| HS Code | 425744 |
| Polymer Type | Medium Density Polyethylene (MDPE) |
| Material Designation | PE 80 |
| Density | 0.935 g/cm³ |
| Melt Flow Rate 190 C 2 16 Kg | 0.6 g/10 min |
| Melt Flow Rate 190 C 5 Kg | 2.0 g/10 min |
| Tensile Stress At Yield | 18 MPa |
| Elongation At Break | >600% |
| Flexural Modulus | 800 MPa |
| Vicat Softening Temperature | 115 °C |
| Environmental Stress Crack Resistance 10 Igepal | >1000 h |
| Carbon Black Content | 2.0-2.5% |
| Uv Stabilization | Yes |
| Color | Black |
| Moisture Content | <0.02% |
| Oxidation Induction Time 200 C | >20 min |
| Minimum Required Strength Mrs | 8.0 MPa |
As an accredited Baystar MDPE HL 3563UV factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | Baystar MDPE HL 3563UV is typically supplied in 25 kg polyethylene bags, 40 bags per pallet (1,000 kg net). |
| Container Loading (20′ FCL) | Baystar MDPE HL 3563UV is packed in 25 kg bags, palletized, and securely loaded into a clean, dry 20′ FCL container. |
| Shipping | Baystar MDPE HL 3563UV is a non-hazardous medium-density polyethylene resin in pellet form, typically shipped in 25 kg bags or bulk containers. Transport in dry, covered vehicles; avoid moisture, heat, and prolonged UV exposure. Not regulated as dangerous goods under DOT/IMDG. |
| Storage | Store Baystar MDPE HL 3563UV in a cool, dry, well-ventilated area, away from direct sunlight, heat, ignition sources, and strong oxidizers. Keep material in sealed, labeled original containers/packaging, off the floor, to prevent moisture pickup, contamination, and physical damage. Avoid generating dust and prolonged UV exposure; follow the manufacturer’s SDS and local storage regulations. |
| Shelf Life | Typically 12 months from manufacture when stored in original unopened packaging in a cool, dry place away from direct sunlight. |
Rotational molders producing 2,000 L vertical agricultural water storage tanks on shuttle-type machines charge 35-mesh Baystar MDPE HL 3563UV powder with a precompounded UV stabilizer package. The powder is dry-blended with a polyolefin color concentrate at 3–5 wt% in a double-cone or ribbon blender. Oven set point is held at 280–320°C, depending on tooling wall thickness and line speed. Peak internal air temperature is typically 185–205°C for 6–8 mm sidewalls. The mold is cooled by forced air for 8–12 min and then a water mist at 40–60 kPa until demold surface temperature falls below 80°C. A slower cooling segment before water mist reduces warpage on flat sidewalls. Melt index measured by ASTM D1238 at 190°C/2.16 kg is a batch release parameter. Typical rotomolding MDPE grades fall at 3.5–6 g/10 min; the specific value is confirmed on the supplier certificate of analysis. Chemical homogeneity is evaluated by ASTM D1693 environmental stress crack resistance testing. North American upright tank buyers often require ASTM D1998-21 compliance. Potable water contact requires NSF/ANSI/CAN 61 certification on the molded part, not the raw resin alone. Powder sieve analysis per ASTM D1921 should show 80–90 wt% through a 35-mesh screen and retained on a 100-mesh screen. At storage relative humidity above 60%, powder should be held in sealed hoppers or pre-dried at 60–70°C for 1–2 h before charging. Published data for this specific configuration is limited.
Cooling rate influences crystalline morphology. Water mist quench increases amorphous fraction and improves low-temperature impact, but reduces flexural modulus and can increase residual stress at thick bosses. Slow air cooling before water mist promotes higher crystallinity and better modulus at the expense of environmental stress crack resistance. The precompounded stabilizer system is typically a hindered amine light stabilizer combined with a UV absorber. Exact chemical identity appears in supply chain SDS documents. The mechanism protects the polymer matrix; it does not automatically protect non-UV-stable pigments.
