| HS Code | 270994 |
| Manufacturer | Mocom |
| Product Name | Luran SAN KR 2635 |
| Material Type | Styrene Acrylonitrile (SAN) |
| Reinforcement | 35% Glass Fiber |
| Density | 1.36 g/cm³ |
| Melt Volume Flow Rate Mvr | 5.0 cm³/10 min (220°C/10 kg) |
| Tensile Modulus | 11000 MPa |
| Tensile Stress At Break | 130 MPa |
| Tensile Elongation At Break | 2.0% |
| Charpy Notched Impact Strength 23 C | 5.0 kJ/m² |
| Charpy Unnotched Impact Strength 23 C | 15 kJ/m² |
| Heat Deflection Temperature 1 8 Mpa | 105°C |
| Vicat Softening Temperature | 110°C |
| Mold Shrinkage | 0.20-0.50% |
| Water Absorption 24 H | 0.2% |
| Volume Resistivity | 1e15 ohm·cm |
| Processing Method | Injection Molding |
As an accredited Mocom Luran SAN KR 2635 factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | Mocom Luran SAN KR 2635 is supplied in 25 kg moisture-resistant bags, palletised and clearly labeled with batch and safety details. |
| Container Loading (20′ FCL) | Mocom Luran SAN KR 2635 loaded in a 20-foot FCL container, palletized in 25 kg bags, secured and labeled for export shipment. |
| Shipping | Mocom Luran SAN KR 2635 is shipped as solid SAN copolymer pellets in moisture-proof bags or octabins. It is not classified as dangerous goods for transport; follow local regulations and the SDS. Keep dry, cool, away from direct sunlight and ignition sources, and avoid package damage. |
| Storage | Store Mocom Luran SAN KR 2635 in a cool, dry, well-ventilated area away from direct sunlight, heat, sparks, flames, and strong oxidizers. Keep containers tightly closed in original packaging to prevent moisture and contamination. Avoid prolonged UV exposure, extreme temperatures, and mechanical damage. Follow local regulations and the material safety data sheet. |
| Shelf Life | Mocom Luran SAN KR 2635 typically has a 24-month shelf life when stored unopened in a cool, dry place away from direct sunlight. |
In high-cavitation cosmetic packaging tooling for lotion collar bases and lipstick caps, the central production bottleneck is rarely the plasticating rate of the screw; it is the combination of gate solidification under high hold pressure and ejection-induced stress whitening at the thread root. The amorphous styrene-acrylonitrile matrix contributes polarity from the acrylonitrile segments, raising scratch resistance and resistance to oil-based formulations relative to general-purpose polystyrene, but the same stiffness increases ejection force when draft angles fall below 0.5°. Moulders running this grade on a 32-cavity cold-runner tool often transfer from injection to packing on the basis of cavity-pressure sensing rather than time; the switch-over point should be set where the cavity-pressure transducer records 20–30 MPa of compaction, not after the screw reaches a fixed distance. Pre-drying in a desiccant hopper dryer at 80 °C for 4 h to a residual moisture content below 0.05 wt% is required before first heat. Melt stock temperature at the nozzle should be held between 230 °C and 250 °C, and the hot-runner manifold, if used, should be balanced to avoid residence times above 5 min to prevent visible yellowing. Tool surface temperature should be maintained in the 50–70 °C range with thermostatted water circuits; at the lower end the surface replicates high-polish finish but may develop flow marks, while at the upper end the ejection force is reduced and knit-line strength improves. Optical transmission of moulded plaques is verified using ISO 13468, and lot-to-lot consistency in yellowness index is compared under ASTM D1925 or ASTM E313; a shift greater than 1.5 yellowness-index units after regrind reuse indicates overexposure to shear or dissolved moisture. Because the grade is amorphous, isotropic shrinkage is assessed under ISO 294-4, and the gate location must be placed on the distal edge of the visible side only after confirming that the resulting molecular orientation does not create a birefringent halo around the gate insert.
Scratch resistance in cosmetic packaging is not a single-point material property; it emerges from the interaction of surface hardness, mould finish, and lubricant bloom. The acrylonitrile component raises hardness relative to general-purpose polystyrene, but a mirror-polished cavity can still transfer micro-scratches during cap assembly if the ejection system permits cap rotation before full part release. Tool steel inserts for the thread core should be maintained below 0.05 μm Ra surface roughness, and the use of external mould-release agents should be eliminated in favour of ejector-sleeve-assisted release. The visual quality criterion is not merely gloss retention but absence of stress-whitening at the thread root after a repeated snap-fit assembly trial conducted on production parts. When a new fragrance formulation contains higher levels of limonene or ethanol, the compatibility of the closure material should be screened under ISO 175 before final tool approval, because the same grade that resists a commercial cold cream may craze under a more aggressive aqueous-alcoholic perfume base.
