Alchemist Worldwide Ltd

Products

Bluesail Dioctyl Adipate (DOA)

    • Product Name: Bluesail Dioctyl Adipate (DOA)
    • Factroy Site: Jiangjun Avenue 55#, Jiangning Area, Nanjing, China
    • Price Inquiry: sales7@alchemist-chem.com
    • Manufacturer: Alchemist Worldwide Ltd
    • CONTACT NOW
    Specifications
    HS Code 930982
    Appearance Colorless transparent oily liquid
    Purity ≥99.5%
    Molecular Formula C22H42O4
    Molecular Weight 370.57 g/mol
    Cas Number 103-23-1
    Einecs Number 203-090-1
    Density 0.925-0.930 g/cm³ at 20°C
    Boiling Point 417°C
    Melting Point -67°C
    Flash Point 206°C
    Refractive Index 1.4470-1.4490 at 20°C
    Viscosity 13-15 mPa·s at 20°C
    Acid Value ≤0.1 mg KOH/g
    Water Content ≤0.1%
    Color ≤30 APHA
    Volatile Matter ≤0.1%
    Solubility Insoluble in water, soluble in most organic solvents
    Ester Content ≥99.5%

    As an accredited Bluesail Dioctyl Adipate (DOA) factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing
    Shipping
    Storage
    Application of Bluesail Dioctyl Adipate (DOA)

    Low-Temperature PVC Insulation and Sheathing Compounds

    In low-temperature PVC wire and cable compounding, Bluesail dioctyl adipate is charged at 12–25 phr per 100 phr suspension PVC resin where product standards specify installation flexural integrity below −25 °C. The plasticizer is introduced during dry-blend preparation and then brought into a co-rotating twin-screw compounding extruder with L/D 32:1. Barrel temperatures are controlled from 145 °C at the feed zone to 170 °C at the metering section, while melt temperature at the die plate is held at 165–180 °C. Strand pelletizing feeds a subsequent single-screw extrusion line equipped with a crosshead die and draw-down ratio of 1.05–1.15:1; insulation wall thickness is maintained between 0.25 mm and 1.20 mm. Batch-to-batch variation in DOA acidity below 0.05 mg KOH/g and hydroxyl value below 0.15 mg KOH/g is correlated with stable insulation shrinkage after 24 h at 80 °C.

    Compliance for automotive and appliance cable types is anchored to ISO 6722-1:2011 for low-tension automotive conductors, IEC 60811-504:2012 for low-temperature elongation testing, and UL 1581 for appliance wiring material evaluations. REACH registration is maintained under REACH Regulation (EC) No 1907/2006, and EU market entries require RoHS Directive 2011/65/EU documentation. Because dioctyl adipate is an adipate ester rather than an ortho-phthalate, it does not fall under the restricted phthalate entries in RoHS Directive (EU) 2015/863 unless regulated impurities are present above threshold concentrations. Aging tests are performed at 100 °C for 7 days with tensile and elongation retention recorded; DOA-plasticized PVC compounds intended for continuous service above 90 °C require formulation redesign with trimellitate or polymeric plasticizers to prevent accelerated volatilization and hardness increase exceeding 3 points within 1 000 h when tested under ISO 188. Published long-term aging data for DOA-specific formulations above 105 °C is limited.

    The single-screw extrusion line operates with a barrier screw, a screen pack of 80/120/80 mesh, and water trough temperatures of 15–25 °C. Finished terminals include automotive engine-compartment hook-up wire, cold-climate appliance internal wiring, portable cord sheathing, and cable filler compounds that require retained flexibility during installation at sub-zero ambient temperatures.

