| HS Code | 365963 |
| Density | 0.935 g/cm³ |
| Melt Flow Rate | 3.5 g/10 min (190°C/2.16 kg) |
| Tensile Strength At Yield | 17 MPa |
| Tensile Strength At Break | 22 MPa |
| Tensile Elongation At Break | 700% |
| Flexural Modulus | 0.700 GPa |
| Izod Impact Notched | 0.800 J/cm |
| Melting Point | 124°C |
| Vicat Softening Point | 104°C |
| Deflection Temperature At 0 46 Mpa | 70°C |
| Hardness Shore D | 55 |
| Uv Stabilization | Yes |
| Processing Method | Rotational Molding |
As an accredited LyondellBasell Icorene 3546 UV+ PUR 5398 Polyethylene, Linear Low Density factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | Typically packaged in 25 kg polyethylene-lined paper bags, palletized and stretch-wrapped, for LyondellBasell Icorene 3546 UV+ PUR 5398 LLDPE. |
| Container Loading (20′ FCL) | 20′ FCL container loading of LyondellBasell Icorene 3546 UV+ PUR 5398 Linear Low Density Polyethylene: palletized 25 kg bags, shrink-wrapped, secured. |
| Shipping | LyondellBasell Icorene 3546 UV+ PUR 5398 Polyethylene, Linear Low Density is shipped as non-hazardous plastic resin pellets in sealed bags, boxes, or bulk containers. It is not DOT/IMDG/IATA regulated. Keep dry, covered, and away from heat, sunlight, and contamination. No special placards required. |
| Storage | Store LyondellBasell Icorene 3546 UV+ PUR 5398 Polyethylene, Linear Low Density in a cool, dry, well-ventilated warehouse. Keep original containers or bags closed, palletized, and protected from sunlight, moisture, heat, flames, and oxidizing agents. Avoid dust generation and static discharge. Use first-in, first-out stock rotation. Do not overstack; prevent punctures. Store away from incompatible materials and ignition sources. |
| Shelf Life | Typically 24 months from manufacture when stored unopened in original packaging, cool, dry, ventilated, away from sunlight and ignition sources. |
Across all established conversion routes for LyondellBasell Icorene 3546 UV+ PUR 5398 polyethylene, linear low density, rotational moulding remains the dominant downstream process when outdoor weather resistance, low-temperature ductility and environmental stress crack resistance are specified simultaneously. The following application scope limits itself to sectors with proven industrial use: chemical storage, potable water handling, agricultural chemical service, outdoor recreational equipment, logistics containers and marine flotation. No injection-moulding or blown-film substitution is assumed where the powder morphology and UV stabiliser package are designed for biaxial rotation.
| Sector | Binding compliance framework | Relevant test method or clause | Numerical limit or criterion |
|---|---|---|---|
| Chemical storage | ASTM D1998, EN 13341 | ASTM D638-14, ISO 1183-1:2019 | Tensile elongation and density per tank design; no crack at drainage fittings |
| Potable water | FDA 21 CFR 177.1520, EU 10/2011, NSF/ANSI/CAN 61 | 21 CFR 176.170(c), ISO 4892-2:2013 | Overall migration 10 mg/dm² |
| Agricultural chemical | ASTM D1998, ISO 16101, UN 31A/31B | ISO 4892-2:2013 | Low-temperature impact retained after chemical exposure |
| Outdoor recreation | EN 71-3:2019+A1:2021, ASTM F1487-21, REACH Annex XVII entry 50 | ISO 8124-1:2022 | BaP and DBAhA each 0.5 mg/kg |
| Logistics | UN 31H2, IMDG Code | IEC 61340-2-3 | Surface resistivity below 10⁶ Ω where antistatic specified |
| Marine flotation | No single sector standard; product-level test suite required | ISO 4892-2:2013, ASTM D256 | Notched impact at −20°C after weathering |
In chemical storage tank fabrication, Icorene 3546 UV+ PUR 5398 is specified in virgin form as the primary wall material because post-mould regrind addition above a defined threshold reduces notched Izod impact and environmental stress crack resistance in alkaline and hypochlorite service. The dominant structural standard is ASTM D1998 for upright and conical polyethylene tanks, while European installations are assessed under EN 13341 for static thermoplastic tanks storing heating oils, diesel and kerosene. Tensile property verification is performed to ASTM D638-14 and density to ISO 1183-1:2019. Production-scale carousel or shuttle rotational moulding machines are typically used with a biaxial rotation ratio of 4:1, primary axis rotation at 6–10 rpm and secondary axis at 1.5–3 rpm. Oven set points range from 260°C to 295°C, while internal air temperature measured by a Rotolog or equivalent data-logging thermocouple should reach 190–210°C for 12–25 minutes in wall sections of 4–8 mm. The formulation addition ratio for aggressive service is 100 phr virgin powder, with same-grade regrind capped at 10–20 wt% only when the stored medium is non-oxidising and ambient temperature remains above −10°C. Coloured masterbatch based on a polyethylene carrier is added at 2–3 wt%, not exceeding 4 wt%, because higher pigment loading produces a measurable loss in tensile elongation at yield. Cooling is staged: forced ambient air is applied to 85–100°C internal air temperature, followed by water mist to 45–60°C, and final stabilisation in a jig to control shrinkage at port faces and threaded inserts. Terminal finished products include vertical cylindrical chemical storage tanks of 500–20,000 L, secondary containment basins, dosing skid enclosures, pump chambers and transportable chemical mixing vessels.
