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| HS Code | 958159 |
| Product Name | Dioctyl Phthalate (DOP) / Di(2-ethylhexyl) Phthalate (DEHP) |
| Abbreviation | DOP / DEHP |
| Cas Registry Number | 117-81-7 |
| Ec Number | 204-211-0 |
| Molecular Formula | C24H38O4 |
| Molecular Weight | 390.56 g/mol |
| Appearance | Clear, colorless, oily liquid |
| Odor | Slight, characteristic |
| Density | 0.985 g/cm3 at 20 °C |
| Melting Point | -55 °C |
| Boiling Point | 385 °C at 760 mmHg |
| Flash Point | 216 °C (closed cup) |
| Autoignition Temperature | 390 °C |
| Viscosity | 81 mPa·s at 20 °C |
| Refractive Index | 1.486 at 20 °C |
| Water Solubility | 0.27 mg/L at 25 °C |
| Logp | 7.6 |
| Vapor Pressure | 1.42E-5 Pa at 25 °C |
| Henry S Law Constant | 1.0E-5 atm·m3/mol |
| Surface Tension | 31.5 mN/m at 20 °C |
| Chemical Category | Phthalate ester |
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Compounding of flexible PVC insulation for non-EU cable constructions begins with a suspension resin of K-value 67–70, DEHP at 40–60 phr, a calcium-zinc or barium-zinc stabiliser at 3–7 phr, calcined clay filler at 10–25 phr, and a lubricant system adjusted for wire-line screw slip. The dry blend is mixed in a high-speed turbo mixer to a drop temperature of 105–115°C, then pelletised on a counter-rotating twin-screw extruder with L/D 28:1 and barrel zones from 145°C to 180°C. A single-screw wire coating unit with a crosshead die and pressure tooling applies the insulation at melt temperature 170–185°C. At 50 phr DEHP, volume resistivity measured by ASTM D257-14 remains above 1×1014 Ω·cm after conditioning for 24 h at 23°C and 50% RH. Tensile properties conforming to IEC 60811-501:2012 typically show a tensile strength of 16–20 MPa and elongation at break of 300–380% for unfilled insulation; the addition of calcined clay reduces elongation to 180–250% while improving cut-through resistance. The upper continuous conductor temperature is usually limited to 75°C because DEHP volatility and exudation accelerate above this threshold; 90°C-rated constructions require trimellitate or polymeric plasticiser.
Regulatory compliance is the decisive boundary. Under EU RoHS 2011/65/EU Annex II entry 7, DEHP is restricted to 0.1 wt% in homogeneous material for electrical and electronic equipment placed on the EU market. This restriction excludes DOP-based cable from most RoHS-scope products after the 22 July 2019 application date. Production of DEHP-containing cable in the EU also requires authorisation under REACH Annex XIV, so current use is concentrated in non-EU jurisdictions or products outside the RoHS scope where national migration limits are less stringent.
| DOP loading (phr) | Shore A hardness ISO 868 | Tensile strength ISO 527-2 | Elongation at break ISO 527-2 | Volume resistivity ASTM D257-14 |
|---|---|---|---|---|
| 30 | 88 ± 3 | 21–24 MPa | 240–280% | 4×1014 Ω·cm |
| 50 | 75 ± 3 | 16–20 MPa | 300–380% | 1×1014 Ω·cm |
| 70 | 62 ± 3 | 11–14 MPa | 360–430% | 6×1013 Ω·cm |
Representative formulation response envelope for suspension PVC K-value 67 with Ca-Zn stabiliser; production values vary with resin particle size distribution, filler type, and extrusion history. No product specification should be derived from this table without full qualification testing.
