| HS Code | |
| Productname | Dioctylphthalate |
| Chemicalname | Bis(2-ethylhexyl) phthalate |
| Synonyms | DOP; DEHP; Dioctyl phthalate |
| Casnumber | 117-81-7 |
| Ecnumber | 204-211-0 |
| Molecularformula | C24H38O4 |
| Molecularweight | 390.56 g/mol |
| Appearance | Colorless to light yellow viscous liquid |
| Odor | Mild odor |
| Density | 0.985 g/cm3 at 20 °C |
| Meltingpoint | -55 °C |
| Boilingpoint | 385 °C |
| Flashpoint | 206 °C |
| Vaporpressure | 1.3e-7 mmHg at 25 °C |
| Viscosity | 81 mPa·s at 20 °C |
| Refractiveindex | 1.485 at 20 °C |
| Watersolubility | 0.27 mg/L at 25 °C |
| Logp | 7.60 |
| Henrylawconstant | 1.5e-7 atm·m3/mol |
| Autoignitiontemperature | 390 °C |
As an accredited Dioctylphthalate factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | Dioctylphthalate is packaged in 200 L steel drums, sealed, labeled, and stored in a cool, dry, well-ventilated location. |
| Container Loading (20′ FCL) | Dioctylphthalate is packed in drums or IBCs, then loaded into a 20′ FCL container, secured and stowed for ocean shipment. |
| Shipping | Dioctyl phthalate (DEHP) is generally not regulated for transport unless it meets marine pollutant criteria. If regulated, ship as UN3082, Environmentally hazardous substance, liquid, n.o.s. (Dioctyl phthalate), Class 9, Packing Group III, Marine Pollutant, with required markings, labels, and documentation. |
| Storage | Store Dioctylphthalate in a cool, dry, well-ventilated area away from direct sunlight, heat, sparks, and open flames. Keep containers tightly closed, clearly labeled, and upright. Use compatible containers; avoid materials softened by plasticizers. Separate from strong oxidizers, acids, and bases. Store at ambient temperature, protected from moisture. Provide secondary containment to control spills, and follow local regulations. Ensure adequate ventilation. |
| Shelf Life | Dioctylphthalate generally has an indefinite shelf life when stored in sealed containers away from heat, light, and moisture. |
In industrial low-voltage cable manufacturing, bis(2-ethylhexyl) phthalate (DOP, CAS 117-81-7, EC 204-211-0) is metered into suspension-grade PVC insulation compound at 35–55 phr in primary insulation and 40–60 phr in outer sheathing. The upper loading limit is governed less by plastication efficiency than by exudation risk after repeated thermal cycling between −25 °C and 105 °C and by the EU RoHS Directive 2011/65/EU Annex II entry 8 maximum concentration value of 0.1% DEHP by weight in homogeneous materials for electrical and electronic equipment. The resulting compound typically falls within a Shore A hardness range of 75–88, which permits stable dispersion of stabilizer, antimony trioxide, and flame-retardant packages without excessive screw torque. Migration of DOP from cable sheathing into adjacent polycarbonate enclosures is a documented production-line failure mode when harness bundles are clamped into clear PC housings; stress crazing at the contact interface can require barrier tape, DEHP content reduction, or substitution with a non-phthalate plasticizer. EU REACH Annex XIV authorization obligations apply to DEHP placed on the EU market unless an allowed exemption exists, while EU REACH Annex XVII entry 51 restrictions for toys and childcare articles are not the controlling industrial-cable requirement; final-article classification must nonetheless be confirmed when cable assemblies enter consumer products.