For rainwater harvesting and potable buffer storage, compliance with drinking water contact regulations becomes the controlling variable because polymeric additives and post-mould surface contaminants must not create sensory or toxicological exceedances. Under FDA 21 CFR 177.1520, the olefin polymer is acceptable for food contact when extraction testing is conducted according to 21 CFR 176.170(c), and in the European Union the finished tank must satisfy EU 10/2011 overall migration limits of 10 mg/dm² for plastic materials in contact with water. System-level approvals typically reference NSF/ANSI/CAN 61, AS/NZS 4020 or WRAS BS 6920 depending on installation geography. The formulation for this sector avoids post-added antistatic agents, amine-based stabilisers and metallic stearates above 0.1 wt% because these species migrate and alter taste-and-odour panel results. The blend remains 100 parts Icorene 3546 UV+ PUR 5398 virgin powder; where colour is required, a 2–3 wt% masterbatch formulated on a compliant polyethylene carrier is added, and total masterbatch content is held below 4 wt% to preserve impact properties after 1,000 h of accelerated weathering under ISO 4892-2:2013. Production of a 5,000 L potable water tank uses closed-mould rotational moulding with an internal air temperature plateau at 190–200°C and a deliberately slow cooling rate of 0.5–1.0°C/min through the crystalline solidification zone to reduce residual stress at baffle cut-outs. Mould release is restricted to food-grade silicone emulsions applied at less than 5 g/m²; wax-based release agents are not used because they can leave non-compliant residues on the contact surface. Terminal finished products include rainwater recovery tanks with leaf-screened inlet structures, underground potable water cisterns, desalination buffer tanks, emergency water distribution bladders and hospital water storage units.
In agricultural chemical handling operations, field failures are observed most often when vessels are exposed to sub-zero ambient temperatures after repeated contact with emulsifiable concentrates and weak acids, which accelerate environmental stress crack propagation at moulded-in ribs and thread bosses. The relevant tank standard is ASTM D1998, supplemented by ISO 16101 for transportable liquid chemical packaging and UN 31A or UN 31B intermediate bulk container requirements when the tank is mounted on a skid or road trailer. Formulation data for agricultural sprayer units indicate that regrind should be limited to 10–25 wt% from the same UV-stabilised grade, with the upper value reserved for non-structural flat zones because rocker-arm and baffle areas exhibit impact transition temperatures that shift upward by 8–15°C when regrind exceeds 30 wt%. Carbon black masterbatch is incorporated at 1–2 wt% for prolonged UV resistance in equatorial agriculture, while conventional phthalocyanine blue or green masterbatches are applied at 2–3 wt%. Processing uses a biaxial rotational moulding machine with a 4:1 arm ratio, oven set point 270–290°C, and internal air temperature hold of 195–210°C for 18–35 minutes depending on wall thickness from 5 mm to 12 mm. After the oven stage, forced air is introduced at 20–25°C and a velocity of 2–4 m/s until internal air temperature falls to 90°C; a water spray is then used to accelerate cooling, but the spray is interrupted at 50°C to avoid condensate marking on post-mould fluorination surfaces. Terminal product types include tractor-mounted sprayer tanks of 400–1,500 L, broadacre self-propelled sprayer sumps, vineyard air-blast sprayer hoppers, fertiliser dosing cones, seed treatment mixing vessels and livestock water troughs.