Calendered vinyl flooring compounds built around suspension PVC K-value 66–68 are plasticised with DEHP at 50–80 phr in the foamable core and 40–55 phr in the transparent wear layer. A Farrel continuous mixer discharges at 165°C, after which the melt passes to a two-roll mill and then an inverted-L four-roll calender with roll temperatures 170–195°C. The foamable core contains azodicarbonamide at 1.5–3.0 phr; decomposition in a hot-air fusion oven at 185–205°C produces a closed-cell structure with density 0.60–0.80 g/cm³. The wear layer is applied at 170–185°C and embossed on the last calender roll. Hardness of the fused wear layer is 70–80 Shore A per ISO 868; tensile strength per ISO 527-2 is 14–18 MPa for a 0.35 mm sheet. Residual indentation after 150 min at 23°C is typically below 0.10 mm for the compact layer when measured by EN 433:1994. DEHP-containing flooring sold in the EU as an article triggers REACH Article 33 SVHC notification at 0.1 wt%; EU manufacture itself requires authorisation under REACH Annex XIV, so production lines for this formulation are located outside the EU or use non-phthalate plasticisers.
| Layer | DEHP (phr) | CaCO₃ filler (phr) | Azodicarbonamide (phr) | Fusion oven set point | Density |
|---|---|---|---|---|---|
| Foamable core | 55–70 | 25–45 | 1.5–3.0 | 190–200°C | 0.60–0.80 g/cm³ |
| Compact underlayer | 45–55 | 40–60 | — | 180–190°C | 1.30–1.45 g/cm³ |
| Transparent wear layer | 40–55 | 0–10 | — | 170–185°C | 1.20–1.25 g/cm³ |
On full-scale calender lines, the principal failure mode is plasticizer exudation at the wear-layer interface when DEHP exceeds 55 phr and roll take-off speed exceeds 25 m/min. Exuded DEHP causes detachment of polyurethane top coats and increases the coefficient of friction on the sheet surface. The compounder must therefore control plasticizer absorption by raising dry-blend temperature to 110°C before Banbury mixing and limiting storage of compounded sheet to 48 h at 30°C.
Knife-over-roll coating of PVC paste resin for synthetic leather, footwear uppers, and tarpaulin covers is governed by the gelation and fusion profile of the plastisol. Dispersion-grade paste resin of K-value 72–80 is mixed under high shear in a planetary mixer; DEHP is added at 50–75 phr to give a Brookfield RVT viscosity of 2,000–6,000 mPa·s at 20 rpm and 25°C. At this loading the plastisol remains pseudoplastic, allowing coating at line speeds of 15–35 m/min. The coated web enters a forced-air fusion tunnel with zone set points from 160°C to 200°C; complete fusion requires a substrate surface temperature of 180–195°C for 60–120 s, depending on coat weight and air velocity. At 170°C the plastisol remains incompletely fused, producing haze, low peel strength, and surface defects; above 205°C, DEHP volatilisation increases and fabric scorch risk becomes measurable. The practical throughput ceiling is therefore set by a narrow dwell-temperature plateau of ±5°C for thin skins, a primary process conflict in high-speed coating.
Peel adhesion to polyester and cotton fabrics is product-specific, but DEHP migration to the bond line weakens wet adhesion after hydrolysis ageing. Automotive interior applications generally reject DEHP-containing skins because DIN 75201:2011 fogging tests show condensate mass above OEM limits when DEHP exceeds 5 wt% of the plastisol formulation. For articles exported to the EU, REACH Article 33 notification applies at 0.1 wt% DEHP in the coated fabric. The formulation is therefore retained for industrial tarpaulins, bookbinding covers, and non-automotive upholstery outside EU RoHS or REACH authorisation requirements.
Extrusion-cast PVC film using DEHP at 30–45 phr is compounded for industrial stationery, book covering, non-food adhesive tape backings, and self-adhesive decorative sheet. In a 65 mm single-screw extruder with L/D 30:1 and barrier screw, barrel temperatures from 160°C to 190°C are maintained; the melt is polished through a three-roll stack at 60–90°C before embossing. Hardness is 75–85 Shore A per ISO 868; tensile strength measured by ISO 527-3 is 15–20 MPa for film at 0.20 mm thickness. DEHP surface migration over time lowers print adhesion on uncoated film; corona treatment above 42 mN/m is required before solvent-based ink application. The film is not suitable for food contact under Regulation (EU) No 10/2011 because DEHP is not listed as an authorised additive for food-contact plastics.
