| HS Code | 423304 |
| Productname | API Megol AM SEBS-Comp. DP2339 |
| Brand | Megol |
| Manufacturer | API Applicazioni Plastiche Industriali S.p.A. |
| Materialfamily | Thermoplastic Elastomer (TPE) |
| Polymerbase | SEBS |
| Compoundtype | SEBS compound |
| Series | AM |
| Grade | DP2339 |
| Adhesionmodified | Yes |
| Productstatus | Development product |
| Supplyform | Pellets |
As an accredited API Megol AM SEBS-Comp. DP2339 factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | API Megol AM SEBS-Comp. DP2339 is supplied in 25 kg net, polyethylene-lined fiber drums, securely sealed and fully labeled for chemical transport. |
| Container Loading (20′ FCL) | 20′ FCL container loaded with API Megol AM SEBS-Comp. DP2339, palletized, secured, and sealed for export shipment. |
| Shipping | API Megol AM SEBS-Comp. DP2339 is typically shipped as a non-hazardous thermoplastic elastomer compound in sealed, labeled packaging. Protect from moisture, heat, and direct sunlight; keep containers closed and avoid damage. Transport at ambient temperature per local regulations and the supplier’s SDS. |
| Storage | Store API Megol AM SEBS-Comp. DP2339 in a cool, dry, well-ventilated area away from direct sunlight, heat, sparks, and open flames. Keep containers tightly closed, upright, clearly labeled, and protected from moisture and contamination. Avoid extreme temperatures. Follow the manufacturer’s SDS and local regulations, and use first-in, first-out stock rotation. |
| Shelf Life | Shelf life is 24 months from manufacture when stored unopened in original packaging, dry, at 15–25°C, away from direct sunlight. |
On automotive interior overmoulding lines, DP2339 is fed as received at 100 phr into a conditioned hopper where residual moisture is held below 0.05% by weight. Processing is performed on horizontal injection moulding machines with clamp force ratings between 800 kN and 2500 kN, using a general-purpose screw with L/D ratio 20:1 to 22:1 and compression ratio 2.5:1 to 3.0:1. The melt is processed with a barrel profile from 160°C in the feed zone to 200°C at the metering zone and a nozzle temperature of 190–210°C; mould surface temperature is controlled between 30°C and 45°C. During overmoulding onto polypropylene or PP/EPDM substrates, bond-line surface temperature is maintained above 120°C for the first 2–4 s of filling to promote interdiffusion and cohesive failure in peel testing. Injection velocity is profiled to prevent jetting, holding pressure is set at 40–60% of peak injection pressure, and hold time is adjusted from 3 s to 8 s depending on wall thickness. Pre-drying for 2–3 h at 70°C is required when ambient relative humidity exceeds 60%; water in the SEBS mid-block otherwise generates surface splay and reduces overmould adhesion. Amine-based lubricants are not used in this application because they accelerate discoloration and loss of bond strength. When a harder tactile surface is required, 5–15 wt% polypropylene homopolymer with an ISO 1133-1:2022 MFR of 25 g/10 min may be dry-blended, but this raises Shore A hardness and lowers peel strength. Compliance for automotive interior air quality is verified by VDA 278:2011 thermodesorption analysis for VOC and FOG emissions, VDA 270:1992 for odour severity with OEM acceptance typically between grade 1 and grade 3, and FMVSS 302 / ISO 3795:1989 for horizontal burn rate. Final articles are screened against REACH Regulation (EC) No 1907/2006 SVHC candidate list and end-of-life vehicle directive 2000/53/EC. Terminal products in this segment include instrument panel midranges, door card armrests, centre console side bolsters, HVAC scroll-wheel grips, and soft-touch insert mouldings on steering column shrouds. Batch-to-batch variation on production lines has been observed when pellet moisture is uncontrolled; melt residence times above 10 min at 200°C increase surface tack and gel content, so start-up and shutdown purging with polypropylene is used to prevent carbonised residue.