Under the toy safety migration limits set by EN 71-3:2019+A1:2021, outdoor playground and recreational components manufactured from Icorene 3546 UV+ PUR 5398 are specified principally for low-temperature ductility, ultraviolet colour retention and controlled heavy metal release. The relevant mechanical safety framework is ASTM F1487-21 for public playground equipment and ISO 8124-1:2022 for mechanical and physical properties of toys where the part reaches the consumer sector. Under REACH Annex XVII entry 50, polycyclic aromatic hydrocarbons in accessible plastic parts are restricted to 0.5 mg/kg for benzo[a]pyrene and 0.5 mg/kg for dibenz[a,h]anthracene, which constrains pigment selection to high-purity organic or inorganic grades. The formulation for structural components maintains 100 wt% virgin 3546 UV+ powder because impact-critical sections such as slide entry rims and rotationally moulded tunnel joints show unacceptable crack initiation when regrind is added above 5 wt%. Light-stable masterbatch is added at 2–4 wt%, with titanium dioxide and selected organic pigments, and no additional lubricant package is introduced beyond the base stabilisation of the grade. Production is carried out on aluminium moulds with a 4:1 biaxial rotation ratio, oven set point of 260–280°C, internal air temperature target of 190–205°C, and forced-air cooling at 1.0–1.5°C/min from 120°C to 60°C to minimise sink marks over large flat surfaces. Mould surface texture is restricted to VDI 3400 class 24–27 on slide contact faces to balance slip performance and cleanability. Terminal finished products include rotomoulded spiral slides, playhouse wall panels, climbing arch sections, tunnel tubes, sand and water tables, balance boards and outdoor fitness equipment covers.
When regrind reuse is cost-driven, industrial logistics containers present a process boundary where exceeding 30 wt% regrind from the same UV-stabilised LLDPE grade begins to produce measurable reductions in low-temperature drop impact and environmental stress crack resistance at weld lines formed during the rotation cycle. Compliance for shipment of dangerous goods is defined by UN 31H2 for plastics IBCs and the IMDG Code for marine transport; for food logistics, FDA 21 CFR 177.1520 and EU 10/2011 apply to the inner contact layer. The formulation split for insulated fish tubs and general bulk containers is 70 wt% virgin Icorene 3546 UV+ PUR 5398 to 30 wt% same-grade regrind, with carbon black masterbatch at 1–2 wt% for antistatic behaviour or grey pigment at 2–3 wt% for non-food closed-loop transport. When static dissipative performance is specified, conductive carbon black is added to achieve surface resistivity below 10⁶ Ω per IEC 61340-2-3, but this addition level typically reduces tensile elongation at break by 10–20% and requires a 5–8°C upward shift in internal air temperature to maintain melt flow during the lay-up phase. Rotational moulding of thick-wall logistics containers uses steel or cast aluminium moulds, a biaxial rotation ratio of 4:1, oven set point 270–300°C, and internal air temperature hold of 200–215°C for 25–45 minutes in sections of 10–25 mm wall thickness. Controlled cooling is critical because unvented internal corners exhibit shrink voids when cooling rate exceeds 1.5°C/min through the crystallisation plateau from 125°C to 95°C. Terminal finished products include UN-certified intermediate bulk containers for solid chemicals, insulated fish tubs, automotive goods handling bins, heavy-duty waste skips, medical waste containers and returnable dunnage trays.