Soft PVC profiles, appliance gaskets, suction hose, and pneumatic tubing are produced by single-screw extrusion of dry blends containing 50–75 phr DEHP, suspension PVC K-value 64–70, and 10–30 phr coated calcium carbonate. The dry blend is prepared in a turbo mixer to 105°C and cooled; the extruder screw has a compression ratio of 2.5:1 and barrel temperatures from 150°C to 180°C, giving a melt pressure of 12–18 MPa at the die. Hardness after cooling is 55–70 Shore A per ISO 868; low-temperature brittleness is -25°C to -30°C per ASTM D746-20 for unfilled compounds. The primary limitation is extraction in paraffinic and aromatic oils: immersion in ASTM Oil No. 3 at 70°C for 72 h can produce mass loss of 5–12% because DEHP is soluble in the oil phase. This extraction shrinks gaskets and increases hardness by 8–15 Shore A, creating seal leakage; nitrile rubber vinyl blends or polymeric plasticiser are required for oil-contact service.
Nitrocellulose lacquers for wood finishing, gravure ink opacifiers, and screen-printing clear coats are plasticised with DEHP at 3–8 wt% of total non-volatile solids to reduce film cracking and improve cold flex. The plasticizer is pre-dispersed in a ketone-ester solvent blend before high-speed dispersion; final viscosity at 25°C is 30–60 s through a Ford #4 cup per ASTM D1200-10. Free-film elongation improves from brittle failure below 2% to 8–15% when tested by ISO 527-3. Compatibility is not unlimited: DEHP loading above 10 wt% of non-volatile solids tends to produce surface exudation and blocking under stacking pressure during warehouse storage. DEHP remains extractable by ethanol and sebum simulants, so these formulations are not suitable for toy coatings under REACH Annex XVII entry 51, which caps DEHP at 0.1 wt% of plasticised material in toys and childcare articles.
Where solvent-cement open time must be extended without altering PVC solubility, DEHP is occasionally added as a secondary plasticiser at 3–10 phr in white or grey PVC pipe cements based on 10–18 wt% PVC resin dissolved in cyclohexanone-THF. The mixed adhesive is applied by brush or trowel at 5–25°C; solvent cement joints are tested according to ASTM D2564-20 requirements for PVC pipe and fittings. DEHP addition improves the flexibility of the dried bond line but lowers resistance to aromatic hydrocarbon service and increases long-term extractables in industrial pressure systems. For EU industrial supply, the formulation must be reviewed against REACH Article 33 notification and Annex XIV authorisation duties because DEHP remains present at 0.1 wt% or more in many finished adhesives.
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Commercial dioctyl phthalate, commonly designated DOP or DEHP, is a primary ortho-phthalate plasticizer supplied as a clear, nearly anhydrous ester liquid. The manufacturing route is esterification of phthalic anhydride with 2-ethylhexanol; the resulting substance is bis(2-ethylhexyl) phthalate with CAS number 117-81-7, molecular formula C24H38O4, and molecular mass 390.56 g/mol. Industrial trade names typically include numerical designations such as DOP 99.5 and DOP-P, with the suffix indicating minimum ester content or a low-acidity production route; because nomenclature is producer-specific, batch acceptance is based on the purchase specification rather than the trade name. Typical incoming limits for standard grade are ester content ≥99.5 wt%, acidity as phthalic acid ≤0.010 wt%, water content ≤0.10 wt%, and Pt-Co colour ≤20 APHA. In flexible polyvinyl chloride compounding, DOP functions as a primary plasticizer: it lowers melt viscosity, reduces glass transition temperature, and confers softness and elongation to coated fabrics, cable compounds, flooring, hoses, and plastisols. It differs from diisononyl phthalate in solvating strength and regulatory classification; from dioctyl terephthalate in backbone chemistry and low-temperature response; and from trioctyl trimellitate in high-temperature permanence.