The following production starting points are used on shuttle machines with forced-air ovens. Tooling heat transfer differs and may require adjustment.
| Nominal wall thickness | Oven set point | Peak internal air temperature | Forced-air cooling | Water mist cooling |
|---|---|---|---|---|
| 3–4 mm | 270–285°C | 170–180°C | 6–8 min | 2–4 min |
| 5–6 mm | 280–300°C | 180–195°C | 8–10 min | 3–5 min |
| 7–8 mm | 290–310°C | 185–200°C | 10–12 min | 4–6 min |
| 10 mm | 300–320°C | 195–210°C | 12–16 min | 5–8 min |
Playground panels and tunnel shells molded from HL 3563UV must satisfy ASTM F1487-21 and EN 1176 structural and entrapment requirements. The UV stabilizer package is melt-homogenized at the resin supplier level; pigment is introduced by dry-blending. Direct addition of liquid pigment at 0.5–1.5 wt% can disrupt particle flow in the mold and create surface porosity. Rotational molding in aluminum tooling with a 4:1 rotational speed ratio permits wall thickness of 5–8 mm. Cycle time at 300°C oven temperature ranges from 18–22 min for 6 mm nominal wall. Accelerated weathering per ASTM G154 Cycle 1 provides a screening comparison, but it does not reproduce all Florida UV and moisture cycles. Outdoors, yellowing and gloss loss are monitored using ASTM D2244 Delta E and ASTM D523 gloss. Heavy metal migration testing for child contact parts uses ASTM F963 or EN 71-3 methods. One process conflict is oven dwell: short dwell leaves porosity; long dwell consumes hindered amine stabilizer and causes discoloration. The peak internal air temperature window is held at 185–200°C with a tolerance of ±5°C. Below this window, powder sintered at the mold surface does not fully coalesce. Above this window, the outer layer oxidizes and yellows.
Zinc stearate release agent applied at 2–4 g/m² prevents mold sticking but can plate out in textured cavities. After 300–400 cycles, textured aluminum tools lose pattern sharpness and should be re-textured or replaced. The molded part is cut at load-bearing posts for tensile strength per ASTM D638 Type IV at 50 mm/min. Low-temperature impact at -20°C is tested by ISO 179-1 to verify no brittle failure in cold climates. Wall thickness variation across a tunnel shell is held within ±15% of nominal to prevent entrapment gaps after assembly.
A flat chemical containment basin is not a simple open-box molding job. The resin is processed as a 35-mesh powder with 2–4 wt% black or dark-green polyethylene concentrate. Flat basins with wall thickness 4–6 mm are prone to oil-canning if cooled too rapidly on one face. Molders use steel tooling with external ribs to limit deflection. Chemical exposure is evaluated by immersion per ASTM D543 using specific solvents or oxidizing agents. Bending resistance after immersion is tested by ASTM D790. ESCR is measured on molded samples per ASTM D1693 Condition A or C. Secondary containment in North America may be reviewed under EPA 40 CFR 264.175 for hazardous waste storage areas, but the resin itself does not confer regulatory approval. End products include pump basin lids, valve boxes, and acid-neutralization trays. The practical operating limit is chemical-specific; oxidizing acids at elevated temperature may promote stress cracking at parting line regions. No universal chemical resistance table exists for this configuration.
Wall thickness is influenced by the rib-to-nominal wall ratio. A rib depth greater than 60% of nominal wall thickness creates sink marks on the back surface. The mold must be rotated at 4:1 primary-to-secondary speed, with reversal every 20–40 s to avoid powder bridging at corners. The oven set point for a 5 mm basin is 280–300°C. Internal air temperature reaches 180–195°C. Demolding temperature below 75°C is standard. If the part is removed too hot, the unsupported flange curls.
In marine dock construction, buoyancy shells and floating dock pontoons use a 6–10 mm outer shell. Rotational molding occurs in steel or aluminum tooling with internal inserts. After cooling starts, a two-component polyurethane foam is injected into the still-warm shell at mold surface temperature 55–70°C. The foam exotherm interacts with the MDPE shell. Premature foam injection at higher shell wall temperature causes outer-surface sink marks. The UV stabilizer package must survive post-mold exothermic heating of 110–130°C at the foam interface. Low-temperature impact is measured by ASTM D256 at -20°C or by ISO 179-1 Charpy notched impact. Long-term creep under buoyancy load uses ASTM D2990 tension or flexural creep. UV resistance is screened by ISO 4892-2 rather than ASTM G154 for marine buyers. Salt spray exposure per ISO 9227 is less relevant to polyethylene, but fittings and attachment inserts require 316L stainless steel to avoid galvanic degradation. Paintability is poor; identification markings should be hot-stamped or embossed.
Foam adhesion to polyethylene is inherently low unless the bond surface is flame- or plasma-treated. A flame treatment at 2–4 m/min travel speed increases surface oxygen content, but the effect decays within 48 h. Mold release agents must be eliminated from the bonding area. The outer shell is often post-machined at attachment points. Hole locations should be molded with insert plates rather than drilled to reduce crack initiation. The wall thickness at insert bosses is increased to 10–12 mm to compensate for local stress concentration. The foam injection window is narrow: shell temperature below 55°C leads to void formation because foam shrinkage separates from the shell; above 70°C leads to surface deformation. This threshold is monitored with infrared thermography or contact thermocouples at the injection port.