| Sector | Typical wall thickness | Oven set point | Internal air temperature target | Cooling rate through crystallisation zone | Regrind cap |
|---|---|---|---|---|---|
| Chemical storage | 4–8 mm | 260–295°C | 190–210°C | Staged air to 85–100°C, then water mist | 10–20 wt% |
| Potable water | 8–15 mm | 265–285°C | 190–200°C | 0.5–1.0°C/min | 0 wt% structural |
| Agricultural chemical | 5–12 mm | 270–290°C | 195–210°C | Air 2–4 m/s to 90°C | 10–25 wt% |
| Outdoor recreation | 3–6 mm | 260–280°C | 190–205°C | 1.0–1.5°C/min from 120°C | 5 wt% |
| Logistics | 10–25 mm | 270–300°C | 200–215°C | Below 1.5°C/min from 125°C | 30 wt% |
| Marine flotation | 6–12 mm | 260–280°C | 190–200°C | Air to 90°C, water mist to 60°C | 0 wt% below waterline |
Because salt-spray exposure and ultraviolet irradiation control service life, marine flotation and fender shells use the UV+ stabiliser package of Icorene 3546 UV+ PUR 5398 to delay surface chalking and impact embrittlement. No single sector-specific standard governs all rotomoulded marine floats; the relevant test suite includes ISO 4892-2:2013 for accelerated weathering, ASTM D638-14 for tensile properties and ASTM D256 for notched Izod impact at −20°C. Float bodies are produced from 100 wt% virgin UV-stabilised powder; regrind is not added to external shells below the waterline because low-temperature impact after seawater plasticisation can degrade. Coloured masterbatch is incorporated at 1–3 wt% using UV-stable pigments, and hygroscopic additives are excluded from the compounding step. For foam-filled units, post-mould injection of closed-cell polyurethane foam with density 40–80 kg/m³ is used after shell cooling to 40°C; foam exotherm must not exceed 120°C to avoid stress cracking at shell walls. Rotational moulding is performed with a 4:1 biaxial ratio, oven set point 260–280°C, internal air temperature hold at 190–200°C, and wall thickness of 6–12 mm. For large cylindrical floats, primary rotation is adjusted to 6 rpm and secondary rotation to 1.5 rpm to maintain powder lay-up without bridging at end caps. Terminal finished products include floating dock floats, mooring buoys, navigation marker shells, aquaculture cage collars, marine fender skins and pontoon modules.
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LyondellBasell Icorene 3546 UV+ PUR 5398 Polyethylene, Linear Low Density is a linear low-density polyethylene powder formulated for rotational molding. The trade designation identifies a UV-stabilised LLDPE base with the PUR 5398 color/additive formulation; the suffix is a product-formulation identifier, not a polyurethane or reactive modifier. The material is supplied as a free-flowing powder with controlled particle-size distribution to promote uniform melt coalescence on multi-axis tooling. Incoming resin evaluation normally records melt mass-flow rate under ISO 1133-1 at 190 °C and 2.16 kg, density under ISO 1183-1, bulk density under ISO 60, and dry flow under ISO 6186. Because the base polyethylene is a linear low-density ethylene copolymer, the short-chain branching distribution reduces post-mold warpage and improves low-temperature impact relative to a high-density polyethylene rotational molding resin of equivalent melt flow. Lot-specific release data for the PUR 5398 formulation should be obtained from the supplier’s certificate of analysis; published data for this specific color configuration is limited, and class-typical LLDPE data should not be substituted for grade qualification.
Rotational molding polyethylene grades are differentiated by density, melt flow, flexural stiffness, low-temperature impact, and environmental stress crack resistance. Unmodified HDPE rotomolding powders typically provide higher flexural modulus and better top-load resistance, but they exhibit lower ESCR and a greater tendency toward brittle failure at sub-zero temperatures. A linear low-density ethylene copolymer such as the Icorene 3546 UV+ base resin retains ductile behavior under ISO 179-1/1eA notched impact conditions at -40 °C, while an HDPE of the same melt flow may fall below the ductile threshold. The UV-plus package is a second separation point: a standard colored HDPE rotomolding powder may contain only a pigment masterbatch, whereas the UV+ designation indicates a formulated light-stabilizer system intended to delay gloss loss, chalking, and tensile elongation loss in outdoor exposure. The PUR 5398 color/additive package does not alter the base resin density class, but pigment particle content and additive loading can shift melt stability and cycle time during rotational molding. Where creep resistance or maximum top-load stiffness is required, the material must be compared with HDPE rotomolding grades using ISO 899-1 creep data and ASTM D1693 ESCR data rather than by single-point tensile values alone. Published data for this specific configuration is limited; comparative ranking should therefore be confirmed on actual molded parts.