Because medical components are exposed to aqueous extraction and terminal sterilisation, DP2339 is supplied without primary plasticiser and is charged at 100 phr; colour masterbatch, where permitted, is added at 1–3 phr, while secondary plasticiser and process-oil let-down are excluded because low-molecular-weight fractions would fail extractables screening. Extrusion of tubing and profiles is performed on polished single-screw extruders with L/D 24:1 to 30:1, barrier screw compression ratio 2.5:1, and a 60/80/100 mesh screen pack to retain additive agglomerates. Melt temperature is maintained between 180°C and 200°C at the die adapter; temperatures above 205°C accelerate oxidative degradation of the styrenic end-blocks and produce yellow index shift. The extrudate is sized in a vacuum calibrator and cooled in a chilled-water bath at 10–15°C, with downstream puller-controlled line shrinkage of 0.5–1.5%. Injection moulding of stoppers and gaskets uses cold-runner tools rather than hot runners because prolonged hot-runner residence generates gels and intermittent flow marks. Sterilisation qualification includes gamma irradiation up to 50 kGy, ethylene oxide cycles, and autoclave exposure at 121°C for 30 min or 134°C for 5 min; repeated autoclave cycling at 134°C increases compression set, and published data for this specific configuration is limited above 20 cycles. Compliance is evaluated by ISO 10993-5:2009 L929 cell extraction at 37±1°C for 24±2 h, ISO 10993-10:2010 sensitisation and irritation protocols, USP <87> biological reactivity, USP <88> Class VI extraction at 50°C, 70°C, and 121°C, FDA 21 CFR 177.2600 for repeated-use rubber articles, and EU MDR 2017/745 documentation for finished components entering the European market. Terminal products include syringe plunger tip seals, IV line connectors, respiratory mask cushions, infusion pump cassettes, enteral nutrition container gaskets, and dialysis machine gaskets. This material is not specified for prolonged contact with lipid-rich drug vehicles without finished-component migration data. Residual PVC decomposition products in processing equipment cause SEBS mid-block degradation; a two-stage purge with PMMA followed by polypropylene is used when the machine has previously run PVC.
| Standard | Test method | Condition | Required output |
|---|---|---|---|
| ISO 10993-5:2009 | L929 cell culture | 37±1°C / 24±2 h extract | No cytotoxicity |
| ISO 10993-10:2010 | Guinea pig maximisation | Polar and non-polar extracts | No sensitisation |
| USP <88> Class VI | Systemic injection and implantation | 50°C, 70°C, 121°C extracts | No systemic toxicity |
| FDA 21 CFR 177.2600 | Total extractives in water and n-heptane | Reflux | CFR migration limits |
| ISO 815-1:2019 | Compression set after 72 h | 23°C and 70°C | Dimensional recovery |
Closure seal applications for carbonated beverage and hot-fill food containers require liners with low compression set after pasteurisation and minimal organoleptic contribution. DP2339 is dosed at 100 phr in compression moulding lines; where lower torque release is needed, slip agent masterbatch is added at 1–2 phr before feeding, but the slip agent must be selected after overall migration testing under EU 10/2011/EC because migration of processing aids is a dominant compliance failure mode. Compression moulding uses platen temperatures of 170–190°C, specific pressure of 5–12 MPa on the projected liner area, and cycles of 15–30 s per millimetre of liner thickness. At ambient RH below 50%, pre-drying is not required; above that threshold, 70°C for 1–2 h prevents steam blisters in the liner centre. Compliance is determined by EU Regulation 10/2011/EC as amended, with overall migration limit of 10 mg/dm², and by FDA 21 CFR 177.1810 for styrene block polymers, with specific migration testing according to EN 1186-1:2002 and subsequent parts. Terminal products include PET bottle cap liners, crown cork liners, lug cap gaskets for hot-fill jars, tamper-evident band liners for sauces, and cap seals for UHT milk. Direct contact with free oils or alcohol concentrations above the assigned food simulant categories in EU 10/2011/EC is not specified unless additional migration testing establishes compliance under the intended use conditions.