    Nitrocellulose lacquer and gravure ink production incorporates dioctyl adipate at 20–40 phr on dry nitrocellulose solids to interrupt interchain hydrogen bonding and reduce film cracking after solvent evaporation. The DOA charge is introduced during letdown following high-shear dispersion of nitrocellulose in an ester/ketone solvent blend. Press viscosity is commonly targeted at 25–40 s in a Zahn Cup No. 2, and DOA additions within the stated range lower flow time by 8–15 s relative to an unplasticized nitrocellulose base of equal solids content. Viscosity verification uses a Brookfield viscometer at 12 rpm with spindle 4. The downstream coating process uses a high-speed dissolver with a Cowles blade at tip speeds of 8–12 m/s, followed by a horizontal bead mill loaded with 0.6–0.8 mm zirconia beads for 15–25 min residence. Letdown mixing is performed at 3–5 m/s tip speed to limit shear-induced nitrocellulose degradation. Gravure application uses a cylinder screen of 60–100 lines/cm, with drying tunnel temperatures held at 60–80 °C and air velocity at 2–4 m/s.

    Compliance for toy coatings and printed surfaces is assessed under EN 71-3:2019+A1:2021 for migration of specific elements. Printed food-contact packaging is evaluated under EU Regulation (EC) No 1935/2004 and Commission Regulation (EU) No 10/2011 only when the printed layer can migrate into food; otherwise a functional barrier or separate compliance demonstration is required. Solvent emissions from industrial coating lines follow local implementation of Directive 2010/75/EU. Finished article types include wood lacquers, industrial maintenance coatings, flexographic surface-printing inks for polyolefin film, and leather finishing base coats. DOA is not selected for nitrocellulose coatings exposed continuously above 120 °C because the ester re-softens the dried film and reduces König hardness values measured under ASTM D4366.

    What Limits Plastisol Pot-Life Stability When DOA Replaces Phthalate Plasticizers in Dip Molding?

    Replacement of DINP or DIDP with dioctyl adipate in PVC plastisol alters solvation kinetics because DOA contributes lower solvation power and lower viscosity per unit mass at equal phr. In dip-molding formulations, DOA loading ranges from 30–70 phr per 100 phr paste PVC resin, with 50–60 phr used for articles requiring simultaneous low-temperature flex and sufficient gel strength. Initial Brookfield viscosity is measured at 20 rpm with spindle 6 after 2 h maturation at 23 °C; replacing an equal phr of DIDP with DOA can lower viscosity by 300–600 mPa·s. Viscosity stability is monitored per ISO 2555:2018. Formulations above 70 phr DOA may exhibit phase separation and exudation after 7 days at 40 °C; published data for long-term pot-life stability beyond this loading is limited and must be confirmed on production batches.

    Mixing uses a high-shear dissolver with a Cowles blade at 15–20 m/s tip speed under vacuum of −0.095 MPa to remove entrapped air. The plastisol is matured at 23 ± 2 °C for 2–24 h before dip molding. Production mandrels are preheated to 40–60 °C, immersion speed is set at 0.5–1.5 m/min, and withdrawal speed at 0.2–0.8 m/min controls coating thickness between 0.8 mm and 3.0 mm. Gelation and fusion take place in a forced-air tunnel at 180–200 °C for 4–8 min. The process window is critical at ±10 °C: below 170 °C, tensile strength and tear resistance decline when measured per ASTM D638 and ASTM D624; above 210 °C, thermo-oxidative yellowing accelerates and can produce delta E values greater than 2 within 30 min.

    Compliance for child-contact dip-molded articles requires migration testing under EN 71-3:2019+A1:2021. Phthalate restrictions under REACH Regulation (EC) No 1907/2006 Annex XVII do not apply to DOA itself, although impurity-related restrictions remain. Industrial bellows and connector covers destined for the EU carry RoHS Directive 2011/65/EU declarations. Food-contact plastisol applications are not assumed; published data for DOA in food-contact plastisol seals under FDA 21 CFR 177.2600 is limited and must be verified for each article type. Terminal products include anti-slip dip-molded tool handles, protective bellows for outdoor hydraulic actuators, flexible electrical connector covers used in refrigeration equipment, and grips for sports and garden implements requiring cold-weather impact resistance. The plastisol route is not selected when pumping circulation exceeds 48 h because viscosity rise from progressive resin solvation may exceed 20% and disrupt coating thickness control.

