Diisononyl phthalate (DINP; CAS 28553-12-0 / 68515-48-0) is a high-boiling branched C9 phthalate ester supplied as a general-purpose plasticizer for flexible poly(vinyl chloride) and plastisol compounds. Commercial DINP is not a single molecular model but a controlled mixture of branched isononyl alcohol esters of phthalic anhydride; supplier designations such as Palatinol N and Jayflex DINP refer to isomer blends rather than distinct chemical entities. Typical release data include an ester content of 99.5–99.8 wt%, acid number ≤0.03 mg KOH/g, water content ≤0.10 wt%, density at 20°C of 0.972–0.977 g/cm³, dynamic viscosity at 20°C of 78–88 mPa·s, refractive index at 25°C of 1.484–1.488, and flash point above 215°C by ASTM D92 Cleveland open cup. The calculated relative molecular mass is 418.6 g/mol for the C26H42O4 ester, higher than DEHP at 390.6 g/mol, which accounts for the reduced volatility and greater permanence reported in high-temperature vinyl compounds.

Bulk storage configurations are tank trucks, flexitanks, 1,000 L intermediate bulk containers, and 200 L epoxy-lined steel drums. Transfer lines should be moisture-traced where ambient RH exceeds 60% because water ingress above 0.10 wt% increases the equilibrium acid number and can corrode carbon steel storage. Production lots should be checked against the supplier certificate of analysis for density at 20°C and gas-chromatographic isomer distribution; published data linking exact branched isomer ratio to plastisol rheology is limited, but field records indicate viscosity scatter of up to ±8% across equivalent shipments in winter conditions when capillary viscosity measurements are made without full temperature equilibration.

What Release Limits Govern Acid Number, Moisture, and Colour in Bulk DINP?

Bulk release criteria for general-purpose DINP are commonly based on ASTM D1045-19 for plasticizer sampling and testing, with supplementary methods for water and colour. Acid number is controlled to ≤0.03 mg KOH/g; values above 0.05 mg KOH/g are considered off-specification because residual acidity accelerates ester hydrolysis and attacks calcium carbonate fillers in dry-blend compounding. Water content is measured by Karl Fischer titration per ASTM E203-16 and held at ≤0.10 wt%. Platinum-cobalt colour by ASTM D1209-05 is typically ≤20 for clean general-purpose product; heat-aged colour after 2 h at 177°C is often specified at ≤40 but remains supplier-specific. A documented plant failure mode is colour drift in bulk storage tanks fitted with copper-alloy heating coils: field audits record Pt-Co values rising from 15 to 35 after 10 days at 60°C when coil passivation is incomplete.

Bulk storage in unheated carbon steel tanks at 20–30°C is acceptable when the vapour space is nitrogen-blanketed or desiccant-dried. Tanks with aluminium fittings are preferred to copper alloys because copper ions accelerate colour and peroxide formation; if copper heating coils are used, they should be passivated. Filtering through 10 µm bag filters before tank discharge prevents rust and polymer residues from reaching compounding units.

Volatility, Fusion Torque, and Low-Temperature Response Relative to DEHP and DIDP

The selection of DINP over DEHP or DIDP is primarily a balance among volatility, processing viscosity, and low-temperature flexibility. At equal plasticizer loading of 50 phr in suspension PVC K-value 67, DINP produces Shore A hardness approximately 2 points higher than DEHP and a brittleness temperature by ASTM D746-14 that is 2–4°C higher; DIDP is generally 1–2°C higher than DINP. This places DINP in an intermediate permanence-vs-flexibility window. Volatility loss in activated-carbon exposure per ISO 176:2005 at 130°C for 24 h is lower for DINP than DEHP but higher than DIDP, consistent with the intermediate molecular weight and vapour-pressure curve. Published comparative data are directionally consistent but vary with isomer distribution, filler type, and stabiliser package.

At equal phr, direct drop-in substitution of DEHP with DINP in dry-blend compounding usually requires an increase of 2–4 phr DINP to maintain deformation recovery and a reduction in external lubricant of 10–20% to avoid plate-out. In plastisol processing, the room-temperature viscosity difference is amplified because DINP solvation is slower than DEHP solvation; this is addressed in the following coating-line description.

Formula decisions are also influenced by fogging behaviour. In automotive interior sheeting, DINP-based soft PVC can show fogging values by ISO 6452-1 below 2.0 mg after 16 h at 100°C, lower than DEHP-based controls in the same formulation; however, published data for this specific configuration is limited and depends on the low-volatile fraction of the product.