For window and door weatherseal profiles, DP2339 is run at 100 phr as supplied, with a talc-filled polypropylene rigid core metered separately at the coextrusion die when profile retention in the frame groove is required. The TPE melt is processed with barrel profile 150–185°C, adapter and die temperature 180–195°C, and gear pump mass-flow stability maintained within ±1%. A single-screw extruder with L/D 24:1 and Maddock mixing section is used; screw speed is limited to 40–70 rpm because higher screw speed generates shear heating, lowers melt viscosity, and causes edge tear in calibration. Vacuum calibration is run at 0.5–0.8 bar negative pressure with water temperature 15–20°C. Dimensional recovery after compression is evaluated by ISO 815-1:2019 at 70°C for 72 h, and finished profiles are classified under EN 12365-1:2003 for gasket and weatherstripping performance. UV weathering is tested according to ISO 4892-2:2013 method A cycles with evaluation of surface cracking. Terminal products include window glazing channel gaskets, door bottom seals, curtain wall expansion joint gaskets, skylight compression seals, and edge protection profiles for flat glass. Continuous contact with hot bitumen or solvent-borne sealants causes surface softening and loss of grip in the frame groove and is not recommended.
For flexible cable jackets processed by pressure extrusion, DP2339 is fed at 100 phr on single-screw extruders with L/D 25:1 to 30:1 and screw compression ratio 2.0:1 to 2.5:1. For halogen-free flame-retardant constructions, a metal-hydrate masterbatch may be incorporated at 30–60 phr by the cable compounder, but this addition lowers tensile strength and elongation at break, so final formulations must be screened according to IEC 60811-501:2012 thermal ageing at 100°C for 168 h. Melt temperature is maintained between 160°C and 195°C, and the melt passes through a 60/80 mesh breaker plate before entering the pressure-type tubing die. A hot-water trough at 60–80°C followed by air cooling reduces rapid crystal-phase contraction and surface tack. Finished flexible cords for appliance connection, robot drag chains, and EV charging connector assemblies are tested under IEC 60332-1-2:2004 for flame spread, IEC 60754-1:2011 for halogen acid gas release, and IEC 60811-501:2012 for tensile retention after ageing; since the jacket is thermoplastic and not crosslinked, hot-set testing under IEC 60811-2-1 is not applied. Terminal products include flexible appliance cord jackets, EV charging cable outer jackets, data-center power cord sleeves, and medical cart power cable sheathing. The compound is not a substitute for crosslinked XLPE primary insulation where conductor temperature ratings exceed 125°C; published data for this specific configuration is limited above that threshold.
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API Megol AM SEBS-Comp. DP2339 is identified as a hydrogenated styrenic block copolymer compound supplied in the Megol AM range. The matrix polymer is styrene-ethylene/butylene-styrene (SEBS), commonly indexed under CAS 66070-58-4, although the commercial compound may contain paraffinic process oil, polyolefin modifiers, mineral filler, stabiliser packages, and pigment dispersions. The DP2339 formulation code is manufacturer-specific and is not defined by an ISO or ASTM material standard. In contrast to unsaturated SBS grades, hydrogenation of the polybutadiene mid-block to an ethylene/butylene sequence eliminates most double bonds and yields a saturated elastomer segment with improved resistance to ozone attack and UV-initiated chain scission. This structural distinction places the material in the same chemical family as other hydrogenated styrenic thermoplastic elastomers but does not define the final Shore hardness, melt-mass flow rate, or tensile response of the compounded grade.