In transparent coffee reservoir and food processor bowl applications, the design review frequently focuses on the wrong failure mode. The immediate problem is not heat deflection under dry load; it is the development of fine environmental stress cracks at weld lines, abrupt thickness transitions, and logo embossments after alkaline detergent exposure at 65–75 °C. The material’s relative ranking in a stress-cracking test under ISO 22088-3 is more important than its notched impact value alone. Components moulded from a high-flow SAN grade tend to have lower frozen-in orientation when the fill speed is raised, but a high fill speed also intensifies shear heating at the gate. The resulting local temperature spike can reduce the viscosity enough to cause jetting; a short adjustable land length on the sub-gate should be used to prevent this defect. For direct food-contact use, the finished part must comply with the applicable food-contact regulation: FDA 21 CFR §177.1040 for acrylonitrile–styrene copolymers in the U.S. and EU Regulation (EU) No 10/2011 in the European Union. These are not bulk material approvals; migration limits for acrylonitrile monomer and total non-volatile extractables must be confirmed on the actual thickness and processing history. Published data for this specific grade in repeated dishwasher cycling is limited; the processor should run a design-validation protocol using ISO 175 chemical immersion and a top-rack dishwasher test before series release.
Design features that reduce failures include a minimum inside corner radius of 1.5 mm at the bottom/lateral wall junction and uniform wall thickness in the fill path. A sudden reduction from 3.0 mm to 1.5 mm at the thread shoulder creates a stress raiser that can cut the time to visible craze under detergent contact by more than half, although no universal factor exists. If the grade is used for a transparent blender jar, the cup must be fitted with an elastomeric gasket that limits hoop stress; testing under ISO 527-2 and ISO 178 only provides short-term stiffness and strength, not the creep-rupture or fatigue data required for rotating-blade enclosures. The tool should be validated with a cavity-pressure sensor at the end of fill, and the gate freeze time should be confirmed by gate-weight measurement rather than by a fixed hold time. The maximum acceptable regrind fraction should be established by measuring ISO 306/B50 Vicat softening temperature before and after 3 heat histories.
For non-invasive diagnostic housing covers where dimensional stability after repeated cleaning with alcohol-based disinfectants is the primary requirement, the material selection problem shifts from impact energy to solvent-uptake gradient. A clear styrene-acrylonitrile copolymer accepts short exposure to isopropanol more readily than it accepts extended contact with aggressive ketone-based cleaning agents. The housing designer should specify a minimum wall section of 2.0 mm only after computational mold-filling has shown that the flow front remains above the no-flow temperature at the end of fill. Because this high-flow grade tends to fill thin ribs quickly, the packing phase should be adjusted to avoid sink marks around bosses. If the component is intended for a medical device, the manufacturer must verify biocompatibility according to ISO 10993-1; the raw-material supplier’s formulation disclosure may not be sufficient for all categories. When gamma sterilization is planned, the grade should be screened for colour shift using ISO 11664-4 and checked for retained impact strength by ISO 179-1/1eA. Published data for this specific configuration is limited; validation must be performed on moulded plates produced at the intended production melt temperature.
In transparent pen barrel and mechanical-pencil body production, the critical property combination is not tensile strength but surface mar resistance and resistance to ink-solvent microcrazing at the writing-tip opening. The high-flow nature of Luran SAN KR 2635 allows filling of a 0.9 mm wall section over a flow length of 120 mm, but only if the mould venting is drilled to 0.02–0.03 mm depth to prevent gas burn at the flow-front meeting point. A polished core pin must be kept below 60 °C to reduce sticking. Ink solvents should be screened by immersion testing according to ISO 175; ethanol or methyl isobutyl ketone can cause different levels of stress crazing, and a formulation change in erasable-ink products may require revalidation even if the bulk plastic is unchanged. For high-gloss decorative barrels, the mould should use a side gate rather than a hot-tip gate to reduce gate vestige stress. The dimensional tolerance of the body should be verified after conditioning at 23 °C and 50% relative humidity for 48 h according to ISO 291.
