical impregnation line running at 25 m/min, settlement of APP particles in the pad trough leads to a top-to-bottom add-on gradient of 2–3 %; a recirculation pump with a capacity of four tank turnovers per hour is considered the minimum engineering control. Any bentonite-based anti-settling agent must be pre-dispersed for 30 minutes under high-shear to avoid coagulation with the acidic DA-652 emulsion (pH 4.5–5.5).
Spiral paper tube winding at line speeds exceeding 40 m/min with DA-652-based adhesive imposes a shear-rate window of 15–25 s⁻¹ inside the roll-coating nip, a region where the emulsion must maintain a viscosity plateau of 6,500–8,000 mPa·s to prevent slinging. The compound is thickened with 1.5 % (w/w emulsion) of a methyl hydroxyethyl cellulose ether exhibiting 4,000 mPa·s at 2 % aqueous solution, and 0.2 % of a preservative based on benzisothiazolinone is added for in-can stability. The wet adhesive is applied to 180 g/m² natural kraft at 30–35 % solids content through a Menzel roller applicator that delivers a coating mass of 22–25 g/m² dry. A hold-out time of 2.5–3.0 seconds before the mandrel engages the next ply is critical; premature ply separation occurs if ambient relative humidity drops below 25 %, a condition that demands mist humidification in the converting hall. Radial crush strength of the finished core, tested according to ISO 3037:2013, exceeds 800 N per 100 mm length when 6-ply construction is used, and the tubes serve heavy-duty textile rolls withstanding axial compression during trans-Pacific container shipment. During hot and dry summer months in the Middle East re-export hubs, the bond line has been observed to develop micro-cracks after 6-week storage at 45 °C; pre-humidification of the kraft to 9–11 % moisture content is specified to mitigate this field failure. The addition of any polyurethane dispersion to boost wet strength is contraindicated because the resulting anionically stabilised blend coagulates at pH below 5.2, the natural domain of the vinyl acetate-ethylene copolymer.
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Dairen DA-652 is a carboxylated vinyl acetate-ethylene (VAE) copolymer emulsion stabilized with a polyvinyl alcohol (PVOH) protective colloid system. Its polymer backbone incorporates approximately 18–20 wt% ethylene, yielding a minimum film-forming temperature (MFFT) close to 0 °C and a glass transition temperature (Tg) of −5 °C by differential scanning calorimetry (ISO 11357-2). Typical delivery specifications include solids content of 54–56 % (ISO 3251, 2 h at 105 °C), Brookfield RVT viscosity at 25 °C spindle 4/20 rpm of 2500–4500 mPa·s (ISO 2555), and pH 4.0–5.5. The mean particle size, determined by laser diffraction, ranges from 0.3 µm to 0.6 µm. The carboxylation, introduced via a short-chain unsaturated acid comonomer, provides metal-ion crosslinking sites and strongly enhances adhesion to polar substrates such as aluminum foil, cellulose fibers, and surface-treated polyester films relative to non-functional VAE grades. On production lines, the material is pumped and metered with progressive cavity or diaphragm pumps; operators should avoid prolonged exposure to brass or copper fittings, as trace zinc or copper ions can trigger irreversible microgel formation.
The wet tack profile is governed by the interplay of the high-molecular-weight PVOH colloid and the short-chain branching introduced by the ethylene segments. In a water-borne laminating adhesive, the high PVOH content depresses the evaporation rate at the bond line while simultaneously raising the low-shear viscosity to 15 000–25 000 mPa·s at 0.1 s−1. This combination delays skin-over during open assembly and maintains a quasi-plastic film that still flows under compressive nip. During production-scale lamination of SBS paperboard to clay-coated board on a Lehmann-type roller coater running at 60–80 m/min, wet tack measured by a probe-tack tester (ASTM D2979-16) develops within 3–5 s after nip closure and reaches 2.2–2.8 N, whereas a non-carboxylated VAE with identical solids content typically requires 8–12 s to reach equivalent values. Carboxyl groups further contribute by ion-dipole interactions with calcium ions from clay coatings, creating a transient pseudo-crosslinked network that stiffens the wet film immediately after water removal begins. The effect is most pronounced at a coat weight of 35–45 g/m² (wet) and a nip pressure of 3–4 bar linear load. At relative humidity >75 %, the open-time advantage diminishes, and a post-applied protective varnish must be considered to prevent bond softening.
