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Butyl Acrylate

    • Product Name: Butyl Acrylate
    • Factroy Site: Yudu County, Ganzhou, Jiangxi, China
    • Price Inquiry: admin@ascent-chem.com
    • Manufacturer: Ascent Petrochem Holdings Co., Limited
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    Specifications
    HS Code
    Product Name Butyl Acrylate
    Synonyms n-Butyl acrylate; Butyl 2-propenoate; Acrylic acid butyl ester
    Cas Number 141-32-2
    Einecs Number 205-480-7
    Molecular Formula C7H12O2
    Molecular Weight 128.17 g/mol
    Appearance Colorless liquid
    Odor Fruity, pungent
    Boiling Point 145-147 °C
    Melting Point -64 °C
    Flash Point 39 °C (closed cup)
    Autoignition Temperature 267 °C
    Density 0.89 g/cm³ at 20 °C
    Refractive Index 1.418 at 20 °C
    Vapor Pressure 0.43 kPa at 20 °C
    Vapor Density 4.4 (air = 1)
    Solubility In Water 0.14 g/100 mL (slightly soluble)
    Solubility In Organic Solvents Soluble
    Log P 2.36
    Viscosity 0.88 mPa·s at 20 °C
    Un Number UN 2348
    Hazard Class 3 (Flammable liquid)
    Packing Group III
    Hs Code 2916.12.00
    Storage Cool, dry, well-ventilated area away from heat, sparks, and open flames
    Polymerization May polymerize on exposure to heat, light, or peroxides
    Inhibitor Typically inhibited with 10-20 ppm MEHQ

    As an accredited Butyl Acrylate factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing Butyl Acrylate is supplied in 200 L steel drums, securely sealed, clearly labeled as a flammable liquid with hazard warnings.
    Container Loading (20′ FCL) Butyl Acrylate loaded into a 20-foot FCL container in sealed drums or IBCs, secured, labeled, and stowed for ocean shipment.
    Shipping Butyl acrylate is shipped as UN 2348, Proper Shipping Name “Butyl acrylate, stabilized,” Hazard Class 3, Packing Group III. It is a flammable, polymerizable liquid requiring approved packaging, flammable-liquid labels, and inhibitor maintenance. Keep away from heat, sparks, oxidizers, and direct sunlight. Follow DOT, IMDG, or IATA regulations.
    Storage Store butyl acrylate in tightly closed original containers in a cool, dry, well-ventilated, fireproof area away from heat, sparks, flames, sunlight, and oxidizing agents. Keep away from acids, bases, and polymerization initiators. Maintain inhibitor levels and avoid temperatures above 30°C; use grounded equipment, secondary containment, and inspect containers regularly. Ensure adequate ventilation and consult the SDS.
    Shelf Life Butyl acrylate typically has a shelf life of six months when stored cool, dark, and inhibited with MEHQ under air.
    Application of Butyl Acrylate

    Architectural Latex Binder Design Across BA–MMA Composition Gradients

    In waterborne architectural paints, butyl acrylate functions as the primary soft monomer in all-acrylic and styrene-acrylic emulsion polymers. Copolymer composition is selected via the Fox equation to place the dried film Tg between -25 °C for elastomeric exterior wall coatings and +20 °C for interior semigloss topcoats. Industrial reactor programs use a semi-continuous monomer-starved feed profile because the reactivity ratios of butyl acrylate and methyl methacrylate differ sufficiently to cause batch composition drift; the unreacted monomer concentration during the feed stage is normally held below 2 wt% to maintain sequence homogeneity. Minimum film formation temperature is measured according to ISO 2115. A BA-rich latex with a calculated Tg of -10 °C may exhibit an MFFT near 0 °C before coalescent addition, whereas an MMA-rich latex with a Tg of +15 °C requires ester alcohol coalescent to form a continuous film below room temperature. Exterior flat and satin finishes use high-BA binders to achieve free-film elongation above 300 % at 23 °C under ASTM D2370, but the same films show lower König hardness under ASTM D4366 and higher field dirt pickup. Wet scrub resistance is assessed by ASTM D2486 and ISO 11998; the endpoint depends as much on pigment volume concentration and binder volume as on BA content. In production paint plants, the latex is introduced after the high-shear Cowles disperser grind stage at 25 m/s tip speed to avoid latex shear instability and microcoagulum formation in 150 μm discharge filters. Low-VOC compliance under EU 2004/42/EC and US EPA Method 24 drives formulators toward BA-rich binders with reduced coalescent demand. The operational boundary is block resistance: when the BA content in the monomer mix exceeds 55 wt%, stacked films at 40 °C block unless the surface is post-crosslinked with a polyfunctional aziridine or acetoacetate-diamine system.