| Regulatory instrument | Scope | Threshold / test method |
|---|---|---|
| EU RoHS 2011/65/EU Annex II entry 8 | DEHP in electrical and electronic equipment cables | 0.1% by weight in homogeneous material |
| EU REACH 1907/2006 Annex XIV | DEHP placed on the EU market | Authorization obligation unless an applicable exemption is demonstrated |
| IEC 60227-3:2018 | 450/750 V PVC insulated and sheathed cables | Aged tensile and elongation requirements for PVC compounds |
| ISO 6722-1:2011 | Road vehicle 60 V/600 V single-core cables | Temperature class and abrasion test matrix for automotive primary wire |
| California Proposition 65 | DEHP exposure warnings for covered products | Warning obligation where exposure threshold is exceeded |
Production-scale compounding runs through a high-speed hot mixer at 100–120 °C, a cooling mixer at 40–60 °C, and a co-rotating twin-screw extruder with L/D 28:1–36:1 operating at melt temperature 145–180 °C. The pelletized compound is then extruded onto copper or aluminium conductors in a 25:1–30:1 single-screw crosshead extruder at 160–190 °C, with insulation wall thickness between 0.6 mm and 1.0 mm under continuous spark testing. Terminal finished article types include building wire specified under IEC 60227-3:2018, automotive primary wire under ISO 6722-1:2011, appliance wiring harnesses, and industrial control cable jackets where RoHS-limited DEHP content is accepted or explicitly declared by the equipment manufacturer.
Wear-layer formulation in heterogeneous PVC floor covering places DOP at 25–35 phr in transparent or pigmented compact layers and at 50–70 phr in chemically foamed core layers; the lower compact-layer loading is controlled by residual indentation recovery, lacquer adhesion after embossing, and resistance to plasticizer migration into adjacent rubber shoe soles, not by tensile strength alone. Finished sheet flooring specified under EN 649:2011 and ISO 10582:2017 must retain dimensional stability and defined residual indentation performance; excessive DOP at the wear-layer surface degrades both properties after long-term service under castor-chair load. Plastisol is produced in a vacuum dispersion mixer at 0.1–0.2 bar absolute to remove entrained air, coated by knife-over-roll at 0.4–1.2 mm wet film thickness, gelled through a multi-zone infrared/convection tunnel at 160–200 °C, and the foamed cushion is expanded at 180–210 °C before mechanical embossing. The foam expansion window is narrow because DOP volatility accelerates cell coalescence above 210 °C, while gelation insuffiency below 160 °C produces open surface pores and lacquer pinholes. EU-facing flooring operations evaluate DOP against REACH Annex XIV authorization obligations, and construction-sector indoor air quality assessment schemes increasingly require homogeneous-material disclosure for phthalate content. Terminal finished categories include heterogeneous vinyl sheet, luxury vinyl tile, wall base profiles, and acoustically modified sports flooring.
For release-paper cast synthetic leather, DOP loading in the compact skin coat is maintained between 45 phr and 65 phr, while the foamed mid-coat is compounded at 55–70 phr; this gradient preserves the low Brookfield viscosity required for knife-over-roll metering at line speeds above 15 m/min while limiting surface tack on finished articles. FMVSS 302 horizontal burn-rate compliance at a maximum of 102 mm/min forces co-formulation with antimony trioxide and phosphate or brominated flame retardants because DOP contributes to smoke density during early-stage combustion. VDA 278:2011 VOC and fogging limits for automotive interior materials impose an upper practical loading because condensed plasticizer on glazing surfaces is measured as a FOG component after thermal desorption according to the norm. The process deposits a skin layer on structured release paper, gels it at 160–200 °C, applies the foamed mid-coat, laminates a polyester/cotton backing with an adhesive tie coat, strips the release paper after cooling, and embosses at 180–210 °C; foam cell collapse is controlled by maintaining the gelation centerline within ±5 °C. Finished article types are automotive seat covers, door panel skins, headliner trim, and heavy-gauge technical tarpaulin for outdoor textile structures.