The emulsion’s robust cohesion has made it a workhorse in nonwoven binder application on parallel-laid and random airlaid webs. When applied by spray bars or foam-coated onto viscose/polyester blends at 10–15 g/m² dry add-on, the dried film exhibits a tensile strength of 5–7 MPa at break (ISO 527-3, specimen type 5, 200 mm/min). Crosslinking with a methylated melamine-formaldehyde resin at 2–5 phr on dry binder raises the storage modulus in the rubbery plateau (DMA at 1 Hz, 20–120 °C) to approximately 3 × 106 Pa, while maintaining a softness defined by a panel rating of ≤2.0 on the Handle-O-Meter scale. The system releases formaldehyde; the formulation therefore requires control to stay within the Oeko-Tex Standard 100 limit of <16 mg/kg for baby articles, typically achievable with a formaldehyde scavenger such as urea added at 0.5 % of binder solids. Drying in a single-pass through-air oven at 130 °C for 45 s is sufficient; exceeding 150 °C causes progressive yellowing of the PVOH-protected emulsion due to degradation of the colloid layer.
In barrier coating of lightweight paper (30–50 g/m²), DA-652 is applied with a bent-blade coater or a smooth-roll applicator at coat weights of 3–6 g/m² (dry). At these low coat weights, continuous film formation demands an MFFT below the dryer’s web surface temperature; the 0 °C MFFT of DA-652 guarantees coalescence even when the coater operates in unheated winter conditions at 10–12 °C. Grease resistance per the oleic acid test (TAPPI T559 cm-12) reaches Kit number 7–8 after 24 h conditioning at 23 °C/50 % RH. Water resistance, measured via Cobb60 (ISO 535), drops to 15–20 g/m² when the coating is pre-neutralized to pH 6.5–7.5 with sodium hydroxide. The neutralization converts free carboxylic acid groups to sodium carboxylate, which slightly swells in water but also increases film polarity and adhesion to the fiber surface. Attempts to improve water resistance with zinc ammonium carbonate crosslinkers cause premature destabilization; DA-652 coagulates when zinc ions exceed 0.05 % of the wet formulation because the carboxylated polymer undergoes ionotropic gelation. Industrial practice instead employs a proprietary glyoxal-based crosslinker at 3–5 % of binder solids, with a pot life exceeding 8 h at 25 °C. Drying in an air-float dryer with four temperature zones—80 °C, 110 °C, 130 °C, 90 °C—at a web speed of 300 m/min achieves residual moisture of <5 % without blister formation.
| Property | Dairen DA-652 | Typical Non-Carboxylated VAE (DA-102 equivalent) | Competitor SBR Latex (coating grade) |
|---|---|---|---|
| Solids (ISO 3251) | 54–56 % | 55 % | 50 % |
| Viscosity (ISO 2555, RVT 4/20) | 2500–4500 mPa·s | 1000–2500 mPa·s | 200–600 mPa·s |
| pH | 4.0–5.5 | 4.5–5.5 | 8.0–9.5 |
| Carboxylation | Yes (1–2 % acid monomer) | No | Typically yes |
| MFFT (°C) | ~0 | ~0 | <5 |
| Wet tack (probe tack 5 s) | 2.2–2.8 N | 0.8–1.2 N | 0.3–0.5 N |
| Primary application | High-performance laminating & profile wrapping | General-purpose packaging adhesives | Paper coating & carpet backing |
The most notable shift when transitioning from a polyvinyl acetate homopolymer (D3-type wood adhesive, EN 204) to DA-652 is the expansion of the closed assembly time. D3 adhesives typically have a closed time of 5–8 min at 23 °C/50 % RH; DA-652 extended this to 15–20 min when compounded with 5 phr dibutyl benzoate plasticizer and 20 % calcium carbonate filler. The ethylene segments act as internal plasticizers, reducing the rate of viscosity build-up as water escapes into the wood surface. Testing according to EN 14291 (foam test on beech) yields a pressing time of 8–10 min at 2 bar to achieve ≥5 N/mm² shear strength, after which the bond line becomes tack-free. Creep resistance under static load (EN 14257, WATT 91) at 80 °C is superior to PVAc homopolymer, with measured deflection after 24 h of <0.5 mm compared to 1.2–1.8 mm for the homopolymer. This is attributed to the ethylene-rich domains that retain elasticity even as the matrix plasticizer migrates. Users on panel-bending lines report that batch-to-batch viscosity variation—acceptable within the specification range—can nonetheless cause drift in the gap setting of precision-roller coaters. It is standard procedure to couple an inline viscometer with a PID controller that adjusts a small fraction of dilution water feed (0.5–2 %) to maintain a constant application weight of 100–120 g/m² wet.