    Pressure-sensitive adhesive latices are produced from butyl acrylate, 2-ethylhexyl acrylate and acrylic acid at 50–55 wt% solids through a seeded semi-continuous pre-emulsion feed with ammonium persulfate initiation. Here, BA raises the copolymer Tg relative to 2-ethylhexyl acrylate because poly(butyl acrylate) has a homopolymer Tg near -54 °C while poly(2-ethylhexyl acrylate) is near -70 °C. Increasing BA at fixed acrylic acid content therefore shifts the adhesive from aggressive tack toward higher cohesion. Acrylic acid is maintained at 2–4 wt% to anchor carboxyl groups for colloidal stability and for ionic crosslinking with zinc ammonium carbonate or aluminum acetylacetonate. Gel fraction is controlled with tertiary-dodecyl mercaptan at 0.02–0.10 phm; an insoluble fraction below about 60 % gives high peel but poor static shear, whereas highly gelled films resist creep. Peel adhesion is measured at 180 ° angle on stainless steel under ASTM D3330 Test Method A, with a 20 min dwell and a 2 kg roller pass per PSTC-101. Loop tack is evaluated by ASTM D6195 or FINAT FTM 9. Static shear is run on a 25 mm × 25 mm bonded area with a 1 kg mass under ASTM D3654; crosslinked high-BA formulations can exceed 24 h at 23 °C, while uncrosslinked variants may fail before 8 h. Dry adhesive coat weight on 50 μm polyester facestock is held between 20 and 30 g/m², and drying occurs in a forced-air tunnel at 110 °C for 3 min. A documented limitation is plasticizer migration from flexible PVC facestocks into BA-rich adhesives, which reduces shear and causes edge ooze; barrier primers or higher internal crosslink density are required for PVC labelstock. Low-temperature adhesion to corrugated board and polyethylene is improved by BA relative to all-MMA or all-styrene copolymers, but the same softness reduces heat resistance in automotive interior tapes unless the adhesive is crosslinked and compounded with a tackifier resin.

    Which BA–AN Copolymer Ratios Prevent Cold-Crack Failure in Finished Leather?

    When chromium-tanned leather is destined for automotive upholstery or footwear, basecoat acrylic emulsions are formulated with butyl acrylate to depress the glass-transition temperature and with acrylonitrile to raise cohesive strength and solvent resistance. The BA-to-AN weight ratio is the main design lever: a 70/30 ratio balances cold flex and dry-rub resistance, while a 60/40 ratio increases hardness for luggage and upholstery leather. Cold-crack resistance is tested on a Bally flexometer according to ISO 5402, commonly at -20 °C for automotive specifications. The finish is applied to crust leather by spray or reverse roll coater at a dry add-on of 20–40 g/m². Crosslinking is required for wet-rub and wet-soak performance and is introduced with a polyfunctional aziridine or polycarbodiimide at 0.5–1.5 wt% on binder solids; pot life after crosslinker addition is limited to 8–24 h at 20 °C. Adhesion of the finish to leather is measured by ISO 11644, and finished leather flex endurance is supported by coating elongation above 200 % under ISO 527-type tensile testing. The operational boundary is narrow: increasing BA above roughly 80 wt% without sufficient crosslinker produces a soft, blocking basecoat that retains press marks and transfer marks during stack storage; increasing acrylonitrile above 40 wt% reduces low-temperature flex life and may require coalescing solvent that increases volatile organic content beyond leather-plant limits.

