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Эпоксидная смола

    • Название продукта: Эпоксидная смола
    • Сайт Factroy: Округ Юду, Ганьчжоу, Цзянси, Китай
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    • Производитель: Ascent Petrochem Holdings Co., Limited
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    Спецификации
    Код ТН ВЭД
    Название продукта Эпоксидная смола
    Химическая классификация Термоутвердительный полимер, образованный реакцией эпоксидной смолы и затвердительного агента
    внешность Прозрачная до янтарной жидкости или твердой
    плотность 1,1 до 1,3 г/см3
    вязкость 500 до 20 000 мПа·с в зависимости от состава
    Соотношение смеси Обычно 1:1, 2:1 или 3:1 по объему или весу
    Жизнеспособность 5-60 минут при 25°C в зависимости от состава
    Излечить время 24-72 часа при комнатной температуре, быстрее при тепле
    Предел прочности 30 до 80 МПа
    Сжательная прочность 60 до 120 МПа
    Прочность на изгиб 80 до 150 МПа
    Удлинение при разрыве От 1% до 6%
    температура стеклования 50-150°C в зависимости от состава
    Водопоглощение 0,1% до 0,5% после 24 часов
    химическая стойкость Устойчивость к воде, кислотам, щелочам и растворителям в зависимости от состава
    Электрическая прочность диэлектрика 15-20 кВ/мм
    Усадка 0,5% до 3% во время лечения
    Срок годности 12-24 месяца при хранении в запечатанных контейнерах
    Классификация опасности раздражающий; может вызвать чувствительность кожи
    Содержание ЛОС Низкий до ничего для составов без растворителей

    Как аккредитованный завод по производству эпоксидной смолы, мы соблюдаем строгие протоколы качества - каждая партия подвергается строгим испытаниям для обеспечения последовательных стандартов эффективности и безопасности.

    Упаковка и хранение
    Упаковка Эпоксидная смола упакована в 20 кг запечатанных металлических ведрах, четко помечены и хранятся вертикально в прохладном, сухом, вентилируемом пространстве.
    Погрузка контейнера (20-футовый контейнер) Эпоксидная смола паллетизируется, загружается в 20-футовый контейнер FCL, равномерно распределяется, закрепляется и запечатается для безопасной морской перевозки.
    Доставка Эпоксидная смола обычно доставляется в герметических стальных барабанах, ведрах или IBC при температуре окружающей среды. В зависимости от состава, он может быть неопасным или регулируется как воспламеняемый, коррозионный или опасный для окружающей среды. Используйте упаковку, утвержденную ООН, правильные этикетки, SDS и соблюдайте правила IMDG/IATA/ADR. Хранить прохладным, сухим, вертикальным, подальше от источников зажигания.
    Хранение Храните эпоксидную смолу в прохладном, сухом, хорошо вентилируемом месте, подальше от прямого солнечного света, тепла, искр и источников зажигания. Держите контейнеры плотно закрытыми, вертикальными, маркированными и во вторичном контейнере. защищать от влаги и замораживания; поддерживать умеренные температуры. Хранить отдельно от твердителей, кислот, оснований и окислителей. Следуйте SDS и местным правилам. Используйте паллеты для разлива и заземленное оборудование, когда это необходимо. Держит
    Срок годности Срок хранения эпоксидной смолы обычно составляет 12-24 месяца, когда хранится в прохладном, сухом месте, подальше от влаги, тепла и солнечного света.
    Применение эпоксидной смолы

    Why Amine-Cured Marine Primers Demand Induction-Time Verification Before Airless Spraying?