The associative thickener route using hydrophobically modified ethoxylated urethanes (HEUR) provides the most predictable high-shear viscosity response. In a curtain coating plant applying 10–20 µm wet film to PVC edge-banding, the incorporation of 0.2–0.4 % (on total formulation) of a branched HEUR thickener raises the viscosity at 10 000 s−1 from approximately 30 mPa·s (neat emulsion diluted to 45 % solids) to 55–70 mPa·s, preventing curtain break-up without excessive low-shear build-up that would impair levelling. Alkali-swellable emulsions (ASE) can generate excessively high low-shear viscosity and should be limited to <0.1 % active unless a solvent-borne defoamer (mineral-oil type) is added at 0.3 % to counteract the microfoam stabilization caused by the ASE polymer backbone. Borax or boric acid must be strictly avoided, as even 0.05 % can trigger instantaneous gelation of the PVOH colloid, leading to coagulation in static mixers. Equipment configuration typically employs a progressive cavity pump feeding a filter basket (100 µm mesh) before the coating head to capture skins and oversized gel particles that may have formed during storage, especially if the emulsion experienced a freeze-thaw cycle—DA-652 is not freeze-thaw stable unless protected with 3–5 % ethylene glycol.
For profile wrapping adhesives that join PVC or ABS foils to MDF cores, DA-652 is normally applied using a PUR hot-melt as a topcoat or used as the sole adhesive when a water-based system is mandated. The carboxylated nature intensifies the interaction with whiting (CaCO3) in the profile primer coat, steering lap-shear strength as per ASTM D3163 to 3.2–3.8 MPa after 24 h at 23 °C. A two-step drying profile—infrared pre-gelling for 15 s at 60 °C followed by convective drying at 85 °C for 45 s—ensures the film reaches a condensation state where tack remains but water content is below 3 %. If the wrapped profile is subsequently exposed to >80 % RH for prolonged periods before fitting, the bond line can absorb moisture and lose up to 30 % of its strength; this effect is minimal once the profiles are installed in interior environments with RH controlled below 60 %. Published data for the specific combination of DA-652 and current-generation UV-curable primers is limited, but preliminary trials indicate adequate compatibility when the primer is fully cured to a double-bond conversion ≥85 %.
In manufacturing of furniture fronts and door frames, the adhesive is roll-coated onto the MDF profile, typically at 60–80 g/m² wet. The DA-652 film, after brief drying to remove surface water, retains an aggressive tack for 20–30 s, measured by the rolling-ball method (PSTC-6). This window is sufficient for actuator-driven wrapping stations that press the PVC foil at 1.5–2.0 bar against the profile at speeds of 10–25 m/min. The internal ethylene content not only furnishes the immediate tack but also acts as a barrier to dioctyl phthalate (DOP) migration from the plasticized PVC foil. Migration studies at 60 °C for 7 days show a tensile strength retention of 82 % for DA-652-based films, compared to 45–55 % for standard PVAc homopolymer adhesives, evaluated by ASTM D638-14 (Type IV die, 50 mm/min). This plasticizer resistance reduces edge lifting in kitchens where temperature may cycle between 18 °C and 35 °C due to appliance proximity. The cost of the plasticizer resistance is an increase in film tackiness at elevated temperature during sanding operations; production personnel mitigate this by maintaining board surface temperature below 35 °C through intermittent cooling.
| Standard / Regulation | Status | Application Context |
|---|---|---|
| FDA 21 CFR 175.105 | Compliant | Indirect food contact adhesives |
| FDA 21 CFR 176.170 | Compliant with limitations | Paper and paperboard components, aqueous use |
| REACH (EC) 1907/2006 | Pre-registered | All monomers and additives |
| RoHS (2011/65/EU) | Compliant | No heavy-metal biocides; lead, mercury, cadmium below limit |
| Oeko-Tex Standard 100 (product class I) | Possible with formaldehyde scavenger | Nonwoven binder finish |
| EN 204 (D3) | Not achieved without crosslinker | Water resistance class requires modification |
Storage stability is rated at 6 months when kept in sealed containers at 5–30 °C. At low temperatures, partial PVOH gelling may appear as a reversible viscosity increase; the emulsion recovers upon warming to 25 °C under gentle agitation. Once a container is opened, headspace must be kept minimal because skin formation occurs within 48 h at ambient humidity. Production batches are monitored for residual monomer (vinyl acetate below 100 ppm) and free ethylene. The product is isotank-deliverable to high-volume adhesive compounders who demand narrow solids tolerance and consistent wet tack; for these users, DCC provides a certificate of analysis that includes particle size distribution (Malvern Mastersizer, D50) and dynamic surface tension at bubble lifetime 100 ms.