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| HS Code | 927485 |
| Product Name | KLJ Plasticizers Kanatol 8080 Dioctyl Terephthalate (DOTP) |
| Chemical Name | Bis(2-ethylhexyl) terephthalate |
| Synonyms | Dioctyl terephthalate; DOTP; Di(2-ethylhexyl) terephthalate |
| Cas Number | 6422-86-2 |
| Einecs Number | 229-176-9 |
| Molecular Formula | C24H38O4 |
| Molecular Weight | 390.56 g/mol |
| Appearance | Clear, oily liquid |
| Color Apha | ≤50 |
| Odor | Slight ester odor |
| Density At 20 C | 0.983–0.987 g/cm³ |
| Specific Gravity At 25 C | 0.984 |
| Refractive Index At 20 C | 1.489–1.491 |
| Viscosity At 20 C | 55–60 mPa·s |
| Viscosity At 25 C | 45–55 mPa·s |
| Boiling Point | >400°C at 760 mmHg |
| Flash Point Coc | ≥230°C |
| Freezing Point | < -40°C |
| Pour Point | < -30°C |
| Acid Value | ≤0.05 mg KOH/g |
| Ester Value | 285–290 mg KOH/g |
| Moisture Content | ≤0.1% |
| Purity | ≥99.5% |
| Volatile Matter | ≤0.1% |
| Water Solubility | Insoluble in water |
| Solubility | Soluble in most organic solvents |
As an accredited KLJ Plasticizers Kanatol 8080 Dioctyl Terephthalate (DOTP) factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
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Kanatol 8080 (dioctyl terephthalate, DOTP) is added to suspension-grade PVC with K-value 65–68 at 55–70 PHR for insulation and 50–65 PHR for sheathing in 600/1000 V building wire and automotive primary cable constructions. The lower vapour pressure of DOTP relative to DEHP or DINP becomes critical in dry-cure crosshead extrusion where melt temperatures at the die exit are held between 150 °C and 170 °C; under these conditions volatile plasticiser loss in an unvented single-screw extruder with L/D 30:1 can shift Shore A hardness by 2–4 points if a lower-molecular-weight ortho-phthalate is substituted. Plasticiser volatility is screened by ASTM D1203 Method A activated-carbon loss over 24 h at 70 °C, with DOTP-containing compounds retaining lower weight loss than DEHP at equal PHR. Compound production for these insulation grades typically runs on a co-rotating twin-screw extruder at L/D 44:1 with barrel zone temperatures from 120 °C to 160 °C, followed by strand pelletising. The dry blend is prepared in a turbo mixer with a drop temperature of 125 °C and cooling to 45 °C before pelletising. Finished primary wire must demonstrate tensile strength at break of at least 12.5 MPa and elongation at break of at least 150% when tested according to IEC 60502-1 Table 17 type PVC/A on tensile specimens cut to ISO 527-2 type 1B; automotive thin-wall grades are additionally checked against ISO 6722-1 thermal overload resistance at 150 °C for 3000 h, and building wires are subject to flame propagation testing under IEC 60332-1-2 with a 60 s vertical flame application. Regulatory documentation for these constructions routinely cites REACH Regulation (EC) No 1907/2006 Annex XVII Entry 51, which restricts DEHP, DBP, BBP, and DIBP, and Entry 52, which restricts DINP, DIDP, and DNOP in certain toys and childcare articles; DOTP is not listed in either entry. EU RoHS 2011/65/EU applies to electrical and electronic equipment and does not prohibit DOTP. The terminal article range includes single-core building wire sizes from 0.5 mm² to 6.0 mm², flexible cords under UL 62, automotive ISO primary wire, appliance lead wire, and internal wiring harnesses for white goods. The critical processing constraint is not initial fusion but longer-term thermal ageing: compounds held above 180 °C for residence times beyond 90 s during crosshead extrusion may initiate dehydrochlorination in stagnation zones, so Ca-Zn or organic phosphite stabiliser packages are adjusted upward when DOTP addition exceeds 65 PHR. No universal extrusion profile can be declared without converter-side validation against the final cable standard.