    In nonwoven highloft and papermaking felt binder applications, self-crosslinking butyl acrylate–vinyl acetate and butyl acrylate–methyl methacrylate latices are applied by spray or foam at dry add-on levels of 8–25 g/m². BA contributes the low Tg required for soft hand and drape; methyl methacrylate or vinyl acetate hardens the film and raises tensile strength. The crosslinking monomer N-methylolacrylamide at 2–4 wt% on monomers reacts during thermal curing at 120–150 °C for 1–3 min in a through-air oven. Under-cure leaves wet tensile retention below 60 % of dry tensile after laundering, while over-cure causes yellowing and loss of fiber wetting. Tensile properties are tested with ISO 9073-3 and ASTM D5034; wet tensile is determined after one or five laundering cycles per ISO 6330 or AATCC 135. The binder must remain stable under high-shear spray application; coagulum above 200 ppm on a 45 μm screen causes spray nozzle plugging and visible specks on the web. Pigment printing pastes use a similar BA-rich copolymer but require controlled particle morphology to limit binder migration and crocking. The printed fabric is dried at 150 °C and assessed for dry and wet crockfastness by ISO 105-X12. A critical threshold exists for BA content in pigment printing: excessive soft monomer reduces film toughness and increases dry crocking, so commercial binders are designed as core-shell or bimodal particle size distributions to separate soft hand from rub resistance. Production-scale curing ovens are zoned; the first zone removes water at 100–110 °C and the final zone crosslinks at 140–150 °C, because full crosslink before moisture removal creates surface skinning and weak adhesion to cellulosic fibers.

    Joint movement capability in acrylic sealants depends on BA dosage and plasticizer migration

    Acrylic sealant dispersions for interior and exterior joint sealing are formulated from BA-rich acrylic emulsions with Tg values between -30 and -45 °C, compounded with fillers, plasticizers and thickeners in high-shear planetary mixers. The low Tg permits joint movement at -20 °C without cohesive failure; movement capability is classified according to ISO 11600 or ASTM C920 as class 7.5 or 12.5 only after adhesion and cohesion tests at extension and compression. Slump is measured with ASTM D2202; tack-free time is determined by ASTM C679. High BA improves elongation and low-temperature adhesion to aluminum, glass and concrete, but it also reduces Shore A hardness and increases dirt embedment. Plasticizer migration from the cured sealant into porous substrates is a long-term failure mode: loss of plasticizer raises tensile modulus and can crack the sealant during joint expansion. Published data for specific plasticizer migration rates in BA-rich sealants is limited, so joint design should account for the fact that wet-applied acrylic sealants shrink by 20–30 vol% during water evaporation. The operational boundary is depth of cure: a bead deeper than 12 mm cures slowly at the core and may fail cohesion during movement after only 24 h. Gun-grade formulations require high-shear stability; a bench-top Cowles rotor at 1500 rpm can generate localized heating above 60 °C, causing skin formation unless the dispersion is cooled.

    When a BA-rich dispersion is metered into cementitious waterproofing slurries, polymer-cement ratio controls film continuity

    Before cement hydration consumes the mixing water, a BA–MMA or BA–styrene dispersion must remain colloidally stable in a two-component polymer-modified cementitious membrane. The liquid component is mixed in a low-speed mortar mixer according to EN 196-1 with a cement–silica filler blend. The polymer-cement ratio is kept between 0.10 and 0.25 by weight; below 0.10 the cured membrane lacks crack bridging, while above 0.25 compressive strength and water vapor permeability fall below values for tile-bearing substrate. BA-rich dispersions with an MFFT below 5 °C coalesce progressively as water is consumed by cement hydration; the film forms around hydrate grains and bridges microcracks under EN 14891 crack-bridging tests at -10 °C. The high ionic strength and calcium concentration of cement pore solution demand an anionic or nonionic emulsifier package; inadequately stabilized latex coagulates during mixing, detected as a viscosity increase above 10 000 mPa·s and visible polymer aggregates on a 0.5 mm mesh. Application by notched trowel or airless spray requires a pot life exceeding 30 min at 20 °C. Water impermeability is tested under EN 12390-8 or ASTM C836; adhesion to concrete is measured by EN 1542. A critical threshold exists for BA content: high BA improves flexibility but reduces hardness and wet abrasion resistance; field failures appear as soft spots and blistering when water ponds before full cement cure. The system is incompatible with gypsum-based substrates and with rapid-hardening calcium aluminate cement unless the latex pH is adjusted above 8.