Robot-applied PVC underbody sealant formulated with DOP at 50–80 phr requires a shear-thinning viscosity profile that permits airless spray through a 0.69–0.84 mm nozzle while preventing slumping on vertical electrophoretic primer surfaces before entering the paint shop oven. The cured film is tested for stone-chip resistance under SAE J400 and for dry/wet adhesion by ISO 4624 pull-off after neutral salt spray exposure to ISO 9227; DOP-rich films above 2 mm dry-film thickness can lose adhesion at the primer interface if oven cure drops below 130 °C, because volatile residues are trapped under a skin that crosslinks before the bulk layer gels. The process applies material at 30–40 °C through an airless robot gun, then cures at 130–160 °C for 15–30 min; oven slope and recirculation airspeed determine whether the plastisol reaches full gelation at the deepest seam geometries. Terminal finished types are underbody anti-stone-chip coatings, seam sealing compounds, wheel arch linings, and floor pan deadener coatings where calcium carbonate extender loading is adjusted to control DEHP surface migration.
In closed-cell NBR/PVC insulation for HVAC refrigeration piping, DOP is incorporated at 10–30 phr relative to the polymer blend, where it reduces Banbury mixing torque and shifts the brittle point to −30 °C; above 30 phr, sulfur/accelerator vulcanization of the nitrile phase is retarded, and compression set after slit-tube installation deteriorates within the first heating cycle. ASTM C534 and EN 14304:2015 govern product density, thermal conductivity, water-vapour permeability, and reaction-to-fire classification, while EU REACH Annex XIV authorization obligations apply to DEHP formulated for the EU market. Mixing runs in an internal mixer at 100–130 °C, drops on a two-roll mill at 60–80 °C, then proceeds through a vented extruder with azodicarbonamide chemical blowing agent; expansion and curing occur in a continuous hot-air tunnel at 150–180 °C, where residual DOP migration to the surface reduces polymer skin tension and widens cell diameter distribution if the tunnel temperature profile deviates from centerline by more than 5 °C. Terminal finished types are preformed pipe insulation tube, sheet and roll stock, duct liner, and slit-fit jacket segments for refrigerant and chilled-water lines.
Extrusion of flexible PVC profiles and industrial hoses uses DOP at 30–50 phr, producing a Shore A hardness between 65 and 85 and a low-temperature brittle point near −35 °C; the lower loading boundary is fixed not by hardness but by kinking during coiling in subzero warehouses and by notch sensitivity under clamp crush on pneumatic lines. Suction and discharge hoses for aqueous chemical transfer are specified under EN ISO 3994:2014, while EU RoHS applies only when the article is integrated into electrical/electronic equipment. Potable-water and food-contact constructions lie outside the practical application window because customer-specific declarations and brand restrictions typically prohibit DEHP-containing compounds. The process converts dry blend produced in a hot/cool mixer at 100–120 °C and 40–60 °C into finished shape through a vented single-screw extruder with L/D 25:1–30:1 at 150–180 °C, followed by vacuum calibration, water cooling, and coiling or precision cutting; multi-layer hose constructions use a DOP-free inner layer where extraction resistance is required. Finished article types are textile-braided industrial hose, pneumatic tubing, furniture edge trim, and glazing gasket profiles for non-automotive use.
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Dioctylphthalate, chemically defined as bis(2-ethylhexyl) benzene-1,2-dicarboxylate and registered under CAS 117-81-7, EC 204-211-0, is supplied as a clear, oily diester of phthalic acid and 2-ethylhexanol. The compound has the molecular formula C24H38O4 and a molar mass of 390.56 g/mol. In flexible PVC processing, the same substance is commonly designated DOP or DEHP, with DEHP referring to the bis(2-ethylhexyl) ester form. Bulk technical-grade Dioctylphthalate is normally accepted against GB/T 11406-2001 for industrial-grade material, while sampling and routine testing follow ASTM D1045-19 for plasticizer esters. Because the product is traded as a base chemical rather than as a formulated product with proprietary model codes, the specification is the practical identifier: technical, low-color, low-acidity, and low-moisture electrical grades differ mainly in tightened limits for moisture, acidity, color, and trace conductivity.