Automotive instrument panel skins and door panel coverstocks are converted from PVC plastisol in which Kanatol 8080 is charged at 70–90 PHR per 100 PHR of paste resin, with viscosity reduced by aliphatic diluents from 10 PHR to 20 PHR before vacuum deaeration at 5–10 kPa. The plastisol is cast onto release paper or directly into a slush-mold nickel shell heated to 220–250 °C; gelation dwell times of 40–90 s produce skins with Shore A hardness 60–75 and surface grain depth determined by post-cooling embossing. Low-VOC and fogging requirements are evaluated under VDA 278 thermodesorption at 90 °C for VOC and 120 °C for SVOC, and fogging condensate is tested by DIN 75201-B or ISO 6452. For a two-layer interior trim laminate, the compact skin layer containing DOTP at 70 PHR is fused to a polypropylene foam backing at 120–150 °C using a hot-plate press at 0.4–0.6 MPa; delamination strength after ageing is checked according to DIN 53357-A. Unlike DEHP-based plastisols, DOTP-containing skins can maintain fogging condensate below the 2.0 mg limit commonly filed in OEM material specifications, but the gelation oven profile must be raised by 5–10 °C when switching from a high-ortho-phthalate formula to avoid under-gelled resin particles that appear as surface pitting. End products produced through this route include instrument panel skins, door insert covers, console armrest skins, and interior coated fabrics for headliners. Process control focuses on plastisol viscosity stability over 48 h at 25 °C and deaeration efficiency, because incomplete air release is the primary cause of pinhole defects on grained surfaces; converter data from three-shift automotive lines indicate that viscosity rise above 1500 mPa·s after 24 h is often correlated with knife-over-roll coating streaks, though exact viscosity limits are typically defined in closed OEM material specifications.
Blood storage containers and extracorporeal tubing produced from medical-grade PVC require plasticiser systems that survive steam autoclave cycles at 121 °C for 30 min without generating tacky surfaces or leaching low-molecular-weight species into stored plasma. Kanatol 8080 is let down into PVC of K-value 70–75 at 60–80 PHR for film and 50–70 PHR for tubing; the resulting Shore A hardness falls in the 70–85 range. Compatibility and migration under simulated contact are assessed under ISO 3826:2013 for plastics collapsible containers for blood and blood components, with extractables profiling performed according to ISO 10993-1 and cytotoxic response screened by ISO 10993-5. Film conversion uses a counter-rotating twin-screw extruder with L/D 24:1 at melt temperatures from 140 °C to 160 °C, followed by flat-die film casting at thickness 0.35–0.50 mm; bags are then sealed by high-frequency welding at 27.12 MHz and sterilised. Unlike DEHP, which has documented extraction into blood and interaction with red blood cell membranes, DOTP shows reduced migration under extraction but must still be evaluated for each blood bag formulation because the plasticizer migrates into lipids over storage periods exceeding 21 days; no universally applicable extractables profile can be assumed across all blood bag formats and lipid contents. Regulatory submissions for medical devices reference ISO 10993 biological evaluation and, where US FDA clearance is being assembled, the compounder may reference 21 CFR 178.3740 for plasticizer inventory; final article clearance under the applicable medical device route remains a converter-specific demonstration. Converters are also required to verify compliance with REACH Regulation (EC) No 1907/2006 Annex XVII Entry 51 and EU Medical Device Regulation (EU) 2017/745 general safety and performance requirements. Terminal product types include red blood cell storage bags, platelet containers, anaesthesia breathing circuit tubing, and peristaltic pump tubes. The critical boundary is not PVC fusion but migration kinetics: plasticizer exudation increases when the compound is exposed to ethylene oxide sterilization gas at residual moisture above 60% RH, because hydrolytic cleavage of the ester is favoured at high humidity; incoming resin and filler moisture should be dried to below 0.05% before compounding to avoid surface haze after steam sterilisation.
In resilient flooring, Kanatol 8080 is incorporated as the primary plasticizer in compacted PVC wear layers where dimensional stability after exposure to 80 °C for 6 h is tested according to ISO 23999, and thermal expansion under 80 °C is controlled for interlocking LVT products. Addition ratios are lower than in cable or medical film: wear layers are typically formulated with 30–50 PHR DOTP on 100 PHR suspension PVC, while printed decorative layers and backing layers use 40–60 PHR to retain calender pick-up without excessive surface tack. The production sequence begins in a Banbury internal mixer at 140–160 °C, continues onto a two-roll mill, and then passes through a four-roll inverted-L calender at 160–180 °C to form a sheet of 0.5–2.0 mm. The calendered sheet is laminated to a PVC core layer in a multi-daylight hot press at 150–180 °C and 20–40 bar, then annealed at 70 °C for 24 h before UV-cured polyurethane topcoat application at 10–20 g/m². Compliance for residential and commercial floor coverings is documented under EN ISO 10582 and EN ISO 26986 for wear layer thickness and indentation resistance; indoor emissions are screened by ISO 16000-6 after 28 days in chamber testing. DOTP’s lower weight loss during calendering reduces roll plate-out compared with DEHP at equivalent PHR, but the compound’s melt viscosity is slightly higher, so calendering bowl temperatures should not drop below 160 °C or the sheet will exhibit marginal bank rotation and surface roughness. End products include luxury vinyl tile, stone plastic composite flooring with resilient LVT top layers, commercial resilient sheet flooring, and wall base profiles. The main processing boundary is the embossing temperature window: when DOTP is used at 60 PHR in the wear layer, post-embossing recovery is less than 1.5% only if the surface is cooled below 40 °C before leaving the embossing nip; otherwise grain depth relaxation occurs within 24 h.