    When Calendered PVC Film and Coated Fabric Lines Demand Sub-Zero Flexibility

    Calender operations producing wide-format tarpaulin and cold-store strip door stocks meter DOA at 20–50 phr into a high-intensity hot mixer before transferring the dry blend to a Banbury internal mixer. The Banbury is filled to 70–80% capacity and dumped at 150–165 °C. The two-roll mill then feeds an L-type calender with roll temperatures maintained at 160–185 °C across top, middle, bottom, and offset rolls. Nip gaps are set between 0.4 mm and 1.2 mm to produce film gauge from 0.20 mm to 0.80 mm, with take-off speed ranging from 15–40 m/min. DOA reduces melt viscosity at the calender nip, but loadings above 50 phr increase plate-out tendency and reduce hot strength, requiring peel tension below 1.5 N/25 mm during embossing and wind-up.

    Cold-crack resistance is evaluated under ASTM D1790; films containing DOA at 35 phr typically show no cracking at −35 °C, although results are resin-molecular-weight and heat-stabilizer dependent. Tensile properties are measured per ASTM D638 or ISO 527-3, and accelerated weathering uses ISO 4892-2 cycles for outdoor textiles. EU product compliance relies on REACH Regulation (EC) No 1907/2006 and RoHS Directive 2011/65/EU. For toy-related flexible sheeting, EN 71-3:2019+A1:2021 applies to element migration. DOA’s relatively low molecular mass introduces a fogging limitation for automotive interior skins; where DIN 75201 gravimetric fogging must remain below 2 mg, DOA-only plasticizer systems are usually replaced by trimellitate or low-fog adipate/polymeric blends. Published data for DOA in automotive in-cabin PVC sheeting under SAE J1756 is limited and indicates volatile condensate increases as plasticizer loading increases.

    Finished stock types include truck tarpaulins, cold-store strip doors, tent and marquee panels, and coated industrial fabrics for double-sided banners. The calender route is preferred when gauge uniformity below ±0.05 mm is specified and when the final article must survive installation flexing at temperatures below −20 °C.

    Compliance matrix for DOA downstream segment qualification
    SegmentStandard codeCritical test method or conditionTypical control point
    Low-temperature PVC cableIEC 60811-504:2012Low-temperature elongation−25 °C conditioning
    Nitrocellulose lacquer and inkEN 71-3:2019+A1:2021Migration of specific elementsArticle-specific limit
    Plastisol dip moldingISO 2555:2018Brookfield viscosity stability23 ± 2 °C maturation
    Calendered PVC filmASTM D1790Cold-crack temperature−35 °C at 35 phr
    Solvent-borne adhesiveFDA 21 CFR 175.105Extractive and barrier verificationFunctional barrier required
    Nitrile and neoprene rubberASTM D1053Gehman torsional stiffnessT10 below −30 °C

    Solvent-borne vinyl and acrylic adhesive systems incorporate dioctyl adipate at 5–15 wt% of total formulation to lower application viscosity and preserve bond flexibility on plasticized vinyl substrates. The plasticizer is added in a sigma-blade mixer after resin dissolution in a methyl ethyl ketone/toluene or ethyl acetate/toluene blend. Mixing continues for 20–35 min at 20–40 rpm until a homogeneous clear phase forms. Viscosity is measured with a Brookfield viscometer at 20 rpm using spindle 7, with target values between 4 000–12 000 mPa·s depending on coating method. Knife-over-roll application uses a gap of 0.2–0.5 mm and line speeds of 5–15 m/min, followed by forced-air drying at 50–70 °C.

    Packaging adhesives containing dioctyl adipate are evaluated under FDA 21 CFR 175.105 as an adhesive component, provided the adhesive is separated from food by a functional barrier or otherwise meets extractive limitations. The adhesive layer is not approved as a direct food-contact layer under this citation, and migration testing under Commission Regulation (EU) No 10/2011 is required when the bonded structure is placed on the EU market without a barrier. Construction sealant formulations are specified under ASTM C920 only when the total formulation meets joint movement and adhesion requirements; DOA is one co-plasticizer within such systems and is not a sole determinant of sealant rating. Terminal products include vinyl floor adhesives, automotive interior lamination adhesives, cold-weather construction sealants, and pressure-sensitive adhesive bases requiring a low-temperature tack window. DOA is not selected for structural metal bonding because plasticizer migration into rigid PVC or ABS substrates can soften the adherend and reduce lap shear values measured per ASTM D1002 after 7 days at 60 °C.