Spread-coating lines running 60 phr DINP in a K-value 70 paste PVC exhibit initial Brookfield viscosity at 20°C of 3,200–3,800 mPa·s at 20 rpm, measured by ASTM D1824-16; the corresponding DEHP-based plastisol typically falls near 2,500 mPa·s. Viscosity ageing at 25°C over 72 h is 1.2–1.4 times initial, and gelation tendency above 30°C storage is more pronounced than with linear phthalates. On knife-over-roll coaters operating above 80 m/min, high-shear viscosity shifts pseudoplastically and coating-head pressure increases by 8–12% relative to DEHP at equal low-shear viscosity. Plant-scale adjustments include adding 5–10 phr of a linear C9–C11 phthalate or 2–5 phr of an aliphatic diluent to restore wet-out on compact calendering lines; these adjustments sacrifice permanence and must be validated against the article specification for volatile loss and tensile retention.

Rotational moulding of DINP-plasticised vinyl shells requires careful control of particle-size distribution and pre-gelation. In production campaigns with ambient temperature above 32°C, paste viscosity can rise by 20–30% within 72 h, causing incomplete fill in thin-wall cavities. Pre-drying of calcium carbonate to ≤0.10 wt% moisture and chilled storage at ≤25°C are therefore operational boundaries; high-shear mixers should be operated below 1,000 rpm during deaeration to avoid temperature-driven viscosity build.

When DINP Replaces DEHP in Extruded Cable Jacketing

Replacement of DEHP with DINP in 105°C rated flexible PVC cable jacketing on a parallel twin-screw extruder with L/D 24:1 and barrel temperatures 150–175°C is not a drop-in substitution. The lower solvation capacity of DINP and its slightly lower plasticizing efficiency increase fusion torque by 5–10% at constant screw speed. On 60 mm twin-screw machines, die-head melt pressure can rise from 180 bar to 195–210 bar; if the screen pack area is not increased, output may drop by 3–7%. Thermal ageing per IEC 60811-401:2012 at 121°C for 168 h shows tensile strength retention above 80% only when calcium carbonate filler is held below 30 phr and the heat stabiliser level is raised by 0.5–1.0 phr relative to the DEHP control. At filler loadings above 30 phr, a property cliff-edge is observed: elongation at break falls below 150% and tensile retention falls below 75% after 168 h when dispersion is inadequate.

Low-temperature flexibility is marginally reduced; brittleness temperature per ASTM D746-14 shifts 2–4°C higher. In cold-climate cable specifications requiring a brittleness below -25°C, a blend of DINP with 10–20 phr of a linear phthalate or an approved adipate may be required. Avoid formulation with amine-based antistatic additives in open mixer environments: residual acid number above 0.03 mg KOH/g combined with humidity can accelerate ester hydrolysis and yellowing, producing die-face deposits. Pre-dry fillers and stabilisers when ambient RH exceeds 60% before dry-blending.

Regulatory distinctions from DEHP are often decisive in electrical and consumer goods. Under REACH Annex XVII Entry 52, DINP is restricted in toys and childcare articles that can be placed in the mouth at ≤0.1 wt% in the plasticised material, whereas DEHP, DBP, and BBP face broader restrictions under the same entry. DINP is not included in the four phthalates restricted in electrical and electronic equipment by RoHS Directive (EU) 2015/863, which limits DEHP, BBP, DBP, and DIBP to 0.1 wt% per homogeneous material. For food-contact applications, use must be specifically authorised under 21 CFR 178.3740 or an effective food-contact notification, and migration testing under EU Regulation 10/2011 or relevant FDA simulants is required for the finished article. Published migration data for aggressive matrices are limited; therefore, food-contact approvals must not be assumed from general-purpose grade data.

Calendered flexible film using DINP at 45 phr in K-value 67 PVC shows lower roll-sticking tendency than DEHP because of the higher molecular weight and lower vapour pressure at calender temperatures 170–185°C. Output on a 1,000 mm four-roll calender is maintained when pre-mix dry-blend temperature is limited to 90–100°C; exceeding 110°C in the hot mixer triggers premature plastication and increases power draw. Film haze per ASTM D1003-21 remains below 12% for unpigmented film when moisture is excluded and roll-slip additives are not over-dosed. Compared with diisononyl cyclohexane-1,2-dicarboxylate, DINP generally provides greater PVC solvation efficiency at equal hardness, but the non-phthalate alternative may be selected where specific non-phthalate certification is required. In low-temperature service, adipate or sebacate esters can shift brittleness temperature 15–25°C lower than DINP, but with higher volatility; the final selection is governed by the article performance specification rather than a single plasticizer property.