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изооктил акрилат

    • Название продукта: изооктил акрилат
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    Спецификации
    Код ТН ВЭД
    Название продукта изооктил акрилат
    Химическое название Изооктилпроп-2-еноат
    синонимы изооктильный эстер акриловой кислоты; изооктил-проп-2-еноат; ИОА
    Cas номер 29590-42-9
    Номер ЕС 249-707-8
    Молекулярная формула С11Н20О2
    молекулярный вес 184,28 г/моль
    внешность Бесцветная жидкость
    запах Эстер-подобный
    точка кипения 120-125 °C при 10 mmHg
    точка вспышки 82 °C (закрытый тигель)
    плотность 0,880 г/см3 при 25 °C
    показатель преломления 1,437 при 20 ° C
    вязкость 2 мПа·с при 20 °C
    Растворимость в воде Практически нерастворяемый в воде
    давление паров 0,01 мм рт. ст. при 20 °C
    Ингибитор полимеризации 50-100 ppm МЭХК
    условия хранения Прохладная, сухая, хорошо вентилируемая область подальше от тепла, света и окисляющих агентов

    Как аккредитованная фабрика по производству изооктил-акрилата, мы соблюдаем строгие протоколы качества - каждая партия подвергается строгим испытаниям для обеспечения последовательных стандартов эффективности и безопасности.

    Упаковка и хранение
    Упаковка Упаковка: Изооктилакрилат в стальных барабанах 200 л или сумках IBC 1000 кг, маркированных и запечатанных.
    Погрузка контейнера (20-футовый контейнер) Изооктилакрилат загружается в контейнер 20' FCL, упаковывается в барабаны, утвержденные ООН, надежно закрепляется, маркируется и отправляется в соответствии с правилами IMDG.
    Доставка Изооктилакрилат доставляется в виде стабилизированной горючей жидкости. Для воздушного транспорта следует использовать № ООН 3334, регулируемая для воздушных перевозок жидкость, не указанная в другой категории (изооктилакрилат), класс 9, ГП III. Сухопутные/морские перевозки, как правило, не регулируются. Держите контейнеры прохладными, подальше от источников зажигания и убедитесь, что присутствует ингибитор полимеризации.
    Хранение Храните изооктил-акрилат в прохладном, сухом, хорошо вентилируемом, огнестойком месте, подальше от тепла, искр, открытого пламени и прямого солнечного света. Держите контейнеры плотно закрытыми и вертикальными. Отделяется от окислителей, кислот, оснований и инициаторов полимеризации. Поддерживайте поставленный ингибитор и контролируйте температуру хранения. Используйте заземление и связывание при обращении. Избегайте длительного хранения выше рекомендованных пределов для предотвращения полимериз
    Срок годности Срок хранения изооктил-акрилата обычно составляет 12 месяцев, когда он хранится в прохладном, темном, сухом и ингибированном состоянии, подальше от тепла и света.
    Применение изооктильного акрилата

    A branched C8 alkyl acrylate with a reported homopolymer glass transition between −50 °C and −58 °C is consumed in solvent-free hot-melt pressure-sensitive adhesive lines when low-temperature tape unwind and low-energy surface wet-out are required. The monomer feed in a typical twin-screw bulk polymerization line with L/D between 48:1 and 64:1 contains 55–70 wt% isooctyl acrylate, 20–35 wt% n-butyl acrylate or methyl acrylate, 2–6 wt% acrylic acid, and 0.2–0.6 wt% diphenyl(2,4,6-trimethylbenzoyl)phosphine oxide as photoinitiator. Melt viscosity at 130 °C is commonly 15,000–60,000 mPa·s depending on conversion and crosslinker addition. The adhesive mass is slot-die coated onto 23–36 µm PET or BOPP carrier at a dry film thickness of 80–140 µm, followed by mercury-arc or LED UV cure at 600–1,200 mJ/cm² UV-A dose. Peel adhesion is measured on stainless steel after 24 h dwell under ASTM D3330/D3330-04, loop tack under PSTC-16, and shear adhesion failure temperature under ASTM D4498. Food-contact tape constructions reference FDA 21 CFR 175.105 and 21 CFR 176.170, while REACH registration is required for European monomer supply. The central process boundary is tackifier loading: hydrogenated rosin ester above 45 wt% raises the continuous-phase glass transition above −20 °C and reduces low-energy substrate wet-out, whereas below 15 wt% the storage modulus at 25 °C commonly exceeds 0.3 MPa and violates the Dahlquist criterion for tack. Pilot-line behaviour on 1200 mm slot-die coaters shows edge-bead instability when melt viscosity drops below 8,000 mPa·s at 120 °C, producing coat-weight variation above ±2 g/m².