    For high-solids anticorrosive primers specified to ISO 12944-5:2019 categories C5M and CX, bisphenol A diglycidyl ether with an epoxide equivalent weight of 185-192 g/eq and viscosity of 12,000-16,000 mPa·s at 25°C per ASTM D445 is combined at 32-38 wt% of Part A with a polyamide-cycloaliphatic amine Part B dosed to an epoxy-to-amine-hydrogen ratio of 0.95-1.05. Zinc phosphate or aluminium triphosphate is added at 8-12 wt% and iron oxide red at 5-10 wt%; a polyamide thixotrope at 1.5-2.0 wt% and a silicone-free defoamer at 0.2-0.5 wt% complete the letdown. After Part A and Part B are mixed, the batch is dispersed in a high-speed disperser with a Cowles blade tip speed of 18-23 m/s and held at 35-45°C until a Hegman grind of 6 is recorded; the catalysed material then undergoes an induction time of 15-30 min at 23°C before spray. Application proceeds via airless spray at 17-22 MPa with a 0.019-0.025 in reversible tungsten carbide tip, producing a single-coat dry film thickness of 250-400 µm. Steel is abrasive blasted to ISO 8501-1 Sa 2.5 with a surface profile of 40-80 µm Rz per ISO 8503-1:2012, and stripe coating is applied to edges and welds before full coverage. The overcoat window is limited to 6-24 h at 23°C and 50% RH; amine blush above 80% RH must be removed by water washing before recoating. Salt spray resistance is rated 8 after 5,000 h under ASTM D1654-08(2019), and ballast tank systems satisfy IMO PSPC MSC.215(82) with a minimum two-coat dry film thickness of 320 µm. Terminal product types include ship ballast tank linings, offshore splash-zone maintenance systems, tank internals for light hydrocarbons, and steel bridge primers in CX corrosivity sites.

    Test parameterMethodRequired value
    Overcoat window at 23°CISO 9117-5:20126-24 h
    Salt spray rating after 5,000 hASTM D1654-08(2019)≥ 8
    Pull-off adhesionISO 4624:2016≥ 5 MPa
    Blast surface profileISO 8503-1:201240-80 µm Rz

    Vacuum Infusion Viscosity, Fiber Wetting, and Exotherm Containment in Rotor Blade Spar Caps

    Liquid epoxy resin with a mixed viscosity of 250-600 mPa·s at 25°C per ASTM D2196 is combined with a cycloaliphatic amine hardener at a 100:31 weight ratio, corresponding to an epoxy-to-amine-hydrogen ratio of 0.95-1.05, and an internal mold release agent at 0.8-1.5 wt% of resin mass. The resin component accounts for 30-38 wt% of the final glass-reinforced laminate, with a target fiber volume fraction of 55-60% in unidirectional spar cap regions. Fiber preforms are dried at 60°C for 8 h when relative humidity exceeds 60% during layup; incomplete drying raises mixed resin viscosity and creates microvoids during the 80°C cure plateau. Vacuum-assisted resin transfer molding is used, with preform evacuation at -95 to -99 kPa for 30 min, followed by resin injection at 22-27°C; pot life is defined as the time for viscosity to rise to 800 mPa·s at 25°C and is maintained between 90-120 min. Curing is staged at 70°C for 6 h then 80°C for 8 h, with mold heating rate limited to 0.5°C/min to contain exotherm. In laminates thicker than 25 mm or mixed masses above 50 kg, published data for this specific configuration is limited; the system may exhibit an exothermic peak of 35°C above ambient, reducing glass transition temperature from 85°C to below 70°C. Compliance for the cured laminate is established under IEC 61400-5:2020, DNV-ST-0376:2015 for rotor blade design, and ISO 527-5:2021 for tensile properties. Terminal product types include spar cap laminates, root-section reinforcements, shear webs, and blade outer shell layups.

    When Capillary Underfill Replaces Dispensing Paste in Flip-Chip Ball Grid Array Assembly