    ApplicationStandard designationReported parameter
    Polymer-modified cementitious waterproofingEN 14891Crack bridging at -10 °C
    Dispersion adhesion to concreteEN 1542Pull-off adhesion on concrete
    Slurry water impermeabilityEN 12390-8Water penetration depth
    Acrylic joint sealantISO 11600Movement class 7.5 or 12.5
    Sealant tack-free timeASTM C679Tack-free interval
    Sealant slumpASTM D2202Slump length

    Controlling Crosslinked Butyl Acrylate Core–Shell Morphology in PVC Impact Modifiers

    Core-shell acrylic impact modifiers are manufactured by seeded emulsion polymerization of crosslinked polybutyl acrylate cores, followed by grafting of a poly(methyl methacrylate) shell to enable dispersion in PVC window profiles, pipe fittings and siding. The poly(butyl acrylate) core is crosslinked with 0.3–1.0 wt% of allyl methacrylate or divinylbenzene; under-crosslinking allows core deformation during extrusion and produces weld-line brittleness, while over-crosslinking suppresses cavitation and reduces low-temperature impact. The latex particle size is controlled between 150 and 350 nm because smaller particles reduce impact efficiency and larger particles lower surface gloss. The dried core-shell powder is melt-blended into PVC on a parallel twin-screw extruder with a 25:1 L/D ratio at barrel temperatures of 170–190 °C. Notched Izod impact strength is measured per ASTM D256 at 23 °C and 0 °C; low-temperature improvement over unmodified PVC depends on rubber volume fraction and interparticle spacing, not on modifier particle size alone. The BA rubber core provides better weatherability than butadiene-based modifiers under ISO 4892-2 xenon arc aging, but residual BA monomer above 50 ppm in the modifier powder can cause odor and film defects in coextruded capstock. Formulators must maintain PVC melt temperature below 200 °C to avoid thermal degradation of the acrylic shell.

    For blade-coated freesheet and coated board, a carboxylated BA–styrene latex at 48–50 wt% solids serves as the secondary binder alongside starch or carboxymethyl cellulose; the relevant specification is limited to offset pick resistance measured as wet and dry picking with IGT or Prufbau instruments per ISO 3783, and published binding strength data for this specific configuration is limited.

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    Certification & Compliance
    More Introduction

    Butyl acrylate (n-butyl acrylate, BA), CAS 141-32-2, formula CH2=CHCOO(CH2)3CH3, molecular weight 128.17 g/mol, is supplied as a clear, inhibited liquid monomer for radical polymerisation. Commercial product designations include Butyl Acrylate Monomer, Polymer Grade, stabilised with 10–20 mg/kg monomethyl ether hydroquinone (MEHQ); Technical Grade with wider acidity and water boundaries; and Low-Acidity Grade for downstream emulsion polymerisation where anionic surfactant compatibility is critical. Under ASTM D3547 classification, polymer-grade material is specified with ester purity ≥99.5 wt%, colour ≤10 Pt-Co (ASTM D1209), water ≤0.05 wt% (ASTM D1364), and acidity as acrylic acid ≤0.009 wt% (ASTM D1613). The liquid has a density of 0.894 g/cm3 at 20 °C, a boiling point of approximately 145 °C at 101.3 kPa, a closed-cup flash point of 36–39 °C, and a vapour pressure near 0.5 kPa at 20 °C. The water solubility is 0.14 g/100 g at 20 °C, which is lower than for methyl acrylate and ethyl acrylate. These boundaries matter because partially oxidised or water-saturated monomer feed changes emulsion particle size and latex stability.