    Formulation and test matrix for hot-melt IOA-based pressure-sensitive adhesive
    ParameterTypical rangeEquipment /standardBoundary condition
    Isooctyl acrylate feed fraction55–70 wt%Twin-screw extruder L/D 48:1–64:1Below 50 wt% raises peel on HDPE sharply
    Photoinitiator BAPO0.2–0.6 wt%UV dose 600–1,200 mJ/cm²Below 400 mJ/cm² residual monomer exceeds 0.1 wt%
    Hydrogenated rosin ester15–45 wt%DMA at 1 Hz; ASTM D4440Above 45 wt% Tg > −20 °C; below 15 wt% G′ > 0.3 MPa
    Coating weight80–140 µm dry on 23–36 µm PETSlot die at 120–140 °CEdge bead instability below 8,000 mPa·s

    What Changes When Branched C8 Acrylate Enters a UV Flexo Ink Formula?

    In UV-curable flexographic inks, isooctyl acrylate functions as a low-viscosity monofunctional reactive diluent with a room-temperature viscosity of 2–4 mPa·s and a reported homopolymer Tg near −58 °C. It replaces ethoxyethoxyethyl acrylate or 1,6-hexanediol diacrylate at 10–25 wt% to reduce ink viscosity to 200–600 mPa·s at 25 °C, allowing high-speed narrow-web flexo presses running at 150–250 m/min to maintain clean anilox release at 35–38 °C. The monoacrylate functionality lowers crosslink density; as IOA loading rises past 25 wt%, MEK double-rub resistance measured by ASTM D5402 often falls below 100 rubs unless compensated with more than 8 wt% trimethylolpropane triacrylate. Formulation control is anchored to a hydroxyl-functional polyester acrylate oligomer at 40–55 wt%, a photoinitiator package of 2–4 wt% alkylphenone plus acylphosphine oxide, and 1–2 wt% of a silicone acrylate surface agent. Cure units are typically gallium-doped mercury lamps with an output of 160–240 W/cm and a peak irradiance of 0.8–1.5 W/cm² in the UV-A band. Under-cure at lamp speeds above 200 m/min is detected as residual ethyl acetate extractables above 5 mg/m². End uses include shrink-sleeve inks and non-absorbent film substrates where adhesion is verified by ISO 2409 cross-cut classification 0 or 1 and by ASTM D3359 tape pull. REACH compliance requires residual monoisooctyl acrylate below 200 mg/kg in the printed article, while Swiss Ordinance 817.023.21 and Nestlé guidance impose migration limits for food packaging. A sharp process boundary appears when pigment loading exceeds 22 wt%: higher opacity reduces photon penetration through the wet film and causes bottom-layer under-cure, leading to residual odour and poor rub resistance.