In shuttle and carousel rotational molding machines, heat transfer into the powder bed is governed by mold swing radius, oven setpoint, and the powder’s particle-size distribution. A free-flowing LLDPE powder with controlled dry flow under ISO 6186 enables uniform filling of deep ribs, vents, and thread inserts; poor dry flow causes particle bridging in narrow cavities and produces thin or voided walls. The powder is often processed at oven setpoints between 240 °C and 290 °C, while the peak internal air temperature is maintained in the region of 200 °C to 260 °C for linear low-density polyethylene. Molders monitor internal air temperature with shielded thermocouples and use that signal to terminate the heating cycle. Heating beyond the necessary peak internal air temperature accelerates oxidative degradation, increases melt adhesion to the mold surface, and discolors the internal wall. After fusion, the cooling phase is controlled by forced air, water mist, or full water spray; rapid cooling raises cycle rate but can increase part warpage and reduce low-temperature impact. In thick-section moldings, differential shrinkage between the outer mold-contact surface and the inner air-exposed surface produces residual stress that is evaluated by annealing trials or by measuring post-mold dimensional change after conditioning at 23 °C under ISO 291. Pigment packages such as PUR 5398 change infrared absorption characteristics; dark or saturated colors can reduce the time required to reach peak internal air temperature in comparison with natural powder. Production-scale line data should be established for the specific mold mass, wall thickness, and color because published data for this exact formulation is limited.
Incoming resin acceptance for rotational molding powder is not limited to melt flow and density. Mechanical tests are performed on rotomolded plaques or compression-molded specimens prepared under controlled conditions. Typical laboratory methods include tensile testing under ISO 527-2 using type 1A specimens, flexural modulus under ISO 178, notched Charpy impact under ISO 179-1/1eA, and environmental stress crack resistance under ASTM D1693 condition B at 50 °C in 100% Igepal CO-630. The ESCR test is especially relevant for LLDPE service in contact with aggressive liquids; a higher ESCR value indicates a slower transition from hinge-area crazing to complete fracture. Oxidation resistance is screened by oxidative induction time under ISO 11357-6, with longer OIT values indicating greater retained stabilizer activity. The UV-plus package is further assessed by accelerated weathering in laboratory xenon-arc or fluorescent UV devices using ISO 4892-2 or ASTM G154 cycles. Color difference after weathering is measured according to ISO 11664-4 with a spectrophotometer and reported in CIELAB ΔE* units; gloss retention is measured at 60° under ISO 2813. Because the PUR 5398 pigment may itself affect spectral reflectance, weathering acceptance criteria for dark or saturated shades should be determined on molded plaques of the actual color rather than on natural resin samples. A complete property matrix is maintained in the supplier’s certificate of analysis and raw material release documentation; several test values are product-lot dependent and not fixed by the grade designation alone.
Outdoor service life is governed by UV irradiance, moisture, temperature cycling, and the chemical environment. The UV-plus stabilization package in Icorene 3546 UV+ PUR 5398 is intended for applications in which the molded part is exposed to direct sunlight for extended periods. In accelerated weathering, the key response variables are tensile elongation loss, surface chalking, color change, and gloss loss. ISO 4892-2 xenon-arc testing with daylight filters and controlled irradiance of 0.51 W/m² at 340 nm is commonly used to simulate outdoor exposure; ASTM G154 fluorescent UV testing at 0.89 W/m² at 340 nm provides a lower-cost screening method but does not reproduce the full solar spectral distribution. The stabilization system can be depleted by surface water carry-off, contact with acidic or alkaline runoff, and high surface temperatures resulting from dark pigmentation. Because PUR 5398 is a formulated color package, the solar heat load of the final part must be measured on the actual color; a dark purple surface can exceed the surface temperature of a natural or white part by 20 °C to 40 °C under high solar irradiance, which accelerates oxidative stabilizer consumption. Parts intended for tropical or desert exposure should be tested under wet/dry cycling rather than continuous dry UV exposure alone. When gloss retention under ISO 2813 falls below 50% of the original 60° gloss value, visual appearance may still be acceptable for some applications, but tensile elongation loss should not exceed the end-user specification. Published comparative data for this exact PUR 5398 configuration is limited; outdoor validation on molded components is required for service-life claims.