Incoming quality control for flexible PVC dry-blend and extrusion operations usually applies gas-chromatographic purity, acidity, moisture, colour, and density tests. The acceptance boundary is not a single value but a set of correlated limits: moisture ingress above 0.10 wt% during tank storage can hydrolyse the ester, raising acidity and shifting colour. Carbon steel storage at 15–30°C is acceptable when moisture is excluded; stainless steel or lined carbon steel is used for plastisol grades where colour stability is critical.
| Property | Typical acceptance range | Test method |
|---|---|---|
| Ester content | ≥99.5 wt% | ASTM D3465 |
| Acidity, as phthalic acid | ≤0.010 wt% | ASTM D1045 or GB/T 1668 |
| Water content | ≤0.10 wt% | ASTM E203 |
| Colour, Pt-Co | ≤20 APHA | ASTM D1209 |
| Density at 20°C | 0.984–0.988 g/cm³ | ASTM D4052 |
| Refractive index nD20 | 1.485–1.487 | ASTM D1218 |
| Flash point, Cleveland open cup | ≥200°C, typical 218°C | ASTM D92 |
| Viscosity at 20°C | 77–82 mPa·s | ASTM D445 |
Dry-blend extrusion of flexible PVC is not a simple metering operation. In high-speed mixers with working capacities from 200 L to 500 L, resin temperature is raised by friction to 110–120°C; DOP is introduced when the resin reaches 80–90°C so that absorption into primary PVC particles begins before peak temperature. Batch-to-batch variation in dry blend quality is commonly traced to resin moisture above 0.2 wt% or to worn mixer blades that reduce shear work. On counter-rotating twin-screw extruders with L/D 25:1 to 33:1, melt temperature is normally maintained below 190°C; thermal history above this threshold increases plasticizer volatility and surface plate-out. DOP reduces melt pressure and torque relative to rigid PVC, but the quantitative effect is screw-specific and cannot be transferred between machines without capillary rheometry data. Compounds with 30–50 phr DOP are typically extruded into profiles and hose jackets without pre-drying if the plasticizer water content remains below 0.10 wt%; at relative humidity above 60%, resin pre-drying at 80°C for 2 h is common.
In plastisol coating and rotational casting, DOP acts as both solvent and permanent plasticizer. Initial paste viscosity on a Brookfield RVT viscometer at 20 rpm and 25°C for a 60 phr DOP paste based on an emulsion PVC of K-value 70 commonly falls between 1500 mPa·s and 3500 mPa·s. Single-point viscosity is insufficient for release because viscosity ageing over 72 h at 35°C indicates storage stability: an increase greater than 30% is often rejected for knife-over-roll coating because it shifts coating thickness control. In dip-moulding lines, vacuum deaeration at 20–50 mbar is used to remove entrained air; residual bubbles in the gelled layer depend on solvating rate and resin particle size distribution as much as on surface tension. DOP solvates suspension resin more aggressively than diisononyl phthalate but less aggressively than butyl benzyl phthalate; this is exploited in formulations that require partial solvation for low paste viscosity.
Plasticization by DOP is based on dipole interaction between ester carbonyl groups and polar sites on the PVC chain, followed by free-volume expansion. Differential scanning calorimetry under ASTM D3418 on a PVC compound of K-value 67 containing 40 phr DOP typically shows a broad glass transition in the region of −20°C to −30°C, compared with approximately 80°C for the unplasticized resin. The reduction is not linear with plasticizer loading; above 70 phr, incremental lowering of glass transition becomes smaller and exudation risk increases. Compatibility is evaluated under compression by ASTM D3291 loop test; surface spew after 72 h at 70°C indicates incompatibility. This behaviour sets a practical upper limit for DOP in many semi-rigid formulations, despite its high solvating strength.
DOP is added to PVC resin at ambient temperature for low-speed liquid blending only when a high-shear mixer is unavailable; this practice produces longer absorption times and is limited to laboratory trials.