    Sealant Movement Capability and Low-Temperature Recovery After Compression

    Solvent-borne and hybrid acrylic sealants employing isooctyl acrylate are formulated for exterior facade joints with movement capability tests under ISO 9047 and durability under ASTM C920-18a. A typical terpolymer consists of 45–60 wt% isooctyl acrylate, 30–45 wt% butyl acrylate or 2-methoxyethyl acrylate, and 3–8 wt% methacrylic acid, polymerised to a molecular weight of 150,000–300,000 g/mol. The sealant formulation includes 25–35 wt% polymer solids, 30–40 wt% ground calcium carbonate with a top cut of 10 µm, 15–25 wt% phthalate-free plasticiser such as DINCH, and 2–4 wt% of a silane adhesion promoter. Shore A hardness after 28 days is 15–25, elastic recovery under ISO 7389 exceeds 85%, and low-temperature flexibility without cracking is confirmed at −30 °C. In production, high-shear dispersers with a tip speed of 15–20 m/s incorporate the filler without destroying the acrylic latex particle structure. A known failure mode occurs when the silane level is raised above 4 wt%: moisture-triggered condensation builds a stiff interpenetrating network, raising modulus above 0.75 MPa and reducing movement capability from ±25% to below ±15%. For that reason, adhesion is qualified on aluminium and glass substrates under ISO 8339 to 0.4 MPa tensile stress, avoiding formulations that trade cohesion for excessive interfacial strength.

    Textile pigment printing pastes using isooctyl acrylate-containing binders are employed where a soft handle below a total hand value of 3.0 is required but crock fastness must survive industrial curing at 150 °C for 3 min. The aqueous dispersion is typically a self-crosslinking acrylic copolymer of 30–40 wt% isooctyl acrylate, 45–55 wt% n-butyl acrylate, 5–10 wt% acrylonitrile or styrene, and 2–5 wt% N-methylolacrylamide. Printing paste formulation comprises 10–20 parts binder solids per 100 parts water, 3–6 parts high-density thickener, and 5–8 parts melamine-formaldehyde or blocked isocyanate crosslinker. Application is by rotary screen at 80–125 mesh on cotton, polyester, or cotton/spandex knits, followed by stenter-frame drying at 120–130 °C for 60–120 s and curing at 150–160 °C for 90–180 s. Wet crock fastness is tested per AATCC 8 or ISO 105-X12; a rating below grade 3 indicates insufficient crosslinking or excess free acrylic acid. Wash fastness is checked under ISO 105-C06 A1S. Discharge printing requires the binder to withstand 5–8 g/kg of sodium sulphoxylate formaldehyde without coagulation. The main operational boundary is the minimum film-forming temperature: lowering IOA content below 20 wt% raises MFFT above 10 °C, causing blocking in stack-to-stack storage at 35 °C and 65% RH.

    When Wound Dressing Adhesion Must Increase Without Raising Skin Stripping Force

    Silicone-gel adhesives are often specified for skin-contact medical devices, but an IOA-based acrylic layer is used when a thinner profile and higher moisture vapour transmission rate are required. In a typical UV-cured skin adhesive, isooctyl acrylate is copolymerised with 2-hydroxyethyl acrylate and acrylic acid at a monomer ratio of 70–85 wt% IOA, 10–20 wt% hydroxyethyl acrylate, and 2–6 wt% acrylic acid. The crosslinked adhesive reaches gel contents above 65 wt% after UV cure at 800–1,200 mJ/cm², yet retains a plateau modulus below 0.35 MPa at 37 °C. Adhesion to human skin is measured by a 180° peel test with a crosshead speed of 300 mm/min on forearm volunteers following a modified ASTM D3330 protocol, with typical peel values of 0.8–2.5 N/25 mm. MVTR is tested per EN 13726-2 with an upright cup at 37 °C and 20% relative humidity; values above 1,500 g/m²/24 h are achievable only when coat weight is kept below 40 g/m². The process conflict is direct: coat weights above 50 g/m² raise peel adhesion but reduce MVTR below clinically acceptable levels for wounds with moderate exudate. Cytotoxicity, sensitisation, and irritation must be evaluated under ISO 10993-5, ISO 10993-10, and ISO 10993-23. Residual acrylic acid is monitored by HPLC to below 100 ppm. For devices sold in Europe, compliance with EU MDR 2017/745 requires chemical characterisation per ISO 10993-18, including extraction with hexane and ethanol-water to detect oligomeric acrylate species. A production bottleneck observed on pilot coating lines is the need to maintain web tension below 20 N on 25 µm polyurethane film; higher tension causes neck-in and uneven coat weight outside ±2 g/m².