Compounded SEBS systems are two-phase materials in which styrene end-blocks form glassy domains that serve as physical crosslinks below the styrene glass transition temperature of approximately 95 °C. The ethylene/butylene mid-block produces a low-modulus elastomer phase with a serviceable flexibility window that depends on the pour point and loading of any paraffinic oil. The balance among styrene content, oil extension, and mineral filler controls hardness measured according to ISO 868 or ASTM D2240. Commercial SEBS compounds typically report density values between 0.89 g/cm³ and 1.30 g/cm³ when tested to ISO 1183-1; the certified value for DP2339 must be taken from the API batch certificate. Melt-mass flow rate is determined by ISO 1133-1:2022, with common test conditions of 190 °C or 230 °C and 2.16 kg or 5 kg. In oil-extended grades, the melt-mass flow rate can shift substantially because the process oil acts as an internal lubricant and reduces apparent viscosity. The AM designation is manufacturer-specific and should not be interpreted as a composition or performance claim without API documentation.
| Property | Standard method | Published range for compounded SEBS | DP2339 verification |
|---|---|---|---|
| Hardness | ISO 868 / ASTM D2240 | Shore A 5–95 | Grade-specific |
| Density | ISO 1183-1 | 0.89–1.30 g/cm³ | Grade-specific |
| Tensile strength at break | ISO 37 / ASTM D412 | 2–25 MPa | Grade-specific |
| Elongation at break | ISO 37 / ASTM D412 | 200–900 % | Grade-specific |
| Melt-mass flow rate | ISO 1133-1:2022 | 1–60 g/10 min | Grade-specific |
| Compression set | ISO 815-1 / ASTM D395 | 15–75 % after 22 h at 70 °C | Grade-specific |
On injection moulding lines producing soft-touch automotive interior and personal care components, compounded SEBS grades are typically dried at 60 °C to 80 °C for 2 h to 4 h only when surface condensation has raised moisture content above 0.1 wt%. Barrel profile settings for medium-hardness SEBS systems frequently range from 170 °C to 230 °C, with the nozzle zone held 5 °C to 10 °C below the metering zone to reduce stringing and drool. Mould temperatures between 20 °C and 50 °C are common; higher mould temperatures improve replication and knit-line strength, but cycle time increases. For extruded profiles or tubing, single-screw equipment with a shallow-compression screw and breaker plate is used. Melt temperatures above 230 °C can initiate gel formation if the stabiliser package is depleted or if residence time is prolonged. DP2339-specific processing limits should be obtained from API; published data for this specific configuration is limited.
For hydrogenated styrenic block copolymers, melt stability is governed by the combined effects of shear heating, residence time, and dissolved oxygen. The non-Newtonian shear-thinning behaviour of SEBS compounds means that apparent viscosity at 1000 s⁻¹ can be less than 50 % of the value measured at 100 s⁻¹ on a capillary rheometer. This shear sensitivity supports thin-wall filling but demands controlled gate sizing because excessive shear at the gate can generate local melt temperatures far above the barrel set point. Production-scale injection moulding reports for compounded SEBS grades in multi-cavity tools indicate that shot-weight inconsistency frequently originates from insufficient back pressure rather than from a shift in melt temperature; a back pressure of 3 MPa to 8 MPa and screw rotation speeds below 150 min−1 are typically applied to homogenise the melt without excessive shear heating. Free paraffinic oil lowers melt viscosity but increases screw slip when the feed throat is too warm. Venting depth is critical because oil volatilisation can generate trapped gas and burn marks in unvented cavities. The operator should verify mould venting and gate freeze-off against the rheological data for DP2339.
Thermal degradation of SEBS compounds under melt processing proceeds through hydrogen abstraction followed by chain scission and crosslinking. Although the saturated ethylene/butylene mid-block is more stable than the unsaturated butadiene mid-block of SBS, exposure to melt temperatures above 240 °C can generate gel particles and a measurable rise in melt viscosity. Hindered phenol and phosphite stabiliser packages are standard in compounded SEBS grades; their depletion during repeated recycling reduces oxidative induction time as measured by differential scanning calorimetry. Under ISO 4892-2 xenon-arc exposure, SEBS compounds generally show lower Delta b and greater retention of elongation at break than SBS or natural rubber systems of similar hardness, although light-coloured grades can still yellow when phenolic antioxidants migrate to the surface. The service temperature window is limited at the upper end by the styrene domain glass transition and at the lower end by mid-block stiffening; continuous use above 90 °C is not recommended for soft SEBS grades because compression set increases and recovery declines. Published data for the specific DP2339 stabiliser system is limited, so thermal endurance must be verified on moulded specimens.
