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| HS Code | 374861 |
| Product Name | Shandong Qilu Di-iso-nonyl Phthalate (DINP) |
| Chemical Name | Di-isononyl phthalate |
| Abbreviation | DINP |
| Cas Number | 28553-12-0 |
| Einecs Number | 249-079-5 |
| Molecular Formula | C26H42O4 |
| Molecular Weight | 418.61 g/mol |
| Appearance | Colorless to pale yellow oily liquid |
| Odor | Slight characteristic odor |
| Density | 0.97–0.98 g/cm³ at 20 °C |
| Boiling Point | >400 °C at 101.3 kPa |
| Flash Point | >200 °C closed cup |
| Viscosity | 80–120 mPa·s at 20 °C |
| Purity | ≥99.5% |
| Acid Value | ≤0.07 mg KOH/g |
| Moisture | ≤0.1% |
| Refractive Index | 1.484–1.489 at 20 °C |
| Freezing Point | < -40 °C |
| Solubility In Water | Insoluble |
| Solubility In Organic Solvents | Soluble in common organic solvents |
As an accredited Shandong Qilu Di-iso-nonyl Phthalate (DINP) factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
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Shandong Qilu di-isononyl phthalate (DINP; CAS 28553-12-0 and 68515-48-0) is a branched C9 phthalate ester with a typical ester content not less than 99.5 % and a molecular weight near 418.6 g/mol. At 20 °C the product exhibits a density of approximately 0.97 g/cm³ and a dynamic viscosity commonly reported between 68 and 85 mPa·s. The plasticizer is characterized by low volatility and high PVC solvency relative to linear C8–C10 phthalates, and its application limits are defined by polarity, migration resistance, and regulatory status in defined article categories rather than by a single processing parameter. The profiles below are separated by downstream conversion route; identical plasticizer concentration across routes produces different failure modes because of differences in heat history, filler surface area, and end-use compliance obligations.
A suspension-grade PVC resin with K-value in the range 70 to 72 is dry-blended with 45–60 phr DINP, 3–5 phr calcium/zinc stabilizer, 0.5–1.0 phr lubricant, and 5–10 phr calcined clay in a high-intensity mixer to 105–110 °C. The hot blend is then compounded in a co-rotating twin-screw extruder with an L/D ratio between 24:1 and 32:1, using a barrel temperature profile from 140 °C to 170 °C and a melt temperature below 190 °C to avoid early dehydrochlorination. During wire-line extrusion, a crosshead die is operated with a melt pressure of 90–140 bar; a sustained increase above 160 bar at constant screw speed is treated as a screen-pack plugging event caused by inadequate dispersion of filler or stabilizer agglomerates. The low-temperature flexural response is evaluated after thermal ageing because plasticizer loss and stabilizer depletion shift the brittle point more rapidly than tensile strength changes. Tensile retention is measured by IEC 60811-401 after oven ageing, while low-temperature brittleness is assessed by ISO 974 and ASTM D746. The compound is not placed in toy or child-care articles covered by REACH Annex XVII entry 52; for North American flexible cords, the finished insulation is evaluated under UL 62 and UL 1581, while European low-voltage cable constructions are manufactured to IEC 60227 series requirements. Finished articles include appliance wiring, industrial flexible cords, and light-duty power supply sheathing.
During high-shear dispersion of automotive PVC plastisols, the sequence of filler and plasticizer addition controls the onset of dilatancy in airless application systems. A typical formulation contains paste-grade PVC homopolymer with K-value 72–75, 50–80 phr DINP, 40–80 phr calcium carbonate with a median particle size of 1–3 µm, 2–6 phr calcium oxide as moisture scavenger, and 1–3 phr of a fumed silica or castor-oil thixotrope. The DINP is pre-blended with the liquid stabilizer and a portion of the filler before the remaining filler and PVC paste resin are added under a dissolver tip speed of 15–20 m/s; vacuum deaeration at about −0.090 MPa reduces entrained air that otherwise produces pinholes in gelation ovens. Application is performed through 55:1 ratio airless pumps at line pressures between 40 and 60 bar, and gelation is carried out in a forced-air oven at 180–200 °C for 20–40 min depending on metal substrate thickness. The principal compliance reference for interior emissions is VDA 278; the branched C9 ester remains in the condensable emission fraction rather than the high-volatility VOC fraction, which supports its use in underbody and wheelhouse areas where windshield fogging is evaluated by OEM material standards. The finished products are stone-chip protective coatings, weldable seam sealants, and battery tray sealants; DINP is not affected by EU ELV heavy-metal restrictions, but individual OEM specifications may impose additional emission or odour limits.