    Acrylic waterproofing membranes for below-grade concrete are modified with isooctyl acrylate when crack-bridging at −20 °C is a specification requirement. Published data for this specific IOA-rich configuration is more limited than for pressure-sensitive adhesives; formulation ranges are drawn from liquid-applied membrane technical datasheets. A two-component spray system typically contains 25–35 wt% isooctyl acrylate, 30–45 wt% n-butyl acrylate, 15–25 wt% methyl methacrylate, and 2–5 wt% acrylic acid in the base latex. The compound is spray-applied in two coats at a combined wet thickness of 800–1,200 µm, with a mineral-spirit-free formulation to meet VOC limits under ASTM D6886. Crack bridging is evaluated by ASTM C1305-19 at −20 °C after 7 days at 23 °C and 50% RH; long-term water resistance is tested per ASTM C836-20. The end product is used as a waterproofing membrane for plaza decks, foundations, and tunnel liners. A practical threshold is the methyl methacrylate content: above 25 wt% the dried film does not bridge cracks wider than 1.5 mm at −20 °C, while below 15 wt% surface tack increases and dirt pickup becomes unacceptable under hydrostatic resistance testing.

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    Сертификация и соответствие требованиям
    Более подробное введение

    Isooctyl acrylate is a branched alkyl acrylate ester supplied as a clear, colorless liquid with the molecular formula C11H20O2, CAS registry number 29590-42-9, and molecular weight 184.28 g/mol. A common high-purity stabilized grade designated IOA-HP is used in radical polymerization operations where low acid content and controlled inhibitor concentration are required. Bulk specification data for IOA-HP typically report GC purity ≥ 99.0 % according to ASTM D3362, water ≤ 0.05 wt% by ASTM E203, acidity as acrylic acid ≤ 0.01 wt% by ASTM D1613, and APHA color ≤ 10 by ASTM D1209. Density at 20 °C lies between 0.878 g/cm³ and 0.884 g/cm³ when tested by ASTM D4052. The closed-cup flash point is typically reported in the 79–86 °C range. The product is stabilized with 15–20 ppm monomethyl ether hydroquinone in the standard grade; low-inhibitor variants containing ≤ 5 ppm MEHQ are used for ultraviolet and electron-beam curing where excessive inhibitor consumes photoinitiator radicals. The ester side group is a distribution of branched octyl isomers, a feature that distinguishes the monomer from linear octyl acrylate and from the more widely available 2-ethylhexyl acrylate.

    Because the octyl branch is distributed, the monomer imparts low-temperature flexibility and hydrophobic character to acrylic copolymers. It is used as a backbone monomer in solvent-borne, waterborne, and hot-melt pressure-sensitive adhesives; as a reactive diluent in radiation-curable coatings; and as a comonomer in architectural caulks and sealants. In these applications, the branched alkyl group alters viscoelastic response differently from the ethyl branch of 2-ethylhexyl acrylate.

    What Distinguishes Isooctyl Acrylate from 2-Ethylhexyl Acrylate and n-Butyl Acrylate?