    In flip-chip ball grid array assembly, low-hydrolysable-chlorine bisphenol A epoxy resin with saponifiable chlorine below 300 ppm per ASTM D1726 is formulated at 18-28 wt% with spherized amorphous silica filler at 65-75 wt%, epoxy silane coupling agent at 0.3-1.0 wt%, boron nitride at 5-10 wt%, and an imidazole catalyst at 2-5 phr. Vacuum planetary mixing at -0.095 MPa for 30 min removes moisture and preserves filler surface treatment; the resulting one-component paste shows a viscosity of 300-1,000 mPa·s at 25°C per ASTM D2196. At die temperatures of 70-90°C, capillary flow fills gaps of 25-75 µm before cure at 150°C for 1 h and 175°C for 2 h. Post-cure volume shrinkage is below 0.3% by ISO 1183-1:2019, and coefficient of thermal expansion below glass transition is 25-35 ppm/°C by IPC-TM-650 2.4.24. Compliance standards include IPC-CC-830C for conformal coating materials, UL 94 V-0 at 3.2 mm, and IEC 61249-2-21:2005 for halogen-free base materials; power module encapsulation is tested by MIL-STD-883 Method 5011 for die shear and JEDEC JESD22-A104 for thermal cycling. Any addition of primary amine hardener to the one-component underfill initiates premature crosslinking at ambient and is incompatible with syringe storage. Terminal product types include capillary underfill for flip-chip BGA packages, chip-on-board glob-top encapsulants, IGBT power module potting compounds, and capacitor encapsulants in automotive inverter circuits.

    Structural Adhesive Bonding in Automotive Body-in-White and Battery Enclosure Assembly

    Robotic dispensing of one-part epoxy structural adhesive onto zinc-nickel coated steel hem flanges in a body-in-white cycle of 38 s exposes uncured paste to ambient temperatures up to 35°C and 75% RH before the electrocoat oven cure. The formulation contains bisphenol A epoxy resin at 35-55 wt%, carboxy-terminated butadiene acrylonitrile toughener at 8-15 wt%, dicyandiamide hardener at 4-8 phr, substituted urea accelerator at 1-3 phr, calcium carbonate filler at 10-20 wt%, and an epoxy silane adhesion promoter at 1-2 wt%. Batch-to-batch variation in carboxy-terminated butadiene acrylonitrile toughener acrylonitrile content is held within ±1.5 wt% by a Fourier-transform infrared method aligned with ASTM D3677-10(2020). The paste is stored at -40°C and dispensed from 50 mL cartridges at 25-40°C in beads of 0.8-1.2 mm diameter. Cure occurs in the electrocoat oven at 160-180°C for 20 min; off-line repair may use induction heating at 180°C for 10-15 min on aluminium substrates. Performance is assessed by lap shear strength exceeding 20 MPa on 25 mm overlap per ASTM D1002-10, T-peel strength exceeding 6 N/mm per ISO 11339:2010, and DIN EN 1465:2009 for rigid-to-rigid bonded assemblies. Volatile organic compound and fogging behaviour are tested under VDA 278:2011; wash-off resistance before electrocoat is evaluated by a mechanical water spray test at line speed 1.5-2.0 m/min and 35°C water temperature. Terminal product types include hem flange bond lines in doors and hoods, structural bonding of roof bows, battery enclosure frame bonding in battery electric vehicles, and mixed-metal joining of aluminium to galvanized steel.

    100% Solids Self-Leveling Epoxy Flooring in Cleanroom and Pharmaceutical Facilities

    A clear bisphenol A epoxy resin component is combined with an aliphatic amine hardener at a 100:50 weight ratio, and quartz sand is added at 0.5-1.5 parts by weight per 100 parts resin when slip resistance must meet DIN 51130 class R11. Barium sulfate is incorporated at 20-40 wt% for solids loading, with a polyether-modified siloxane defoamer at 0.3-0.5 wt% to limit pinholes in 3-5 mm self-leveling films. The mixed system has a viscosity of 700-1,100 mPa·s at 23°C per ASTM D2196, providing a working time of 40-50 min for a 100 kg batch before a gel time of 2 h per ISO 9514:2019. The concrete substrate is evaluated for moisture vapor emission rate below 3 lb/1,000 ft²/24 h by ASTM F1869-22 and relative humidity below 4% CM by ASTM F2170-20, then abrasive blasted to CSP 3 profile per ASTM F710-22. A primer coat is applied at 150-250 g/m²; the self-leveling body coat is installed at 2-4 mm thickness with a pin-laminated or contractor roller and spike roller to release entrapped air. Cure before chemical exposure is 7 days at 23°C and 50% RH. Compliance standards include EN 13813:2019 for synthetic resin screed materials, ISO 13007-3:2017 for resin flooring, and EN 1504-2:2004 for surface protection systems. Amine blush can form below 10°C or above 85% RH; exposure to glacial acetic acid or concentrated hydrochloric acid is not recommended. Terminal product types include pharmaceutical cleanroom floors, hospital operating theatre floors, beverage plant wet-process floors, and aircraft hangar maintenance floors.