Rotomoulded vinyl toys and childcare articles are a regulatory-sensitive downstream for Kanatol 8080 because the substance is not covered by REACH Annex XVII Entry 51 restrictions on DEHP, DBP, BBP, and DIBP, while DINP remains restricted under Entry 52 when the toy can be placed in the mouth. In PVC plastisol for soft doll bodies and squeeze toys, addition levels range from 50 PHR to 80 PHR per 100 PHR paste resin, depending on target Shore A hardness 55–70. Processing uses open-mould rotational casting or slush casting; the metal mould is heated to 190–220 °C, filled with plastisol, rotated on two axes at 6–12 rpm, and cooled to 40 °C before demoulding. The documented processing conflict is gelation: DOTP-containing plastisol generally requires a mould-surface temperature 5–10 °C higher than an equivalent DINP formula to achieve complete fusion. When this adjustment is ignored, the inner surface remains under-gelled and organic compounds can migrate during EN 71-10 sample preparation and EN 71-11 analysis, causing a fail under EN 71-9 category-specific migration limits; additionally, under-cured parts exhibit plasticizer exudation and surface tack quantified as blocking force above 1.0 N after 24 h under 0.5 kPa. Compliance documentation should cite EN 71-1 mechanical requirements, EN 71-3 migration of certain elements, and EN 71-9/10/11 organic chemical compounds where applicable. The operational boundary for molder conversion is that DOTP provides slightly lower plasticising efficiency than DINP; adding 5–10 PHR higher DOTP is often necessary to maintain identical Shore A hardness, but this can push total plasticizer above 85 PHR, at which point embossing definition and rotational mould release degrade unless a silicone release agent is applied. Terminal product types include soft vinyl doll heads, squeeze-activated bath toys, ball-shaped rattles, and vinyl book covers for young children. Final articles must be verified under the notified-body test regime specified by the Toy Safety Directive.
Because DOTP exhibits lower vapour pressure than ortho-phthalate plasticizers at 180 °C, synthetic leather foam layers made from Kanatol 8080 are used for shoe uppers and furniture upholstery where emissions and long-term flex crack resistance are controlled. The plastisol for the foamed interlayer contains 60–85 PHR DOTP on 100 PHR PVC paste resin, 3–5 PHR azodicarbonamide blowing agent, and a kicker such as zinc oxide at 1–2 PHR; the compact top coat is formulated at 50–70 PHR DOTP to maintain abrasion resistance. Coating is performed by release-paper transfer on a knife-over-roll line running at 12–45 m/min; gelation tunnels are set to 140–190 °C in six zones, with the final zone at 210–220 °C triggering foaming and collapse to the final thickness before lamination to polyester knitted scrim. After cooling to 30 °C, the release paper is stripped and the surface is embossed on a heated grain roller at 120–150 °C. Compliance for upholstery uses ISO 105-C06 colour fastness to domestic and commercial laundering, ISO 12947-2 abrasion resistance by Martindale at 50,000 cycles, and ISO 16000-6 indoor emission testing; footwear material is additionally checked for flexing endurance under ISO 5402-2 after 50,000 cycles dry and 10,000 cycles wet. End product types include breathable microporous synthetic leather for athletic footwear, coated fabric for handbags, contract-grade upholstery, and automotive seating topcoats where OEM VOC requirements are met through low-VOC plasticizer selection. The main equipment boundary is the final foaming zone: if the web temperature exceeds 220 °C, excessive blowing agent decomposition creates cell coalescence and delamination at the fabric interface, while below 200 °C the foam layer lacks uniform cell structure and fails flex endurance; DOTP viscosity stability in the coating trough over an 8 h shift must be monitored with a Brookfield RV spindle 6 at 20 rpm to maintain knife-over-roll coat weight within ±3%.