Rotational molded parts within the performance window of this grade include outdoor playground components, agricultural hoppers and feed troughs, chemical storage tank liners, dock floats, and enclosures requiring a balance of impact strength and UV resistance. For playground components, the material is typically evaluated for low-temperature impact after conditioning at -20 °C and for extractable metals and phthalates according to regional toy safety requirements; compliance with regional toy regulations is not automatically established by polyethylene resin compliance alone. In agricultural tank applications, the resin’s ESCR response is tested under ASTM D1693 in 100% Igepal CO-630 at 50 °C, and the molded part is inspected for pinholes and thin-out around inserts. Chemical storage tank liners produced from LLDPE rotomolding powder resist stress cracking but are not universally compatible with oxidizing acids, aromatic hydrocarbons, and strong oxidizers; compatibility must be verified by immersion testing under ASTM D543 for the specific chemical, concentration, and service temperature. In water-contact applications such as dock floats or water storage liners, the resin may be evaluated against extraction limits under the applicable drinking-water standard. Because the PUR 5398 color package is integrated into the powder, additional pellet-color masterbatch dosing at the machine may not be required; however, the processor must verify that the target wall thickness and dry flow are maintained with the as-supplied powder. The absence of a post-machining blending step reduces the risk of dose-related color variation but also fixes the final pigment concentration at the supplier’s formulation.
The processing window is bounded by melt flow, oxidative stability, and the thermal sensitivity of the UV-plus stabilization system. The LLDPE base resin is not designed for injection molding, sheet extrusion, or blow molding; its molecular architecture and powder morphology are optimized for rotational molding. The stabilizer package imposes a maximum processing temperature above which discoloration, crosslinking, or volatile generation can occur. In practice, peak internal air temperature should be monitored and controlled; operation above the supplier’s maximum recommended value can deplete antioxidant and light stabilizer reserves before the part enters service. Under very high relative humidity, condensation on cold powder surfaces may produce surface defects; drying with warm air at 60 °C for 1–2 h is common if the powder has been stored outside the original sealed packaging. The powder should not be combined with copper-based pigments, pro-oxidant masterbatches, or reactive fillers that may deactivate hindered amine light stabilizers. Post-mold regrind addition can be used only if the regrind is free of oil, metal fines, and other rotational molding contamination; the addition rate is determined by dry flow and bulk density testing rather than by melt flow alone. If dark PUR 5398 powder is blended with natural or white resin, the resulting color and UV performance will shift; the blend ratio must be controlled gravimetrically. Processing data for this specific color on a particular machine is not universally transferable because mold thickness, oven air speed, and part mass change the thermal history.
Regulatory screening for the formulated product addresses polymer composition, colorant chemistry, and migration potential. The polyethylene base resin may be assigned a cell classification under ASTM D3350 for polyethylene pipe and fitting materials when tested in the unfilled, unpigmented condition; the PUR 5398 pigment package modifies the final classification and must be considered separately. For food-contact uses, the resin is assessed under FDA 21 CFR §177.1520 olefin polymers, but the finished article must meet the end-use limitations for fatty foods, alcoholic foods, and high-temperature service. European Union compliance is evaluated under REACH Regulation (EC) No 1907/2006 for registration and SVHC screening. RoHS Directive 2011/65/EU restrictions on lead, mercury, cadmium, hexavalent chromium, PBBs, and PBDEs are typically confirmed by supplier declaration and X-ray fluorescence screening. The table below summarizes the main screening layers; it is not a substitute for a written regulatory certificate for the specific PUR 5398 lot.
| Screening layer | Standard or regulation | Application boundary |
|---|---|---|
| Olefin polymer food-contact | FDA 21 CFR §177.1520 | Finished article must be evaluated for food type and use temperature |
| EU chemical registration | REACH (EC) No 1907/2006 | SVHC screening and authorization not waived by grade name |
| Electrical and electronic equipment | RoHS Directive 2011/65/EU | Restricted substance thresholds apply to homogeneous material |
| Child-use articles | EN 71 series where applicable | Migration limits are determined on the finished article |
| Drinking-water contact | NSF/ANSI 61 where specified | Extraction testing is formulation and part-geometry dependent |
The presence of organic and inorganic pigments in PUR 5398 can influence density measurement; density should be determined on the formulated material, not on the translucent natural base resin. A lot-specific certificate of analysis should state which tests were performed on the final colored powder and which values are inherited from the unfilled base resin. The distinction is critical for release testing because a natural-powder value may not represent the molded colorformulation in outdoor service or in contact with aggressive media.