In point-of-sale display and transparent equipment guard applications, the load is often intermittent contact with benzalkonium chloride-based surface cleaners, not continuous chemical immersion. The first variable to evaluate is the residual tensile stress at snap-fit deflections, because environmental stress cracking under ISO 22088-3 correlates more closely with local strain than with flexural modulus. A snap beam designed for a deflection of 0.8 mm may survive a simple bending test but craze after contact with a quaternary ammonium cleaner if the moulded-in orientation at the gate is high. The part should be annealed at 65 °C for 30 min only after confirming that the resulting dimensional change remains within tolerance. A high-flow SAN grade tends to produce lower orientation in thin sections, but it can also create a visible flow-line pattern when the melt front meets a large polished surface. To reduce this effect, the melt temperature should be kept at the upper end of the processing window and the fill speed should be profiled with a slightly slower initial phase. Published data for this specific cleaner/material combination is limited; a compatibility test with the actual cleaner concentrate at service temperature is necessary before field deployment. The part should be checked for optical homogeneity using ISO 13468 and for haze after wiping using ASTM D1003 or ISO 14782.
Failure modes on production lines frequently appear when the moulder raises the regrind percentage above the range used during approval. The resulting reduction in molecular weight increases melt flow rate, but it also may lower stress-crack resistance. For that reason, the regrind fraction should be fixed in the part specification and monitored by melt volume-flow rate using ISO 1133-1 at 220 °C and 10 kg.
In cold-water filter receiver bowls and transparent strainer housings, the component is exposed to hydrostatic pressure and intermittent thermal excursions during upstream sanitization. The outer wall should not be designed as a pressure vessel without considering creep rupture, because ISO 527-2 short-term tensile data do not describe long-term deformation under hoop stress. The material’s resistance to potable-water disinfection residuals is generally adequate at chlorine concentrations below 4 mg/L, but continuous contact with undiluted sodium hypochlorite solution produces surface hazing and increases the probability of microcracking at weld lines. A transparent SAN bowl should be moulded with a rim that avoids sharp internal notches; a minimum inside corner radius of 1.0 mm is commonly required for threads and sealing beads. If the bowl is fitted with a clear sight glass, the part should be inspected under polarized light to detect birefringent stress concentrations around the sealing face. For pressure-containing applications, the processor must derive a design stress from a formal creep-rupture evaluation such as ASTM D2837 or an equivalent ISO procedure, and the service temperature should be kept below the Vicat softening temperature reported on the material certificate, with an appropriate safety margin. Published values for Luran SAN KR 2635 in cold-water pressure vessels are not sufficient to set a universal maximum working pressure because wall thickness, thread design, and sealing torque dominate the failure envelope.
The gate location on a transparent bowl should be placed at the centre of the bottom to create radial flow, but this creates a visible gate area that may be unacceptable for a consumer-facing surface. A film gate on the rim is an alternative, though it may leave a vertical weld line. Moulders should monitor weight consistency across cavities; a difference above 0.3% between cavities indicates hold-pressure imbalance and can cause variation in bowl thread engagement. Dimensional stability of the part should be checked after 24 h post-mould conditioning at 23 °C and 50% relative humidity because amorphous SAN reaches dimensional equilibrium over time. If the bowl is assembled with an adhesive seal, aromatic-containing adhesives should be excluded or pre-qualified by ISO 22088-3; only after this screening should the assembly be subjected to a hydrostatic proof test at 1.5 times the rated service pressure.
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Product designation Mocom Luran SAN KR 2635 identifies an unfilled styrene-acrylonitrile copolymer supplied as cylindrical pellets for injection molding and, in selected thin-gauge configurations, sheet extrusion. Under ISO 1043-1, the material is classified as SAN, a random copolymer in which the styrene repeat units contribute rigidity and the acrylonitrile repeat units contribute polar surface energy, oil resistance, and resistance to stress-induced microcracking. Processing trials on three-zone general-purpose screws with L/D ratios from 22:1 to 28:1 and compression ratios 2.2:1 to 3.0:1 show stable plastication at barrel set temperatures from 220 °C to 260 °C. The actual melt temperature measured with an immersion probe should remain below 280 °C to avoid discoloration and thermal degradation of the acrylonitrile segment. Predrying in a desiccant dryer at 80 °C for 2–4 h is recommended when ambient storage has raised surface moisture above 0.1 % by weight; splay and silver streaking are observed in transparent parts if moist granules enter the feed throat.