| Parameter | Unit | Typical acceptance range | Reference method |
|---|---|---|---|
| Ester content | % by mass | ≥99.5 | GB/T 11406-2001 / ASTM D1045-19 |
| Acidity as phthalic acid | % by mass | ≤0.010 | GB/T 11406-2001 |
| Water content | % by mass | ≤0.10 | ASTM E203 |
| Density at 20 °C | g/cm³ | 0.983–0.987 | ASTM D4052 |
| Refractive index n20/D | — | 1.485–1.487 | ASTM D1218 |
| Flash point, Cleveland open cup | °C | ≥207 | ASTM D92 |
| Pour point | °C | ≤-46 | ASTM D97 |
Neat Dioctylphthalate displays a dynamic viscosity of approximately 75–82 mPa·s at 20 °C and near 56 mPa·s at 25 °C. This steep temperature dependence must be accounted for when calibrating mass-flow meters on bulk unloading skids. The normal boiling point is approximately 385 °C at 760 mm Hg; however, prolonged heating above 150 °C in open storage can increase color and acidity, so nitrogen blanketing or sealed headspace is used for installations where bulk storage exceeds 30 days.
Dioctylphthalate functions as a primary plasticizer. Its ortho-phthalate diester structure interacts strongly with amorphous PVC and reduces glass-transition-related stiffness at loadings of 40–60 phr in a K-value 67 suspension resin. At 50 phr DOP, a calendered film compound commonly shows Shore A hardness of 78–82 under ISO 868, tensile strength of 14–18 MPa, and elongation at break of 250–350 % under ISO 527-2. Low-temperature brittleness under ASTM D746 is typically in the range of -25 °C to -30 °C for the same compound. Compared with dibutyl phthalate, CAS 84-74-2, Dioctylphthalate has a higher molar mass and lower vapor pressure, which reduces volatile loss but also slows initial gelation. Compared with dioctyl terephthalate, Dioctylphthalate is generally more cost-efficient in standard industrial compounds but produces higher volatile loss and higher extractable mass in non-polar media under ASTM D1203-16 and ISO 6452 fogging tests.
DINP, represented by CAS 28553-12-0, has a higher molar mass of 418.61 g/mol and is less solvating per unit mass; a direct mass-for-mass substitution from DOP usually requires a small formulation increase to match hardness. The resulting DINP compound typically gives lower volatility and lower migration in automotive interior fogging, but the higher plasticizer viscosity can reduce dry-blend absorption rate in high-intensity mixers. DOTP, CAS 6422-86-2, is a terephthalate isomer with the same molar mass as DOP but a para-substituted structure; it is selected for higher-temperature wire jackets because it shows lower mass loss and lower exudation, although published data for exact melt-pressure differences on a given extruder configuration is limited. TOTM, CAS 3319-31-1, is a trimellitate of higher molar mass 546.78 g/mol and is used where low volatility and high heat stability are critical, such as 90 °C or 105 °C PVC insulation compounds.