In calendered sheet flooring, the plasticizer-pigment-filler distribution is controlled by two-stage fluxing before the material enters the calender. A flooring wear-layer or foam-layer compound typically consists of suspension PVC with K-value 65–68, 28–45 phr DINP, 2–3 phr epoxidized soybean oil as co-stabilizer and secondary plasticizer, 20–60 phr calcium carbonate, and a calcium/zinc stabilizer system. The dry-blend is fluxed in a Banbury internal mixer to 155–165 °C, then transferred to a two-roll mill with a front-roll temperature 5 °C lower than the back roll to prevent sticking, and finally passed through a four-roll or five-roll calender with roll temperatures between 165 °C and 185 °C. Filler loading above approximately 45 phr reduces calender bank height stability and increases embossment recovery time; below 20 phr the sheet surface becomes subject to blocking unless a separate topcoat is applied. The finished resilient floor covering is tested for dimensional stability and wear group classification under EN 649, while tensile properties are measured by ISO 527-3. Regulatory documentation for European architectural use must confirm that the article falls outside REACH Annex XVII entry 52, and for North American channels the formulation is not intended for children's toys or child-care articles under 16 CFR 1307. End products are luxury vinyl tile, heterogeneous sheet flooring, and commercial wall base profiles.
Synthetic leather and coated fabric compounds are produced from PVC paste resin with K-value 72, 65–80 phr DINP, 2–4 phr azodicarbonamide blowing agent for foamed intermediate layers, 1–2 phr potassium/zinc stabilizer, and 5–15 phr calcium carbonate. The paste is knife-over-roll coated onto release paper or fabric at line speeds of 10–25 m/min, gelled at 190–200 °C, and then embossed or topcoated with a polyurethane skin. Because the polyurethane topcoat is sensitive to plasticizer transfer from the foamed PVC layer, compatibility under compression is evaluated using ASTM D3291; specimens aged under the prescribed compression cycle at 70 °C are inspected for exudation, and a zero-exudation result at 80 phr cannot be assumed if filler dispersion is uneven. Volatile organic emission from finished upholstery is controlled through ISO 12219-4 or automotive OEM protocols that reference VDA 277; the low vapour pressure of the C9 ester reduces early emission peaks compared with lower-molecular-weight esters, but published data for this specific configuration is limited in public databases. The finished articles are automotive seat covers, technical upholstery, and coated fabric panels for contract furniture; these are outside the toy restrictions in REACH Annex XVII entry 52.
| Segment | Controlling method | Measured parameter |
|---|---|---|
| Wire and cable insulation | IEC 60811-401 | Tensile retention after thermal ageing |
| Automotive plastisol | VDA 278 | Volatile and condensable emission fractions |
| Resilient flooring | EN 649 | Wear group classification and dimensional stability |
| Synthetic leather | ASTM D3291 | Plasticizer compatibility under compression at 70 °C |
When industrial suction hose profiles are run at line speeds above 25 m/min, the limiting variable shifts from plasticizer solvency to the stability of the calibration vacuum. A dry-blend is produced from suspension PVC K-value 67, 40–55 phr DINP, 1–2 phr acrylic processing aid, 0.2–0.5 phr stearic acid, and 3–6 phr calcium carbonate; the mixture is pre-dried at 60 °C if ambient relative humidity exceeds 60 %. Extrusion is carried out on a counter-rotating twin-screw extruder with an L/D ratio of 25:1, a die temperature of 175–195 °C, and a vacuum calibrator maintained at 20–30 °C. The melt pressure upstream of the breaker plate is normally maintained between 120 and 160 bar; surface melt fracture appears when the die land temperature falls below 170 °C at high shear rates. The finished profile or hose is not a food-contact material and is not intended for children's articles; DINP is outside the restricted phthalate list in RoHS Directive 2011/65/EU Annex II, but the supplier must still confirm that the compound does not contain the four listed ortho-phthalates above 0.1 % by weight in homogeneous material. End products are industrial gasketing, low-pressure suction hose, and extruded edge trim.
Because plasticizer loss governs field weldability and seam integrity, the formulation is compounded with suspension PVC K-value 70–72, 45–65 phr DINP, 10–30 phr calcium carbonate, 3–5 phr titanium dioxide, and a UV stabilizer package based on benzotriazole and hindered amine light stabilizer. Calendering or spread coating produces a membrane with a thickness between 1.2 and 2.4 mm; hot-air welding is conducted at nozzle temperatures of 320–420 °C with a contact pressure sufficient to form a fused seam without scorching. Seam shear strength is evaluated after heat ageing by ISO 527-3 or ASTM D638, while the product specification is written against ASTM D4434 and EN 13956. The high boiling point of DINP reduces plasticizer volatilization during thermal welding compared with C7–C8 phthalate esters, but migration into bitumen or expanded polystyrene must be assessed when the membrane is placed in direct contact with those materials. The finished membrane is installed as mechanically fastened or adhered roofing; it is outside the scope of REACH Annex XVII entry 52 and not intended for toy or child-care applications.