    At the molecular level, 2-ethylhexyl acrylate contains a single ethyl branch at the C2 position, while isooctyl acrylate is an isomeric mixture with methyl branching distributed along the octyl chain. This structural difference changes side-chain packing and free volume. Differential scanning calorimetry according to ASTM E1356 places the homopolymer glass transition temperature of poly(isooctyl acrylate) near −58 °C, whereas poly(2-ethylhexyl acrylate) is typically reported at −50 °C; published values shift with isomer composition and tacticity. The lower glass transition temperature reduces storage modulus at ambient temperature and improves low-temperature tack when used at equivalent mass fractions in acrylic copolymers. n-Butyl acrylate has a molecular weight of 128.17 g/mol and higher vapor pressure, which increases odor and evaporative loss during drying; its homopolymer glass transition temperature is commonly reported in the −45 °C to −54 °C range, making isooctyl acrylate more effective for low-temperature flexibility at equal copolymer loading.

    In solution copolymerization, the reactivity ratios of isooctyl acrylate with acrylic acid are solvent-dependent. Published data for 2-ethylhexyl acrylate and acrylic acid may be used as a rough approximation, but isooctyl acrylate-specific reactivity ratio data remains limited, especially in aqueous emulsion systems where monomer partitioning differs. Hydrophobic side-chain architecture reduces water uptake in cured films: long-term water immersion of isooctyl acrylate-rich copolymers generally produces lower equilibrium water absorption than n-butyl acrylate copolymers at equivalent acid content, although actual values depend on comonomer ratio and crosslink density. Aging under 85 °C and 85 % relative humidity for 1000 h per ASTM D2247 can be used to compare moisture resistance; published data for isooctyl acrylate formulations under these exact conditions is limited.

    Table 1. Comparative typical properties of isooctyl acrylate, 2-ethylhexyl acrylate, and n-butyl acrylate
    PropertyIsooctyl Acrylate2-Ethylhexyl Acrylaten-Butyl Acrylate
    CAS registry number29590-42-9103-11-7141-32-2
    Molecular weight184.28 g/mol184.28 g/mol128.17 g/mol
    Density at 20 °C0.878–0.884 g/cm³0.884–0.890 g/cm³0.894–0.898 g/cm³
    Boiling point200–215 °C213 °C145 °C
    Homopolymer glass transition temperature−58 °C typical−50 °C typical−45 to −54 °C

    Bulk procurement specifications for a high-purity stabilized grade are summarized in Table 2. These values are not maximum impurity ceilings for all applications; end uses involving ultraviolet curing, food-contact evaluation, or high-clarity films may require lower MEHQ content, lower peroxide value, or narrower isomer distribution. Low-acid grades are preferred when isooctyl acrylate is copolymerized with acid-sensitive monomers or used in cationic UV systems.

    Table 2. Bulk specification profile for a high-purity stabilized isooctyl acrylate grade
    PropertyTest methodTypical specification
    AppearanceVisual inspectionClear, colorless liquid
    GC purityASTM D3362≥ 99.0 %
    Water contentASTM E203≤ 0.05 wt%
    Acidity as acrylic acidASTM D1613≤ 0.01 wt%
    APHA colorASTM D1209≤ 10
    Density at 20 °CASTM D40520.878–0.884 g/cm³
    MEHQ inhibitorHPLC-UV at 280 nm15–20 ppm
    Boiling rangeASTM D1078200–215 °C

    When Isooctyl Acrylate Replaces 2-Ethylhexyl Acrylate in Ultraviolet-Cured Adhesive Coating

    In ultraviolet-curable pressure-sensitive adhesive formulations, isooctyl acrylate is incorporated as a monofunctional monomer to reduce coating viscosity, adjust glass transition temperature, and modify peel behavior. Because it contains no photocrosslinkable group, it must be combined with difunctional monomers such as 1,6-hexanediol diacrylate and an appropriate photoinitiator system. Lower MEHQ content is preferred: concentrations above 20 ppm can retard radical cure under low-intensity 365 nm LED lamps. A typical UV-cure pressure-sensitive adhesive processed on a 450 mm wide slot-die coater at line speeds of 30–80 m/min uses a coating weight of 15–50 g/m² and a UV-A dose of 200–600 mJ/cm². Cure completeness is assessed by gel fraction using Soxhlet extraction in ethyl acetate for 24 h; gel fractions below 50 % may indicate oxygen inhibition at the free surface if inerting is absent. Peel adhesion on stainless steel is measured by ASTM D3330/D3330M, and loop tack is measured by ASTM D6195. In comparative formulations, replacing 2-ethylhexyl acrylate with isooctyl acrylate typically lowers the plateau modulus and shifts the tan δ peak measured by dynamic mechanical analysis per ISO 6721-1:2019 to lower temperature by 3–8 °C, depending on comonomer ratio. This shift can improve low-temperature adhesion to low-energy substrates but may reduce high-temperature shear unless crosslink density is increased. Amine-modified acrylate oligomers should be avoided during storage because they can undergo Michael addition with isooctyl acrylate and increase formulation viscosity during aging.