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KLJ Plasticizers supplies KANATOL 8080 as a primary non-ortho-phthalate plasticizer for flexible poly(vinyl chloride) and PVC plastisols. Chemically, the product is bis(2-ethylhexyl) terephthalate, CAS 6422-86-2, with a molar mass of 390.56 g/mol. It is handled as a high-boiling ester plasticizer in flexible compounds at 40–80 phr and in plastisols at 60–100 phr, depending on the target hardness, low-temperature flexibility, and migration resistance. Unlike DEHP, the ester groups occupy the para positions of the aromatic ring; the molecule therefore falls outside the ortho-phthalate restrictions of REACH Annex XVII Entries 51 and 52. Industrial deployments include cable insulation, automotive interior skins, vinyl flooring, artificial leather, and calendered sheet. The product is selected where a non-phthalate regulatory statement, reduced volatility, and lower plastisol viscosity are required in the finished article.
Because the para-isomer solvates suspension PVC less aggressively than DEHP, hot-mix absorption can require a final dry-blend temperature at the higher end of the range used for general-purpose plasticizers. On a high-speed mixer with a total batch size of 250–400 kg, a dry blend containing 50–70 phr KANATOL 8080 is typically discharged at 115–125°C and transferred immediately to a cooling mixer until the blend temperature drops below 45°C. Published torque-rheometer data for this specific configuration is limited, but the observed gelation plateau in plastisol and dry-blend processing commonly shifts upward by 4–8°C relative to equivalent DEHP formulations. The elevated discharge temperature should not be generated by excessive shear alone; high-speed mixer tip speeds above 25 m/s can produce local thermal gradients that accelerate PVC dehydrochlorination and acid value drift. Operators typically add the plasticizer in two stages: 60% of the total plasticizer is introduced after the resin reaches 80°C, and the remaining 40% is introduced after 100°C. This staged addition reduces peak torque and improves dry blend uniformity for free-flowing storage in silos. For total mixing times beyond 30 minutes, a nitrogen purge on the mixer lid is recommended to limit moisture uptake from ambient air.
On a co-rotating twin-screw extruder with 25:1 to 30:1 L/D ratio and vacuum venting at 0.07–0.08 MPa, a 70 phr DOTP/PVC insulation compound is usually processed with barrel set points between 145°C in the feed zone and 165°C at the die. The screw layout includes two shearing zones with kneading blocks at 30° and 60° stagger angles, followed by back-pressure elements before the vent. If the plasticizer is injected downstream rather than at the feed throat, unabsorbed liquid can flood the vent and cause output surging; therefore KANATOL 8080 is preferentially metered into the feed throat together with the resin and stabilizer stream. Residual moisture above 0.05% in the plasticizer is associated with surface roughness and microvoids in the extrudate. A gravimetric feeder with repeatability of ±0.5% on the plasticizer stream is sufficient for maintaining hardness within ±2 Shore A points in continuous runs. On a 90 mm single-screw extruder operating at 55–75 rpm, head pressure at 70 phr loading generally falls between 120 bar and 180 bar; published data for other equipment sizes is limited.
The values below represent typical release data for DOTP grades in this product class; a certificate of analysis for a specific production lot should be requested from the manufacturer. The test methods are standard plasticizer and hydrocarbon tests used to control acid value, moisture, colour, and viscosity.
| Parameter | Typical Value/Range | Test Method |
|---|---|---|
| Density at 20°C | 0.983–0.985 g/cm³ | ASTM D4052-22 |
| Dynamic viscosity at 20°C | 60–66 mPa·s | ASTM D445-21 |
| Acid value | ≤ 0.02 mg KOH/g | ASTM D1045-19 |
| Moisture | ≤ 0.05% | ASTM D1364-02 |
| Ester content | ≥ 99.0% | ASTM D1045-19 |
| Colour APHA | ≤ 25 | ASTM D1209-14 |
| Refractive index at 25°C | 1.488–1.490 | ASTM D1218-21 |
| Flash point, Cleveland open cup | ≥ 238°C | ASTM D92-18 |
In plastisol processing, KANATOL 8080 produces a lower initial Brookfield viscosity than DINP at equal loading, particularly at low shear. The viscosity difference is measurable on a Brookfield RVT rheometer using spindle 4 at 20 rpm and 25°C; typical plastisols with 60 phr plasticizer and K-value 67 paste resin range from 1800 mPa·s to 3500 mPa·s, depending on filler, emulsifier content, and resin particle size distribution. Published comparative data for this specific configuration is limited, but the viscosity trend is reproducible across multiple paste-resin suppliers. In chemically blown vinyl flooring, the lower solvating power of DOTP can delay gelation. Processing lines compensate by raising the gel-section oven temperature by 3–7°C or by adding a faster-solvating secondary plasticizer where the end-use regulatory profile permits. The elevated gelation temperature demands uniform thermal stabilizer distribution in the foam layer; otherwise cell coalescence and partial foam collapse can occur before full expansion. A tin stabilizer package at 1.5–2.5 phr or a Ca-Zn stabilizer at 4–6 phr is typically used depending on volatile organic compound limits and end-use extraction requirements. Tensile and elongation testing of the expanded sheet after aging for 7 days at 70°C is commonly performed according to ASTM D638-14 or ISO 37:2017, depending on the regional specification framework.