| Parameter | Dioctylphthalate | DINP | DOTP | TOTM |
|---|---|---|---|---|
| CAS registry | 117-81-7 | 28553-12-0 | 6422-86-2 | 3319-31-1 |
| Molar mass (g/mol) | 390.56 | 418.61 | 390.56 | 546.78 |
| Density at 20 °C (g/cm³) | 0.983–0.987 | 0.973–0.977 | 0.980–0.986 | 0.986–0.992 |
| Volatility/migration profile | Higher volatility than DINP and DOTP | Lower volatility than DOP | Lower volatility and lower extraction than DOP | Lowest volatility of the listed plasticizers |
| EU regulatory status | REACH Annex XIV authorisation and Annex XVII entry 51 restriction in toys | Restricted under REACH Annex XVII entry 51 in toys and childcare articles | Not subject to the same ortho-phthalate listing | Not subject to the same ortho-phthalate listing |
In a production-scale flexible PVC calendering line, Dioctylphthalate is metered by loss-in-weight feeders and dispersed in a high-intensity mixer at drop temperatures near 110 °C. The dry blend then enters a counter-rotating twin-screw extruder with L/D ratio between 36:1 and 40:1, where barrel zones are held at 150 °C to 170 °C. Operators maintain calender roll temperature within ±5 °C across the roll width because a deviation above this window accelerates volatile plasticizer loss and can generate plate-out on chrome polishing rolls. Plastisol viscosity is measured under ASTM D1824-16; a DOP-containing plastisol based on K-value 67 paste resin and 60 phr plasticizer typically falls within a Brookfield RVT viscosity range of 1,500–3,500 mPa·s at 20 rpm, depending on filler, stabilizer, and resin grade. The same formulation can exhibit much lower high-shear viscosity during knife-over-roll coating, which is why low-shear Brookfield data alone does not predict coating head pressure.
Fusion torque response measured in a torque rheometer under ASTM D2538-18 decreases as Dioctylphthalate loading increases. At 40 phr DOP, the fusion peak appears at a lower stock temperature than at 30 phr DOP, but the decrease is not linear because free plasticizer also changes dry-blend bulk density and feed stability. On a twin-screw line with L/D 36:1, increasing DOP feed above 65 phr without adjusting resin feed can reduce melt pressure by 0.5–1.5 MPa, but may move the melt into an overplasticized regime with poor dimensional stability at the die lip. Published data for every screw geometry and temperature profile is limited, so alarm limits should be established by process-capability trials on the specific line.
Field experience with bulk handling shows that batch-to-batch moisture variation above 0.10 % by mass can produce surface roughness on high-speed sheet extrusion, particularly when ambient relative humidity exceeds 60 %. Pre-drying of the powder blend or vacuum devolatilization on the extruder at -0.08 MPa is used to prevent blistering and gloss reduction. If the stabilizer system is calcium-zinc buffered, free acidity from the plasticizer above 0.010 % can consume part of the stabilizer reserve and shorten thermal stability time under ISO 182-2.
Storage and handling boundaries include incompatibility with strong aqueous alkali, which saponifies the ester to sodium phthalate and 2-ethylhexanol. Caustic cleaning systems should not be used on Dioctylphthalate-wetted transfer lines unless a solvent flush is specified. Contact with strong oxidizing agents should be avoided. Bulk storage tanks are typically stainless steel or lined carbon steel; elastomer seals and sight glasses should be evaluated because the ester can plasticize or extract certain rubber components.
Under EU RoHS Directive 2011/65/EU, Annex II as amended by (EU) 2015/863, DEHP is restricted to 0.1 % by weight in homogeneous materials used in electrical and electronic equipment placed on the EU market after 22 July 2019. Under REACH Annex XVII, entry 51, Dioctylphthalate cannot be placed on the market in toys or childcare articles at concentrations greater than 0.1 % by mass of the plasticized material, individually or in combination with DBP and BBP. These restrictions do not automatically prohibit all industrial DOP use, but they exclude many consumer-facing PVC products unless an authorisation is held under REACH Annex XIV.
Reformulation to a non-restricted plasticizer is not a direct mass substitution. At equivalent plasticizer volume, DOTP may raise compound viscosity slightly and can shift fusion torque response, while TOTM generally requires higher processing temperatures. Qualification of an alternative requires migration testing under EN 71-9 or EN 71-10 for toy applications, plus heat-aging retention under IEC 60227 insulation requirements if the component is a wire jacket. Compounds containing Dioctylphthalate remain technically available for industrial applications where REACH authorisation is held, but those grades are excluded from children’s articles and from electrical and electronic equipment above the homogeneous-material concentration limit of 0.1 % under Directive 2011/65/EU as amended by (EU) 2015/863.