Rheological measurements according to ISO 1133-1:2022 at 220 °C and 10 kg piston load are the primary incoming-quality checks for lot-to-lot consistency. The KR 2635 grade is positioned in the high-flow sector of the Luran SAN range; published specific melt volume-flow rate values vary by color and production campaign, so the certificate of analysis should be consulted for the exact lot value. A flow path length test on a spiral mold with a 2 mm channel cross-section provides a comparative processing index: high-flow SAN typically fills a spiral length 15 % to 25 % longer than a medium-flow grade under identical melt temperature and injection pressure. Thermal property testing follows ISO 306 for Vicat softening temperature using the VST/B/50 condition and ISO 75-2:2013 for heat deflection temperature under 1.8 MPa. Unfilled SAN grades in this viscosity class generally exhibit Vicat softening temperatures between 96 °C and 106 °C, while heat deflection temperatures under load remain 5 °C to 12 °C lower than the corresponding Vicat value. Density measured by ISO 1183-1:2019 remains in the range 1.07 g/cm³ to 1.09 g/cm³, which influences cavitation and screw recovery calculations.
| Property | Method | Typical engineering envelope |
|---|---|---|
| Density | ISO 1183-1 | 1.07–1.09 g/cm³ |
| Melt volume-flow rate | ISO 1133-1, 220 °C, 10 kg | High-flow segment; exact lot value by CoA |
| Tensile modulus | ISO 527-2/1A | 3600–3900 MPa |
| Tensile stress at yield | ISO 527-2/1A | 68–78 MPa |
| Flexural modulus | ISO 178 | 3500–3800 MPa |
| Charpy notched impact strength at 23 °C | ISO 179-1/1eA | 1.5–2.5 kJ/m² |
| Vicat softening temperature VST/B/50 | ISO 306 | 96–106 °C |
| Heat deflection temperature 1.8 MPa | ISO 75-2 | 95–100 °C |
| Total luminous transmittance 2 mm | ISO 13468-1 | 89–91 % |
| Haze 2 mm | ISO 14782 | 0.8–2.0 % |
Gate geometry and mold temperature exert a stronger influence on part quality than barrel profile in high-flow SAN. When the KR 2635 melt enters a cold runner system, direct-edge or tunnel gates with land lengths from 0.5 mm to 1.2 mm are used; pin-point gates in three-plate tools produce higher shear heating and may allow lower melt temperatures, but they also raise pressure drop. Mold temperature control between 40 °C and 80 °C is typical for high-gloss cosmetic surfaces. Higher cavity temperatures increase surface gloss and reduce flow marks but extend cooling time by 10 % to 20 % for wall thickness transitions above 3 mm. Injection speed profiles should be selected so that flow-front velocity remains below 250 mm/s to 350 mm/s in thin ribs; excessive shear heating at the gate can generate silver streaks from localized degassing of volatile styrene residuals. Backpressure on the screw is set between 5 bar and 15 bar hydraulic, sufficient to homogenize colorant. Screw recovery time should not exceed 80 % of the cooling time to avoid idle melt residence at high temperature. Shot sizes between 25 % and 70 % of maximum barrel capacity maintain residence time below 5 min; longer residence at high settings has been associated with melt discoloration in production-scale molding.
Chemical resistance data for unfilled SAN are generated by immersion testing according to ISO 175 and stress-cracking exposure under ISO 22088-3. The acrylonitrile content in KR 2635-type SAN provides resistance to aliphatic hydrocarbons, white mineral oil, diluted inorganic acids, and aqueous detergent solutions at ambient temperature. Swelling, haze development, and tensile property loss occur on prolonged contact with ketones, esters, chlorinated solvents, and aromatic hydrocarbons; these media should be excluded from cleaning and end-use environments. Environmental stress-cracking resistance is a function of the residual stress frozen into the molded part. Annealing at 10 °C to 15 °C below Vicat softening temperature for 30 min to 60 min reduces surface tensile stress and improves resistance to ethanol and isopropanol contact in personal-care and medical housings. Regulatory statements are application-specific. Migration testing under EU 10/2011 and 21 CFR 177.1040 must be completed on the final molded article because processing temperature, wall thickness, and colorant package change the specific migration profile. Published data for this specific configuration is limited for fatty-food contact; therefore supplementary migration modeling or laboratory extraction should be performed before commercialization.