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CAS 28553-12-0 identifies Shandong Qilu Di-iso-nonyl Phthalate (DINP), a high-molecular-weight branched phthalate ester produced by catalytic esterification of phthalic anhydride with an isononanol stream derived from propylene oligomerization and oxo synthesis. The production sequence includes neutralization of residual acidity, water washing, vacuum stripping, and polish filtration; the finished material is a clear, essentially anhydrous oily liquid supplied as a single commodity grade designated DINP. No separate specialty model is catalogued for this product. Bulk packaging comprises tanker, ISO tank, flexitank, 200 L drums, and 1000 L IBC totes. Because the isononanol feedstock is a mixture of branched C9 alcohols, the isomer distribution is feedstock-dependent and is not routinely reported; instead, batch certificates report functional parameters governing plasticizer behavior: viscosity, density, ester content, acid value, and water content.
The typical release corridor for the bulk grade is shown in the following table. Values are not a contractual sales specification unless reproduced on the manufacturer’s Certificate of Analysis; they represent the normal range observed in bulk production. Contractual limits should be fixed through an incoming-inspection agreement, particularly when the downstream formulation contains calcium-zinc or barium-zinc heat stabilizers.
| Property | Test method | Typical acceptance value |
|---|---|---|
| Appearance | Visual inspection | Clear oily liquid, no suspended matter |
| Colour | GB/T 1664 | ≤ 30 APHA |
| Ester content | GB/T 1668 | ≥ 99.5% m/m |
| Density at 20 °C | ASTM D4052 | 0.972–0.978 g/cm³ |
| Refractive index at 25 °C | ASTM D1218 | 1.484–1.488 |
| Acid value | GB/T 1668 | ≤ 0.08 mg KOH/g |
| Water content | ASTM D6304 | ≤ 0.10% m/m |
| Dynamic viscosity at 20 °C | ASTM D445 | 78–110 mPa·s |
| Flash point, Cleveland open cup | ASTM D92 | ≥ 230 °C |
| Pour point | ASTM D97 | ≤ -45 °C |
Acid value above 0.08 mg KOH/g indicates residual acidity from incomplete neutralization or hydrolysis during storage; such acidity interferes with calcium-zinc stabilizer performance and promotes plate-out on calender rolls. Water content above 0.10% is a critical threshold for calendered film because moisture vaporizes during plastication and produces surface streaking or pinholes. Bulk storage in carbon steel or stainless steel is acceptable; nitrogen blanketing is recommended when atmospheric relative humidity exceeds 60%, and transfer lines should be fitted with desiccant breathers. Copper and zinc alloys should be avoided in transfer equipment because dissolved metal ions can catalyze PVC dehydrochlorination during subsequent processing.
DINP is not a drop-in mass-for-mass replacement for DOP in all formulations. The molar mass of DINP is approximately 418.6 g/mol, compared with 390.6 g/mol for DOP; this higher mass contributes to lower vapour pressure and lower extractability but reduces plasticizing efficiency. Published comparative formulation data indicate that 1.04–1.10 parts of DINP are required to match the softness produced by 1.00 phr of DOP. In an equal-loading substitution, the compound may show an increase of 2–4 Shore A units when hardness is measured according to ISO 868 or ASTM D2240. Torque-rheometer traces show a later fusion peak and lower equilibrium torque for DINP; on a counter-rotating twin-screw extruder with L/D 30:1, processors typically raise barrel set points by 5–10 °C or reduce feed rate to restore melt homogeneity. This adjustment is more pronounced with suspension PVC of K-value 70 or above because the crystalline regions require additional thermal energy for solvation.