    Lowering Gehman Torsional Stiffness in Nitrile and Neoprene Compounds with DOA

    At the second-pass mixing stage of nitrile and neoprene compounding, dioctyl adipate is dosed at 5–20 phr to lower glass-transition-associated stiffening without excessive cure-rate suppression. The ester is added after carbon black and processing oil have developed shear heat; dump temperatures are held at 105–125 °C to avoid thermal decomposition of DOA and to prevent scorch in sulfur-cured recipes. Mixing uses an internal mixer with a fill factor of 0.75 and rotor speed of 30–50 rpm for 70–110 s following plasticizer injection. The batch is sheeted on an open two-roll mill at 50–60 °C before compression molding at 160–170 °C and 12–15 MPa for 6–12 min, depending on the cure system.

    Low-temperature flexibility is measured by Gehman torsional stiffness per ASTM D1053, with acceptance frequently set at T10 below −30 °C and T100 below −45 °C for cold-service seals. Hardness is measured per ASTM D2240, and tensile/elongation properties are evaluated per ASTM D412. Oil-aging behavior is tested in IRM 901 and IRM 903 oils per ASTM D471; DOA-plasticized nitrile compounds show larger volume swell than trimellitate-plasticized controls. For rubber articles intended for repeated food contact, FDA 21 CFR 177.2600 may apply, but specific end-use extractive limits must be verified because DOA migration increases with temperature and oil contact.

    Typical terminal products are cold-climate automotive fuel hose covers, refrigeration compressor gaskets, low-temperature O-rings for hydraulic equipment, and diaphragm stock used in pneumatic actuators. The adipate content is limited to 20 phr in sealing applications because higher additions increase plasticizer extraction and reduce hardness retention after aging. DOA is not recommended for EPDM peroxide-cured systems where low-molecular-weight esters inhibit cure rate and lower crosslink density; published data for DOA in EPDM-specific formulations is limited and reveals cure-state regression at loadings above 10 phr when compared with paraffinic or naphthenic processing oils.

    Free Quote

    Competitive Bluesail Dioctyl Adipate (DOA) prices that fit your budget—flexible terms and customized quotes for every order.

    For samples, pricing, or more information, please contact us at +8615371019725 or mail to sales7@alchemist-chem.com.

    We will respond to you as soon as possible.

    Tel: +8615371019725

    Email: sales7@alchemist-chem.com

    Inquiry

    Get Free Quote of Alchemist Worldwide Ltd

    Flexible payment, competitive price, premium service - Inquire now!

    Certification & Compliance
    More Introduction

    Commercial designation Bluesail Dioctyl Adipate (DOA) is a monomeric ester produced by catalytic esterification of adipic acid with 2-ethylhexanol. The substance is identified by CAS 103-23-1 and EINECS 204-652-9 and is supplied as a clear, low-color liquid in bulk, intermediate bulk containers, or epoxy-phenolic lined drums. The product is classified as a plasticizer-grade adipate ester with a diester content not less than 99.0%. It is used where low-temperature flexibility, reduced plastisol viscosity, or lower solvating efficiency relative to aromatic phthalates is required.

    The structural basis for its performance is the saturated six-carbon aliphatic diacid backbone. In flexible PVC, a 2-ethylhexyl adipate ester provides greater free volume and chain mobility than an ortho-phthalate ester of the same alcohol. The difference is measurable as a shift in the Clash-Berg torsional stiffness temperature Tf of approximately 15–20 °C when DOA replaces DOP at equivalent plasticizer loading in suspension PVC K 66, evaluated to ASTM D1043-16. This behavior is relevant in freezer gaskets, cold-store curtains, automotive interior films, and cable sheathing specified for intermittent service below -30 °C.