    Polymer-grade n-butyl acrylate specification boundaries and test methods
    Parameter Limit or typical value Test procedure
    Ester purity ≥99.5 wt% ASTM D3362
    Water content ≤0.05 wt% ASTM D1364
    Acidity as acrylic acid ≤0.009 wt% ASTM D1613
    Colour, Pt-Co ≤10 ASTM D1209
    Inhibitor, MEHQ 10–20 mg/kg ASTM D3125
    Appearance Clear, free of suspended matter Visual inspection

    Technical grade butyl acrylate may contain higher concentrations of acrylic acid, n-butanol, and n-butyl acetate; the polymer-grade specification is preferred for automated continuous feed systems because 0.1 wt% additional water can perturb redox initiator feeds in continuous emulsion polymerisation. The monomer is miscible with common esters, ethers, aromatic hydrocarbons, and ketones, but its reduced water solubility compared with ethyl acrylate translates into lower aqueous-phase oligomer formation during emulsion processes.

    What process constraints govern emulsification feed strategy in butyl acrylate copolymerisation?

    Butyl acrylate is rarely homopolymerised at production scale because the homopolymer is soft and lacks cohesive film strength. Instead, it is co-fed with methyl methacrylate, styrene, acrylonitrile, or vinyl acetate in thermostatted reactors. In seeded semi-continuous emulsion polymerisation, butyl acrylate is delivered by monomer-starved feed because the heat of polymerisation is high. The enthalpy of polymerisation is approximately 77 kJ/mol for the acrylate double bond; a delayed or interrupted feed can create monomer accumulation, and sudden unpolymerised monomer pooling leads to a sharp exotherm that exceeds condenser duty. Production experience on 25 m3 stainless steel reactors with reflux condensers and 45° pitched-blade turbines shows that loss of agitation during butyl acrylate feed can produce local gel deposits on the agitator shaft and temperature probe, generating coagulum that is not present in smaller pilot batches.

    Emulsion polymers produced with butyl acrylate typically use anionic surfactants and ammonium persulfate initiator at 0.3–0.6 wt% on total monomer. The resulting latex particle size is measured by dynamic light scattering; batches with 120–250 nm mean particle size and narrow polydispersity are standard for pressure-sensitive adhesives and architectural binders. If BA feed is not separated from acidic monomers, acid-catalysed side reactions can increase the aqueous-phase ion burden and reduce coagulum stability. The operating boundary is therefore a pH setpoint of 2–4 during feeding, followed by neutralisation to 7–8 only after monomer conversion exceeds 99.5%. Published data for this specific reactor configuration is limited, but the need for slow BA feed in large-volume free-radical polymerisation is well documented.

    Pressure-sensitive adhesive formulation windows and 180° peel resistance

    In pressure-sensitive adhesives, butyl acrylate provides the low glass transition temperature required for tack, with homopolymer glass transition measured by differential scanning calorimetry under ASTM E1356 at -49 °C to -54 °C. Typical emulsion PSA compositions copolymerise 80–95 wt% butyl acrylate with 2–5 wt% acrylic acid or methacrylic acid and a hard comonomer; the carboxyl groups provide internal cohesion and crosslinking sites. The 180° peel adhesion is evaluated on stainless steel panels under ASTM D3330, loop tack under ASTM D6195, and shear holding power under ASTM D3654. In silicone-coated release liner constructions, a 25 g/m2 dry coat weight can yield peel values of 6–18 N/25 mm, depending on acid monomer content and crosslinker. When residual n-butyl acrylate is not stripped below 500 ppm, peel may be artificially high initially and then drift downward as the unreacted monomer migrates into the facestock.

    The operational boundary with butyl acrylate PSA latices is shear resistance at elevated temperature. A low-acid formulation below 2 wt% acrylic acid may show clean peel and high tack but can fail shear testing under 1 kg load at 70 °C within 1 h. Additions of methyl methacrylate above 10 wt% raise cohesion but depress tack because the copolymer glass transition moves away from the Dahlquist criterion range, where storage modulus at application temperature should be below 0.3 MPa at 1 Hz. Compatibility constraints require avoidance of free primary amines unless fully consumed before addition, because unreacted amines can add to residual acrylate unsaturation and shift peel behaviour.