Flexible PVC insulation compounds formulated with KANATOL 8080 can maintain volume resistivity above 1×10^12 Ω·cm after 7 days water immersion at 70°C when measured by IEC 60093 or ASTM D257. This property is sensitive to ionic impurities, stabilizer residues, and residual moisture. A production-scale fault observed on a 90 mm single-screw insulation line is a progressive drop in resistivity from 1.5×10^12 Ω·cm to 7×10^11 Ω·cm over a 6-hour run when ambient relative humidity exceeds 60% and the plasticizer is held in open day tanks. The corrective action is to install a nitrogen-blanketed storage tank and maintain plasticizer moisture below 0.05% by ASTM D1364-02. The compound is cooled to below 45°C before granulation; otherwise plasticizer exudation at silo temperatures above 50°C can create uneven plasticizer distribution in subsequent extrusion runs. In contact with polycarbonate, DOTP can induce environmental stress cracking; wetting or migration contact between DOTP-plasticised PVC and polycarbonate glazing should be prevented. For bedding compounds under high-voltage cables, manufacturers also check DC volume resistivity at 23°C and 50% relative humidity after conditioning for 24 h; published data for specific cable types is limited until qualification testing is completed.
Automotive interior skin and dashboard compounds select DOTP because fogging condensate mass is typically below 2 mg under ISO 6452:2021 after 16 h at 100°C, provided the stabilizer and processing aid package are matched to low-volatile additive requirements. The plasticizer contributes no ortho-phthalate signal in extractable-content screening for REACH-relevant substances and is compatible with Ca-Zn stabilizer systems used in low-emission PVC grades. In calender lines producing 0.8–1.2 mm unsupported sheet, the processing window for KANATOL 8080 is wider than for short-chain phthalates because the terephthalate ester has a flash point above 238°C and low vapour pressure at calender temperatures of 180–200°C. Roll release behaviour is governed by the complete lubricant package; the plasticizer alone cannot eliminate plate-out. If gloss reduction is required after thermoforming, a matting agent is added rather than relying on plasticizer incompatibility.
KANATOL 8080 is not a universal drop-in for all DEHP applications. Although DOTP lies outside the ortho-phthalate restrictions in REACH Annex XVII, food-contact and medical devices require separate positive-list verification. For food-contact materials in the European Union, Commission Regulation (EU) No 10/2011 must be checked for the specific ester and final migration limit; published data for this specific product and application is limited. In the United States, relevant sections of 21 CFR must be confirmed for the intended use, because generic DOTP clearance cannot be assumed. For medical-grade PVC, ISO 10993-1:2018 biological risk assessment and material characterization are required, and the manufacturer’s regulatory support statement should be requested for each product code. The operational boundary is therefore limited to applications where written supplier confirmation and finished-article testing verify the relevant migration or medical device requirements.
Comparative property trends between KANATOL 8080, DEHP, and DINP are summarized below for equal plasticizer loading in flexible PVC. The trends are based on publicly available industrial data for DOTP and ortho-phthalate plasticizers; batch-specific values require qualification on the target formulation.
| Property/Tendency | KANATOL 8080 DOTP | DEHP | DINP |
|---|---|---|---|
| Ester configuration | para-terephthalate | ortho-phthalate | ortho-phthalate |
| Molar mass | 390.56 g/mol | 390.56 g/mol | 418.62 g/mol |
| Plastisol viscosity at equal loading | Lower than DINP; moderately lower than DEHP | Reference | Higher |
| Gelation temperature in suspension PVC | Higher than DEHP by ca. 4–8°C | Reference | Similar to slightly lower than DEHP |
| Volatility from PVC at elevated temperature | Lower than DEHP under identical aging | Reference | Lower than DEHP |
| REACH Annex XVII Entry 51/52 | Not listed | Restricted under Entry 51 | Restricted under Entry 52 |