    What specification envelope governs Bluesail DOA ester quality and handling?

    The quality envelope is defined by residual acid content, moisture, color, and ester purity. The parameters below are representative release limits; the certificate of analysis for a specific lot may contain additional data such as sulfur content, arsenic content, or clarity after heating. The ester is controlled as a chemical intermediate, not as a finished formulation component, so downstream processors should verify compatibility in the final polymer matrix.

    Representative quality specification for Bluesail DOA
    ParameterTest methodTypical value or limit
    Diester contentGB/T 166599.0%
    Acid valueGB/T 16680.02 mg KOH/g
    Platinum-cobalt colorASTM D120930
    Density at 20 °CASTM D40520.922–0.926 g/cm³
    Kinematic viscosity at 20 °CASTM D44513–14 mm²/s
    Refractive index nD20ISO 56611.446–1.448
    MoistureASTM D15330.10%
    Flash point, open cupASTM D92190 °C

    Residual acidity above 0.05 mg KOH/g is rejected because it accelerates consumption of barium-zinc or calcium-zinc stabilizer systems during PVC processing. Moisture ingress above 0.10% can produce haze in clear film and increases the risk of ester hydrolysis in moisture-sensitive cellulose ester applications. Bulk storage under dry nitrogen is required when the material is held for more than 30 days or when ambient relative humidity exceeds 60%.

    Calendering and extrusion viscosity response in 40 phr flexible PVC

    In production-scale flexible PVC processing, DOA is typically introduced into a hot dry blend at 40–60 phr depending on the target Shore A hardness. On a counter-rotating twin-screw extruder with L/D 32:1 and closed-loop barrel temperature control, DOA-plasticized dry blends reach gelation at lower melt temperatures than equivalent DOP-based dry blends. The neat kinematic viscosity of 13–14 mm²/s at 20 °C to ASTM D445 is 40–50% lower than that of DINP, which reduces melt pressure and torque during extrusion. Capillary rheometry at 180 °C and shear rates of 100–1000 s⁻¹ records lower apparent shear viscosity for DOA compounds relative to phthalate compounds at identical plasticizer loading.

    A practical processing boundary is the lower volatility of the ester relative to phthalates. Open-mill compounding with roll temperatures above 200 °C produces visible fuming and gradual plasticizer loss; therefore, melt temperatures during calendering are normally held at 160–180 °C. On polished calender bowls, roll sticking has been observed above 170 °C in calcium-zinc stabilized formulations when zinc stearate exceeds 1.0 phr. The lower polarity of DOA reduces the solubility of certain metal carboxylate complexes, and this can appear as plate-out on the embossing roll or die lips. Formulators using calcium-zinc stabilizer packages above 3.0 phr should pre-disperse the stabilizer in the plasticizer before dry blending.

    Comparison of monomeric ester plasticizer physical properties

    The distinction between DOA and other monomeric plasticizers is best expressed through neat physical properties and the resulting low-temperature response in plasticized PVC. The table below uses representative industrial literature values; exact values depend on the specific commercial grade and the test temperature.

    Comparative physical data for monomeric ester plasticizers
    PlasticizerCASMolecular weight (g/mol)Density at 20 °C (g/cm³)Kinematic viscosity at 20 °C (mm²/s)Low-temperature character in PVC
    Bluesail DOA103-23-13710.922–0.92613–14Very good; Clash-Berg Tf approximately -39 °C at 50 phr
    DOP117-81-73910.98457–65Moderate; Tf approximately -18 °C
    DINP28553-12-04180.97278–82Moderate-low; Tf approximately -29 °C
    DIDA27178-16-14270.91419–23Good; Tf approximately -34 °C

    Bluesail DOA differs from DOP primarily in the aliphatic backbone. The adipate ester lacks the aromatic ring that contributes to DOP’s higher solvent strength and higher neat viscosity. This absence reduces polymer-plasticizer intermolecular constraints, lowering the glass transition temperature more effectively. However, the lower molecular weight and aliphatic character increase volatility and extraction loss in non-polar media. In heat aging by ISO 176, DOA-plasticized sheet can lose more mass than DINP-plasticized sheet of equal thickness, so DOA is not an automatic substitute where long-term aging above 60 °C is the primary mechanical requirement.