| Property | Shandong Qilu DINP | DOP (DEHP) | DOTP |
|---|---|---|---|
| Molar mass | 418.6 g/mol | 390.6 g/mol | 390.6 g/mol |
| Density at 20 °C | 0.972–0.978 g/cm³ | 0.983–0.985 g/cm³ | 0.981–0.985 g/cm³ |
| Relative plasticizing efficiency vs DOP | 1.04–1.10 | 1.00 | 1.04–1.12 |
| Fusion behaviour in flexible PVC | Slower than DOP; higher torque stability | Fast fusion; lower high-shear viscosity | Slower than DINP; widest processing window |
| Volatility and migration resistance | Lower volatility than DOP; moderate oil extraction | Higher volatility; higher migration in rubber | Similar volatility to DINP; phthalate-free |
| Low-temperature flexibility | Intermediate; may require secondary plasticizer for extreme cold | Good; better than higher molecular-weight phthalates | Slightly better than DINP in some formulations |
| Regulatory status | REACH Annex XVII Entry 52 restriction; not CMR | REACH Annex XIV SVHC | No phthalate restriction |
Calendered sheet and film compounds use DINP at 40–80 phr in suspension PVC with K 65–75. Dry-blend mixing in a high-intensity mixer heats the resin to 110–120 °C; the free-flowing dry blend is then starve-fed to a vented twin-screw plastication extruder or a planetary extruder. Calender roll temperatures between 160 °C and 180 °C are common, and melt temperature should not be pushed above 190 °C unless the stabilizer package is designed for high-temperature shear. Production campaigns show that residual moisture above 0.10% in the dry blend correlates with surface defects on polished rolls; filler and resin pre-drying at 80–100 °C is therefore applied when ambient relative humidity exceeds 60%. For injection molding, DINP-based compounds produce lower low-shear viscosity than DOP compounds at equal loading, which may reduce filling pressure; however, screw recovery time and gate freeze-off may shift because the melt is less elastic and more heat-transfer-limited. Molders should verify fill and pack stages with in-mold pressure transducers rather than relying solely on melt temperature adjustment.
Plasticizer loss from a finished PVC article includes volatilization, extraction by liquids, and migration into solid contact media. DINP is selected when volatility must be lower than that of DOP; its vapour pressure at ambient temperature is approximately one to two orders of magnitude below DOP. Under ISO 176, activated-carbon volatilization at 100 °C for 24 h shows a substantially smaller mass loss for DINP than for DOP; published data for the specific Shandong Qilu grade under all test configurations are limited and should be generated on the finished compound. Soxhlet extractables determined by ISO 6427 are lower in soap water for DINP than for DOP, but hydrocarbon extraction resistance remains below that of trimellitates or polymeric adipates. In applications involving prolonged contact with styrenic or acrylic pressure-sensitive adhesives, migration testing on the laminated construction is required because the plasticizer can plasticize the adhesive interlayer and reduce peel strength.
Automotive interior skin and instrument panel compounds impose fogging limits that cannot be met by plasticizer choice alone. When DINP is used with low-volatility epoxidized soybean oil and high-purity calcium-zinc stabilizers, fogging values under ISO 6452 may fall within OEM limits; validation on the finished grained sheet is mandatory because condensate mass depends on stabilizer, processing temperature, and regrind content. The lower vapour pressure of DINP relative to DOP is an advantage, but it does not eliminate condensation from co-additives or from partial degradation of the PVC matrix. Under-hood cable and airbag cover formulations require additional heat-aging data at 120 °C or above; published data for this specific Qilu grade in these configurations is limited, so end-user qualification testing is required.
EU REACH Annex XVII Entry 52 restricts DINP and DIDP in toys and childcare articles that can be placed in the mouth at concentrations greater than 0.1% by mass of the plasticized material. DINP is not classified as a CMR substance under EU CLP and is not listed in REACH Annex XIV, which distinguishes it from DOP. In the United States, FDA 21 CFR 178.3740 provides a general regulatory reference for plasticizers in certain food-contact applications; the applicability of a specific grade must be confirmed for the article, use temperature, and food type. For the Chinese market, compliance with GB 9685-2016 or the applicable food-contact positive list must be verified before DINP is used in food-contact materials. The Shandong Qilu grade is not supplied as a food-contact plasticizer unless explicitly declared on the Certificate of Analysis. RoHS directives do not currently list DINP as a homogeneous-material restricted phthalate; however, finished-article testing may be driven by customer-specific substance lists such as IEC 62474 or brand restricted-substance standards.
For 90 °C PVC wire insulation, DINP is typically compounded at 50–60 phr with suspension PVC K 70, calcined clay or calcium carbonate filler, and a lead-free stabilizer system. Extrusion on a single-screw extruder with L/D 24:1 to 30:1 and a vacuum vent at the metering zone is used; melt temperature is controlled at 170–190 °C to maintain tensile strength and elongation at break. Heat-aging at 100 °C for 168 h according to IEC 60811 or equivalent cable standards will differentiate DINP from DOP; retention of elongation at break is generally better for DINP because of lower volatility, but the final result depends on filler loading and antioxidant package. For 105 °C continuous service, trimellitate plasticizers such as TOTM are typically specified rather than DINP.