    Fusion-Bonded Epoxy Pipeline Powders: Differential Scanning Calorimetry Cure Parameters and Cathodic Disbondment Resistance

    After twin-screw compounding at an L/D ratio of 32:1 and barrel temperatures of 90-120°C, powder-grade solid bisphenol A epoxy resin with a softening point of 90-105°C per ASTM D6090 is compounded at 55-68 wt% with dicyandiamide hardener at 3-4 wt%, phenolic accelerator at 1-2 wt%, calcium silicate filler at 15-25 wt%, iron oxide pigment at 1-3 wt%, and fumed silica flow control agent at 0.3-0.8 wt%. Cooled flake is milled to a particle size distribution with D50 35-65 µm per ISO 13320-1:2020; batch-to-batch variance in fluidized-bed pickup is controlled by particle size distribution and powder moisture below 0.3 wt%. Gel time at 180°C is 60-90 s per ISO 8130-6:2021. Electrostatic spray deposition at 60-80 kV is applied to pipe preheated to 230-240°C after blast cleaning to ISO 8501-1 Sa 2.5, and the film cures at 180-200°C for 3-6 min to achieve a dry film thickness of 350-500 µm. Compliance is established under ISO 21809-2:2015 for external fusion-bonded epoxy coatings, NACE SP0394-2013 for factory-applied fusion-bonded epoxy, CSA Z245.20-22 for plant-applied external pipe coatings, and ASTM G14-04(2019) for impact resistance. Cure completeness by differential scanning calorimetry per ISO 11357-5:2014 must show a residual exotherm below 5 J/g and a glass transition temperature above 110°C. Cathodic disbondment is tested at 23°C for 28 days with an applied potential of -1.5 V versus a saturated calomel electrode, requiring radial disbondment below 6 mm. Powder moisture content above 0.3 wt% causes pinholing during spray; substrate temperature below 215°C yields undercured films with crosslink density insufficient to maintain adhesion under the applied cathodic potential. Terminal product types include onshore gas pipeline external coatings, offshore riser coatings, reinforcing bar coatings, and ductile iron pipe linings.

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    Сертификация и соответствие требованиям
    Более подробное введение

    Epoxy resin supplied as a liquid diglycidyl ether of bisphenol A (DGEBA) with an epoxide equivalent weight of 182–192 g/eq functions as a base resin in amine-, anhydride-, and homopolymerized thermoset systems. Model EP-4101 is used here to designate a commercial liquid DGEBA grade corresponding to CAS 25068-38-6 and verified against ASTM D1652, ASTM D2196, ASTM D1475, ASTM D1726, and ASTM D1544. Typical batch data report a viscosity of 11 000–14 000 mPa·s at 25 °C, a density of 1.16 g/cm³, and a hydrolysable chloride content of ≤ 5 ppm in the low-chloride variant. The resin complies with the compositional limits of DIN 16945 and ASTM D1763-00. Storage below 5 °C can induce crystallisation, which is reversible at 50–60 °C for 2 h; prolonged exposure above 35 °C raises viscosity and reduces epoxide equivalent weight stability through trace-alkali-initiated homopolymerization.

    The product differs from phenolic and furan resins by addition polymerization rather than condensation. No water, formaldehyde, or low-molecular-weight alcohol is released during network formation, which permits low-void castings and closed-mold laminates. The absence of a condensation byproduct also means the mixed mass does not self-dry; wet substrates above 0.5% surface moisture can produce interlayer adhesion failure under ASTM D4541. The resin is incompatible with strong Lewis acid accelerators in bulk storage because cationic homopolymerization can initiate at ambient temperature and raise viscosity beyond 50 000 mPa·s within 24 h.