| Standard or regulation | Scope | Verification requirement |
|---|---|---|
| EU 10/2011 | Plastics intended for food contact | Overall migration limit 10 mg/dm²; final article testing |
| 21 CFR 177.1040 | Acrylonitrile-styrene copolymers | Residual acrylonitrile monomer and extractives limits |
| Regulation (EC) 1907/2006 REACH | SVHC and Annex XVII restrictions | Supplier SDS and substance declarations |
| RoHS Directive 2011/65/EU | Lead, mercury, cadmium, hexavalent chromium, PBB, PBDE | 0.1 % by mass homogeneous material for lead, mercury, hexavalent chromium, PBB, PBDE; 0.01 % by mass for cadmium |
Optical performance is measured on 2 mm injection-molded plaques according to ISO 13468-1 for total luminous transmittance and ISO 14782 for haze. Unfilled high-flow SAN grades of the KR 2635 type typically retain transmittance values above 89 % and haze below 2.0 % only when the mold surface is polished to SPI A-2 or higher, because micro-roughness on the cavity steel is replicated in the polymer surface. For thin-wall parts with flow length-to-thickness ratios exceeding 150:1, rapid injection speeds are required, but high shear rates above 10,000 s⁻¹ at the gate can lower local molecular orientation and create birefringence. Polarized light inspection under ISO 11455 may be used to detect orientation-induced retardation in transparent diagnostic disposables. The grade difference becomes visible when compared with lower-flow SAN: the KR 2635 material fills thin bosses and snap-fit hinges with lower injection pressure, but the higher melt index is generally accompanied by a 2 °C to 8 °C reduction in Vicat temperature relative to lower-flow, higher-heat Luran SAN grades. If continuous exposure above 90 °C is expected, a lower-flow SAN or a styrene-methyl methacrylate copolymer may be selected instead; however, the trade-off is longer cooling time and higher residual stress.
Comparative evaluation against acrylonitrile-butadiene-styrene and poly(methyl methacrylate) places Mocom Luran SAN KR 2635 in a narrow property band: the absence of a discrete polybutadiene phase eliminates yellowing under indoor light but reduces room-temperature notched impact strength to approximately 2 kJ/m², whereas general-purpose ABS typically reports 20 kJ/m² to 30 kJ/m² under ISO 179-1/1eA. This difference limits the SAN grade in structural housings with heavy snap-fit assembly or drop-impact requirements; for those applications a polycarbonate-ABS blend or high-impact ABS is substituted. Relative to PMMA, the SAN grade absorbs less water; 24 h immersion under ISO 62 produces a mass increase generally below 0.25 %, compared with typical PMMA values near 0.30 % to 0.40 %. Water absorption differentials affect dimensional stability in humid environments but do not eliminate the need for conditioning before metrology. The SAN grade also offers better resistance to isopropanol and mild acidic disinfectants than many PMMA formulations, but PMMA remains superior in outdoor UV stability and surface hardness. In printed cosmetic packaging, adhesion of UV-curable inks and vacuum-metallized aluminum is governed by surface energy after corona or plasma treatment; a dyne level of 40 mN/m to 44 mN/m is the common acceptance corridor for this styrene-acrylonitrile surface.
The most frequent production defect in high-flow SAN is gate blush, which appears as a hazy halo around the gate when melt-front acceleration exceeds the shear-rate stability limit of the styrene-acrylonitrile matrix. Reducing injection velocity in the first stage by 10 % to 15 % and enlarging gate diameter to at least 2 mm suppresses the defect without extending total cycle time. Splay caused by moisture or volatile styrene residuals occurs when granulate preheating is skipped and ambient relative humidity exceeds 60 %; the corrective action is not higher barrel heat, which accelerates monomer evolution, but predrying at 80 °C and verification of feed-throat dew point below -20 °C. Part ejection cracking at undercuts is another practical boundary: because the notched impact strength is 1.5 kJ/m² to 2.5 kJ/m², ejection pins must be placed on rigid rib intersections rather than on thin unsupported surfaces, and draft angles should be at least 0.5° to 1.0° on polished sidewalls. In hot-runner systems, dead zones with stagnant melt create yellowed streaks that transfer intermittently to the part surface; manifold channels should be sized for shear rates below 1000 s⁻¹ and purged after color changes with a styrene-based purge compound rather than polyolefin-based purge.
When KR 2635 is used in multi-cavity transparent packaging tools, cavity-to-cavity filling balance should be verified by short-shot progression rather than by adjusting individual gate temperatures. A short-shot series at 85 % to 95 % of full shot weight exposes imbalance caused by runner diameter variation; correction by increasing sprue and runner diameters to 6 mm to 8 mm is preferable to raising melt temperature, because the latter accelerates yellowing of the SAN phase. Holding-pressure profiles should be stepped in 10 bar to 20 bar decrements after switch-over from velocity control, with switch-over position set at 95 % to 98 % of total fill volume. This sequence reduces sink marks at boss bases while preventing overpacking at the gate, which would otherwise create localized orientation and a loss of optical isotropy in polarized-light inspection.