    When methyl methacrylate is co-fed to shift free-film hardness and tensile strength

    In architectural acrylic binders, butyl acrylate functions as the flexibilising monomer, while methyl methacrylate functions as the hardening monomer. Copolymer glass transition is estimated by the Fox equation: a 50:50 mass mixture of BA and MMA yields a computed midpoint glass transition near 7 °C, assuming bulk homopolymer glass transition values of 218 K for poly(butyl acrylate) and 378 K for poly(methyl methacrylate). If the BA fraction exceeds 60 wt%, free films produced by drawdown show high elongation at break under ISO 527-3, often 300–600%, but tensile strength may remain below 6 MPa and block resistance measured by ASTM D4946 deteriorates. A BA reduction toward 30 wt% raises tensile strength above 15 MPa, but creates low-temperature cracking risk when the binder is applied to masonry below 5 °C.

    Production experience with high-Tg latex binders shows that butyl acrylate must be fed in parallel with methyl methacrylate rather than sequentially; sequential feeds can produce a core-shell particle but also create composition drift that produces two glass transitions by ASTM E1356, indicating a heterogeneous phase structure. For facade paints tested under EN 1062-1, such heterogeneity can appear as early dirt pickup or variable wet scrub resistance, particularly on north-facing exterior surfaces.

    The performance difference between butyl acrylate and other acrylic monomers is controlled by side-chain length, water solubility, and volatility. Ethyl acrylate has higher water miscibility and a higher vapour pressure, requiring different volatile organic compound handling. 2-Ethylhexyl acrylate delivers a lower homopolymer glass transition and greater hydrophobicity, but its molecular weight is higher and its diffusion mobility in copolymer matrices is lower. Methyl methacrylate is a hard methacrylate reference monomer, not an acrylate ester flexibiliser. Table 2 compares typical industrial values for inhibited monomer grades; the values are method-dependent and should be verified against the supplier certificate of analysis.

    Comparative properties of acrylic monomers commonly used alongside butyl acrylate
    Parameter n-Butyl acrylate Ethyl acrylate 2-Ethylhexyl acrylate Methyl methacrylate
    Homopolymer glass transition -49 to -54 °C -24 °C -65 °C 105 °C
    Boiling point at 101.3 kPa 145 °C 99.7 °C 216 °C 100.3 °C
    Water solubility at 20 °C 0.14 g/100 g 1.5 g/100 g 0.01 g/100 g 1.5 g/100 g
    Vapour pressure at 20 °C 0.5 kPa 3.9 kPa <0.01 kPa 3.9 kPa

    Butyl acrylate therefore occupies an intermediate position among flexible acrylic monomers. It is more hydrophobic than ethyl acrylate and less volatile, which improves process safety in large-volume emulsion polymerisation, but it is not as low-Tg as 2-ethylhexyl acrylate. In practice, the choice of butyl acrylate is often retained when balanced adhesion, water resistance, and moderate vapour pressure are required in a single monomer feed.

    Controlling residual monomer and oxygen-dependent inhibition during storage

    Butyl acrylate is stabilised with MEHQ, and the inhibition mechanism is oxygen-dependent. Storage under nitrogen blanketing is therefore not appropriate for inhibited butyl acrylate because oxygen starvation can produce dormant inhibitor and create a polymerisation hazard. Atmospheric storage tanks maintained at 25–35 °C with headspace air and monitored dissolved oxygen above 4 ppm are specified in supplier handling guidance. Recirculation loops should be continuously operated to prevent stagnant zones; monomer returning from a vent condenser is inhibitor-depleted and must be recombined with the stabilised bulk through a dip leg, not allowed to stratify in the top layer. The vapour is heavier than air, with a vapour density relative to air near 4.4; extraction points should therefore be located at low level in enclosed areas.

    Residual butyl acrylate in finished acrylic copolymers is controlled by redox post-polymerisation and steam or vacuum stripping; residual n-BA below 100 mg/kg is often achieved in polymer dispersions, but this is formulation-dependent. Published data for this specific configuration is limited; migration testing is required for food-contact adhesives under FDA 21 CFR 175.105 and for low-odour architectural paints. The monomer is a skin and respiratory sensitiser under REACH, and closed transfer systems with fume extraction are required wherever heated bulk storage, drum offloading, or reactor charging occurs.

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