    What Limits Pot Life in Ambient-Cure Amine Systems?

    The kinetic boundary for a liquid DGEBA resin and a polyamine hardener is controlled by amine hydrogen equivalent weight, cast mass, and initial mix temperature rather than resin viscosity alone. For a standard EEW of 190 g/eq, a fast aliphatic amine with an amine hydrogen equivalent weight of 24 g/eq requires 12.6 phr, while an amidoamine with AHEW 120 g/eq requires 63 phr. A stoichiometric deviation of ±5% on the hardener side is sufficient to change the apparent glass-transition temperature by 8–12 °C when measured by dynamic mechanical analysis according to ASTM E1640. Under-dosing leaves unreacted oxirane, lowering adhesive shear at 85 °C; overdosing produces free amine that can exude to the bond line as a waxy surface layer.

    Pot life is best treated as a thermal runaway threshold, not a single viscosity endpoint. For a 150 g mass at 23 °C, a fast aliphatic amine system commonly gels within 28–35 min and reaches a peak exotherm of 140–160 °C when tested per ASTM D2471. A polyamide adduct with AHEW 100–110 g/eq extends gelation to 65–90 min under the same conditions but may sag on vertical metal at wet-film thickness above 150 µm. On production-scale meter-mix-dispense machines with static mixers, purging intervals should be no longer than one-third of the stated pot life; field observations on automotive hem-flange dispensing lines record viscosity stratification and gel-particle release after interruptions of 12 min or more. At relative humidity above 60%, hygroscopic amine hardeners absorb water and may develop amine blush; carbon steel substrates and fumed silica fillers require vacuum drying at 80 °C for 2 h before bonding.

    Room-temperature adhesive bonding of aluminum adherends requires phosphoric-acid anodizing or chromic-acid etching to prevent interfacial hydration, not merely solvent degreasing. In a two-component DGEBA/amine adhesive with a mixed viscosity of 4000–8000 mPa·s at 25 °C, lap-shear strength on 2024-T3 aluminum after 7 days at 23 °C is reported under ASTM D1002 as 18–24 MPa. Chromic-acid-anodized surfaces retain the highest cohesive failure ratio; solvent-wiped surfaces can fail adhesively below 6 MPa. Single-part epoxy paste adhesives cured at 120 °C for 60 min eliminate mix-ratio variability but require freezer storage below −18 °C and have a post-thaw work life of 4–8 h.

    In solvent-free epoxy coating formulations, post-mix induction time controls air release, blush, and surface defect density more than final viscosity does. After A-side and B-side are mixed, a quiescent induction period of 15–20 min at 23 °C is typically required for a polyamide-cured DGEBA coating to allow bubbles generated during high-shear dispersion to escape. Mixed viscosity at 25 °C should be held between 600 mPa·s and 1200 mPa·s for airless spray application when measured by ASTM D2196; above this band, the wet film retains solvent or air, and below it, the coating sags on vertical surfaces beyond the limits of ASTM D4400-22. On production airless spray lines with 45:1 ratio pumps and 0.015–0.021 inch reversible tips, pot life is consumed faster because shear heating raises the material temperature by 5–10 °C; this reduces the usable spray window by 20–30% compared with static pot-life data. Batch-to-batch variation in hydrolysable chloride above 5 ppm may promote carbamation with polyamide hardeners and increase amine blush under high humidity; the issue is controlled by specifying the low-chloride grade.

    Table 1. Typical specification limits for a commercial liquid DGEBA resin
    PropertyMethodSpecification
    Epoxide equivalent weightASTM D1652182–192 g/eq
    Viscosity at 25 °CASTM D219611 000–14 000 mPa·s
    Density at 25 °CASTM D14751.16 g/cm³
    Hydrolysable chlorideASTM D1726≤ 5 ppm low-chloride grade
    Color, GardnerASTM D1544≤ 1
    Water contentASTM E203≤ 0.05 wt%