Application assignments for DP2339 should be derived from the API technical data sheet, but the general class of adhesion-modified SEBS compounds is used in two-shot overmoulded grips, seals, gaskets, soft-touch automotive interior surfaces, personal care items, and ergonomic consumer electronics enclosures. On polypropylene substrates, adhesion is typically improved by maintaining a mould surface temperature above 40 °C and by selecting a substrate grade with a polar modification when the substrate is an engineering thermoplastic. Production failure modes include delamination at the overmoulded interface when the substrate surface temperature drops below the melt’s wetting threshold, and gloss variation when the mould surface temperature is not controlled within ±5 °C. Knit-line tensile strength can be assessed by ISO 527-2 specimens cut perpendicular to the knit line. In extrusion, SEBS compounds may show higher die swell than equivalent Shore hardness TPU, requiring adjustments in drawdown ratio and die land length. Published data for DP2339 in specific end-use geometries is limited; qualification under the intended application standards is mandatory.
When plasticised PVC is replaced by SEBS-based compounds, the removal of phthalate plasticiser is accompanied by changes in low-temperature flexibility, oil resistance, and compression set. SEBS systems can retain flexibility at −40 °C if the paraffinic oil pour point is sufficiently low, whereas plasticised PVC may stiffen below −10 °C depending on plasticiser type. However, SEBS compounds are less resistant to non-polar solvents and mineral oil than TPU or copolyester elastomers; immersion testing under ASTM D471 with IRM 903 oil generally produces higher volume swell in SEBS than in TPU. Compared with liquid silicone rubber, SEBS compounds offer lower tooling cost and shorter cycle times but exhibit higher compression set and lower continuous-use temperature. Against thermoplastic vulcanisates, SEBS compounds may provide softer feel and better colour stability but usually have lower flex-fatigue resistance. The DP2339 grade should be compared using a common test matrix that includes hardness, density, tensile stress at 100 % elongation, compression set after 22 h at 70 °C, and dynamic mechanical analysis.
| Attribute | Compounded SEBS | TPU | TPV | Silicone LSR |
|---|---|---|---|---|
| Hardness range | Shore A 5–95 | Shore A 60–95 | Shore A 35–90 | Shore A 3–80 |
| Compression set at 70 °C | 15–75 % | 15–60 % | 20–50 % | 2–20 % |
| Oil resistance in IRM 903 | Moderate to high swell | Low swell | Moderate swell | Low swell |
| Continuous-use temperature | −40 °C to 90 °C | −30 °C to 110 °C | −40 °C to 120 °C | −50 °C to 200 °C |
| Processing route | Injection moulding, extrusion | Injection moulding, extrusion | Injection moulding, extrusion | Liquid injection moulding |
Compliance for DP2339 should be verified against the grade-specific API regulatory sheet. General SEBS compounds can be evaluated for food-contact applications against FDA 21 CFR 177.1810 when all formulation components meet the same regulation; for medical applications, cytotoxicity screening under ISO 10993-5 and extraction testing under USP <661> may be required. The European Union restricts polycyclic aromatic hydrocarbons in certain consumer articles under REACH Annex XVII, and electrical and electronic equipment must comply with RoHS Directive 2011/65/EU limits for lead, mercury, cadmium, hexavalent chromium, PBB, and PBDE. Halogen content can be assessed by DIN EN 14582 or combustive ion chromatography. The absence of intentionally added phthalates may be documented by IEC 62321-8:2017 or gas chromatography-mass spectrometry. Because formulations vary with hardness, colour, and filler system, a composition certificate from API is necessary to confirm the status of DP2339 under each regulatory framework.