    Emulsion polymerizations with isooctyl acrylate are typically run as semi-batch processes in jacketed stainless-steel reactors. A pre-emulsion of isooctyl acrylate, methyl methacrylate, and acrylic acid is fed over 3–4 h at 75–85 °C with ammonium persulfate initiator and an anionic/nonionic surfactant package. The ester group is more sensitive to hydrolysis than that of methyl methacrylate, so pH is maintained below 4.5 during polymerization and adjusted with ammonia or alkali after residual monomer reduction. Residual monomer is typically reduced to below 500 ppm of total volatiles using a redox chase with tert-butyl hydroperoxide and sodium metabisulfite at 60–65 °C. Final latex solids of 50–55 wt% and Brookfield viscosity of 200–1,500 mPa·s at 25 °C are common in pressure-sensitive adhesive production. The cast film glass transition temperature is measured by ASTM E1356 and is typically between −45 °C and −25 °C for isooctyl acrylate/methyl methacrylate/acrylic acid terpolymers containing 50–70 wt% isooctyl acrylate. In production, batch-to-batch variation in isooctyl acrylate isomer distribution can shift glass transition temperature by 2–3 °C; therefore, gas chromatographic integration of the isomer profile is recommended before large-scale campaign changes.

    Solution polymerization in ethyl acetate or toluene is used for solvent-borne adhesives and high-molecular-weight modifiers. Thermal initiation with 2,2′-azobisisobutyronitrile at 70–80 °C yields random copolymers with number-average molecular weights from 30,000 g/mol to 300,000 g/mol when measured by size-exclusion chromatography calibrated with polystyrene standards. Higher isooctyl acrylate content reduces chain stiffness and solution viscosity at equal solids; this permits solids loading up to 45–50 wt% in ethyl acetate while maintaining application viscosity below 20,000 mPa·s. The same hydrophobicity is exploited in pour point depressant and viscosity-index modifier intermediates, where isooctyl acrylate-rich copolymers are further functionalized to alter wax crystal growth in lubricant basestocks. Published performance data for specific base oil formulations is limited, and bench-scale pour point testing by ASTM D97 is required to confirm treat-rate effects.

    Storage of isooctyl acrylate requires dissolved oxygen for the monomethyl ether hydroquinone inhibitor to function. Long-term storage under nitrogen can deplete oxygen and allow uninhibited radical initiation at temperatures above 35 °C. Bulk storage tanks should be fabricated from stainless steel or aluminum; carbon steel is not recommended because iron can catalyze acrylate polymerization. Recommended storage temperature is 10–30 °C with headspace oxygen concentration maintained at 5–21 vol% using dry air, not pure oxygen, to avoid flammability concerns. The ester is sensitive to hydrolysis under strong alkaline conditions, so it should not be combined with high-pH buffering agents without prior evaluation. Contact with amines and strong oxidizing agents should be avoided. In moisture-sensitive applications, fillers and other raw materials should be pre-dried at 80–100 °C when ambient relative humidity exceeds 60 %; otherwise, water introduced with fillers can reduce molecular weight or interfere with moisture-sensitive photoinitiator systems.

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