    For electrical encapsulation, the selection of bisphenol A or cycloaliphatic resin is driven by thermal endurance and ionic cleanliness rather than initial viscosity. A cycloaliphatic epoxy/anhydride system processed at 60–80 °C under vacuum typically maintains a mixed viscosity below 300 mPa·s at 70 °C; this permits bubble-free encapsulation of IGBT modules in vacuum potting equipment chambers at 5 mbar. After curing at 120 °C for 4 h and 150 °C for 4 h, the network exhibits a glass-transition temperature of 140–155 °C by differential scanning calorimetry per ISO 11357-2. The coefficient of linear thermal expansion below glass transition is 60–70 ppm/K for unfilled resin per ISO 11359-2; adding 60–65 wt% spherical fused silica lowers CTE to 25–30 ppm/K but raises mixed viscosity to 20 000–40 000 mPa·s at 25 °C. Ionic extractables are controlled to below 0.1 mg/kg sodium chloride equivalent when tested per IPC-TM-650 2.3.25. Anhydride-cured systems are incompatible with hydroxyl-bearing reactive diluents above 5 phr because esterification competes with anhydride ring opening and leaves an uncured fraction; this is detected as reduced dielectric strength under IEC 60243-1.

    When Epoxy Is Compared With Vinyl Ester, Polyurethane, and Silicone for Acid Immersion Service

    In acid immersion linings, bisphenol A epoxies and novolac epoxies are differentiated from vinyl ester, polyurethane, and silicone by their crosslink-density response and bond strength to prepared steel. Vinyl ester resins, cured through methacrylate double bonds, deliver lower viscosity at equal solids and faster room-temperature cure, but their volumetric cure shrinkage reaches 7–10% based on density change under ASTM D792; a filled DGEBA/amine lining typically shrinks 0.5–1.5% during cure, reducing stress cracks at expansion joints. Polyurethane linings provide elongation at break of 200–400% under ASTM D638 but soften above continuous service temperatures of 80 °C in acid-containing hydrocarbon streams. Silicone coatings maintain thermal stability to 250 °C but exhibit lower pull-off adhesion on Sa 2½ blast-cleaned steel; epoxy systems generally exceed 12 MPa under ISO 4624, while silicone systems are often below 2 MPa. Novolac epoxy grades raise the crosslink density of the DGEBA network and are preferred when sulfuric acid at 20–40% concentration and temperatures up to 90 °C require service life beyond 5000 h; published data for the specific DGEBA/novolac concentration gradient is limited, so immersion coupon testing is required.

    Table 2. Comparative property ranges for resin classes used in chemical resistant linings
    PropertyStandardDGEBA/amineVinyl esterPolyurethaneSilicone
    Tensile strengthASTM D63850–75 MPa60–85 MPa20–40 MPa4–8 MPa
    Elongation at breakASTM D6382–6%3–6%200–400%100–400%
    Pull-off adhesion on Sa 2½ steelISO 4624> 12 MPa> 10 MPa> 6 MPa> 2 MPa
    Volumetric cure shrinkageASTM D7920.5–1.5%7–10%2–4%0.5–1.5%

    In vacuum-infused carbon fiber laminates, a low-viscosity infusion epoxy with an EEW of 160–180 g/eq and mixed viscosity below 250 mPa·s at 25 °C is required to wet resin distribution medium and compacted carbon fabric without dry-spot formation. Vacuum bag processing at −0.95 bar vacuum and mold temperature 35–45 °C requires a pot life of 120–180 min; this is achieved with an anhydride or latent aliphatic amine system rather than a fast ambient amine. The laminate is demolded after 8 h at 60 °C and post-cured at 120 °C for 4 h; the resulting glass-transition temperature is measured by ASTM E1640 and must exceed the operating temperature by at least 25 °C. Fiber volume fraction is controlled at 55–60% by ultrasonic thickness verification after infusion. In this application, the epoxy resin differs from infusion-grade vinyl ester by its lower cure shrinkage and better retention of interlaminar shear strength above 70 °C; the trade-off is longer degassing time and more sensitivity to moisture in carbon fabric at relative humidity above 60%, which requires pre-drying at 80 °C for 4 h before layup.

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