Wire jacketing formulations are used to compare DOP with dioctyl terephthalate and trioctyl trimellitate because of the simultaneous demands for flexibility, electrical insulation, and oil resistance. DOP is a general-purpose primary plasticizer for PVC jacketing at continuous conductor temperatures below 60°C; volume resistivity measured by ASTM D257 is typically specified at ≥1×1012 Ω·cm at 20°C when stabilizer selection avoids ionic contamination. In oil immersion testing for sheath compounds, IEC 60811-404 provides mass uptake comparison; DOP-based jackets show higher mass loss into ASTM No. 2 oil at 70°C for 168 h than TOTM-based jackets. For hardness-matched compounds, TOTM generally requires 10–15 phr higher loading than DOP when Shore A hardness is measured by ASTM D2240. DOTP can match DOP hardness at nearly equal loading but provides lower volatility loss under ASTM D2288 and better low-temperature flexibility by ASTM D1043. The regulatory difference is equally material: DEHP is classified as Repr. 1B with hazard statement H360FD under the CLP Regulation, whereas DOTP and TOTM are not classified as reproductive toxicants. This distinction affects safety data sheets, waste management, and customer qualification, not simply formulation cost.
| Performance parameter | DOP/DEHP | DINP | DOTP | TOTM | Test method |
|---|---|---|---|---|---|
| Relative phr for Shore A 80 | 1.00 reference | 1.03–1.07 | 1.00–1.02 | 1.10–1.15 | ASTM D2240 |
| Volatility loss, 24 h at 100°C | 1.5–2.0 wt% | 0.7–1.0 wt% | 0.8–1.2 wt% | 0.3–0.5 wt% | ASTM D2288 |
| Clash-Berg low-temperature flex, Tf | −24°C to −18°C | −20°C to −15°C | −30°C to −25°C | −15°C to −10°C | ASTM D1043 |
| Regulatory trigger | REACH Annex XVII entry 51, RoHS 2011/65/EU | REACH Annex XVII entry 52, toys and childcare only | No reproductive classification | No reproductive classification | — |
Migration of DOP from flexible PVC into contacting media is diffusion-controlled in the early stages. Published diffusion coefficients for DEHP in plasticized PVC at 25°C generally lie between 10−12 cm²/s and 10−9 cm²/s, with the higher values observed at plasticizer loadings above 40 phr and in highly mobile media. Fatty food simulants extract measurably more plasticizer than aqueous simulants; under Commission Regulation (EU) No 10/2011, 95% ethanol or isooctane is used to simulate fatty contact. For toys and childcare articles, REACH Annex XVII entry 51 restricts DEHP to ≤0.1 wt% of the plasticized material. RoHS Directive 2011/65/EU imposes a similar 0.1 wt% limit in homogeneous materials used in electrical and electronic equipment. These boundaries do not exclude DOP from industrial hoses, flooring, or profiles, but they require analytical verification of finished articles and segregation of non-compliant compounds.
For medical devices, DEHP is not universally banned, but Commission Regulation (EU) 2017/745 requires justification of DEHP use where patient exposure risk cannot be controlled by design; infusion tubing and blood bags are conventional DOP applications that require risk-benefit documentation. The operational boundary is defined by the intended exposure route and contact time.
In calendered film and sheet production, DOP is incorporated in hot-mix cycles and the melt is processed on four-roll calenders with roll surface temperatures from 150°C to 170°C. The roll gap is adjusted to control the plastified compound bank; plasticizer volatility becomes visible as condensation on extraction hoods when stock temperature exceeds 180°C. Published data for specific calender line configurations is limited, but process operators typically monitor extract air back pressure and roll surface cleanliness rather than relying on a fixed temperature setpoint alone. The selection of DOP over diisodecyl phthalate or DOTP in calendered sheet is often influenced by the interplay of solvating strength, line speed, and end-use hardness specification, with Shore A hardness measured by ASTM D2240 and tear strength by ASTM D624 or ASTM D1004.