    When a phthalate-to-adipate substitution is evaluated in extruded film

    Replacement of DOP or DINP with DOA in extruded flexible PVC film changes the plastisol or dry-blend rheology, the film blocking tendency, and the migration profile into adjacent surfaces. In a cast film line with a single-screw extruder and L/D 25:1, melt temperature at the die is usually reduced by 3–6 °C when DOA replaces DOP at the same phr; the exact reduction depends on screw speed and back pressure. The lower melt viscosity permits lower processing temperatures, which can reduce thermal stabilizer demand, but it also increases film blocking if the film is wound above 30 °C. Anti-blocking agents such as silica at 0.5–2.0 phr are commonly required.

    Migration into contact surfaces must be evaluated with a recognized extraction method. For applications involving polycarbonate or ABS housings, DOA can stress-crack the substrate more readily than polymeric adipate plasticizers. A susceptibility test such as the notched bend test described in ISO 22088 should be performed before specification. The lower polarity of DOA improves wetting of mineral fillers but reduces the solubility of certain UV absorbers; haze can develop in clear formulations if the UV absorber loading exceeds its compatibilizer-limited threshold.

    In plastisol formulations, DOA reduces Brookfield viscosity more strongly than DOP or DINP at equivalent concentration. A plastisol containing 100 phr suspension PVC and 60 phr DOA may exhibit a low-shear viscosity below 2000 mPa·s at 25 °C, whereas the same formulation with DINP can exceed 5000 mPa·s. This behavior allows higher filler addition before the viscosity reaches the target for knife-over-roll coating or rotational molding. The trade-off is a reduction in gel strength after fusion; formulators should check tensile strength to ASTM D638-14 and tear strength to ASTM D1004-13 before finalizing the plasticizer loading.

    Regulatory status and migration control in food-contact articles must be verified on the finished article. Bluesail DOA is subject to REACH registration under Regulation EC 1907/2006. For food-contact use in the European Union, the finished article must comply with Regulation (EU) No 10/2011 as amended; a migration test according to EN 1186-1 is required because published specific migration data for this exact commercial grade is limited. In U.S. applications, the end-user must confirm coverage under the applicable section of 21 CFR, such as the rubber article provisions of 21 CFR 177.2600 where the ester is used as a plasticizer in repeat-use rubber goods. The product is not a direct food additive; migration limits apply to the finished article, not to the neat plasticizer.

    Non-PVC applications include nitrocellulose lacquers, cellulose acetate butyrate coatings, and certain rubber compounds. In nitrocellulose wood lacquers, DOA is added at 5–15% of binder solids to improve cold-crack resistance measured by conical mandrel bending to ASTM D522. In cellulose acetate butyrate formulations, compatibility is limited; cloud point determinations should be run before scale-up. In acrylonitrile-butadiene rubber, DOA can be used as a low-temperature plasticizer, but its volatility limits continuous service above 80 °C. The ester is not recommended for use with strong oxidizing agents, strong acids, or amine-based additives that may catalyze ester hydrolysis or premature crosslinking reactions in the host polymer.

    Batch-to-batch consistency is monitored by gas chromatographic diester content, acid number, and color after heat stressing. The production-scale control range for acid value is 0.01–0.02 mg KOH/g; lots above 0.03 mg KOH/g are diverted from food-contact-sensitive applications. Volatile content at 150 °C by ISO 3251 is maintained below 0.1% to limit fuming during open-mill processing. The material is stored in closed carbon steel or stainless steel vessels at 5–40 °C; partially emptied containers should be blanketed with dry nitrogen because prolonged contact with humid air can raise moisture above the 0.10% specification and shift the color toward higher Pt-Co values.