Above-grade utility vault lids and pull boxes in power distribution use MDPE for impact resistance and UV resistance. Wall thickness transitions from 10 mm at load-bearing ribs to 4 mm at cable entry knockouts create differential shrinkage. Molders use cast aluminum tools with air venting at the rib intersections. Oven set point is 290–310°C. Internal air temperature at the thin section reaches 195°C while the thick rib section may lag by 5–8°C. This thermal lag is reduced by extending plateau time after peak internal air temperature by 3–5 min. Structural acceptance uses ASTM D638 tensile and ASTM D790 flexural modulus on cut specimens. Deflection under distributed load is tested using a three-point test method agreed with the utility buyer because flat molded parts do not have a directly applicable ring stiffness method. The resin is not suited for continuous service above 60°C in direct sun due to heat distortion limits. Specific production data for this exact mold geometry is not publicly available.
The rib section must be designed with a draft angle of at least 3° to prevent mold sticking. Shrinkage of MDPE after cooling can reach 2–3% in the thick sections, and warp at the cover edge is controlled by adding a 10 mm perimeter flange. The flange is tested for flatness by placing the cover on a surface plate and measuring the gap with a feeler gauge. A gap above 2.0 mm over a 500 mm span is generally rejected. This measurement is commercial, not governed by a single ISO standard.
Without painting, outdoor telecom enclosures rely on the precompounded UV stabilizer package and molded-in color. The resin can be rotomolded into enclosures with 4–6 mm walls. Because MDPE is inherently combustible and carries an UL 94 HB classification at best, it is not proposed for indoor plenum or power distribution compartments. Outdoor enclosures must meet IEC 62208 for empty enclosures or NEMA 250 type ratings. Sealing surfaces are machined after molding to maintain flatness. The material exhibits a high coefficient of thermal expansion; a 1 m side wall can expand by 1.5–2.0 mm over a 40°C temperature swing. Designers use slotted holes and flexible gaskets. UV stabilizer protects against chalking in direct sun. Gloss retention is checked per ASTM D523. Published data for this specific configuration is limited.
Gasket sealing faces are machined with a 0.5–1.0 mm flatness tolerance over 300 mm. The material is not compatible with solvent-borne paints; surface treatment requires flame or plasma. Hinges and attachment bosses are molded with stainless-steel inserts. Inserts are preheated to 120–150°C before placement to reduce local cooling. Thread-forming screws into MDPE bosses should engage 2–2.5 times the screw diameter to avoid pull-out. Pull-out force is measured by a customer-specified bolt-pull method. Raw material declarations for REACH and RoHS are requested from the resin supplier; this UV-stabilized MDPE does not contain a halogenated flame retardant package.
Compliance testing is application-dependent. The matrix below summarizes the standard designations relevant to each segment.
| Downstream segment | Primary product standard | Weathering or chemical standard | Mechanical test |
|---|---|---|---|
| Agricultural water tanks | ASTM D1998-21; NSF/ANSI/CAN 61 | ASTM D1693 | ASTM D638 |
| Playground panels | ASTM F1487-21; EN 1176 | ASTM G154; EN 71-3 | ISO 179-1 |
| Chemical containment | EPA 40 CFR 264.175 | ASTM D543; ASTM D1693 | ASTM D790 |
| Marine buoyancy shells | Buyer-specific buoyancy specification | ISO 4892-2; ISO 9227 | ASTM D256; ASTM D2990 |
| Utility vault lids | Utility specification | Buyer-specific UV exposure | ASTM D638; ASTM D790; three-point deflection |
| Telecom enclosures | IEC 62208; NEMA 250 | ASTM D523 | ASTM D638 |
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Baystar MDPE HL 3563UV is a medium-density polyethylene hexene copolymer supplied as a pre-compounded ultraviolet-stabilised pellet. Manufacturer-published nominal values include a density of 0.935 g/cm³ and a melt index of 6.5 g/10 min at 190 °C under a 2.16 kg load when tested in accordance with ASTM D1505 and ASTM D1238. The resin occupies the medium-density polyethylene band and is distinguished from butene-copolymer MDPE by its hexene comonomer and from non-UV grades by the absence of a separate high-letdown UV masterbatch at the converter. Applications include rotationally molded tanks, outdoor enclosures, agricultural chemical containers, and extruded profiles where long-term weathering stability is required.
ASTM D883 defines medium-density polyethylene as ethylene plastics having a density from 0.926 to 0.940 g/cm³. At 0.935 g/cm³, Baystar MDPE HL 3563UV is positioned in the upper portion of the MDPE range, which provides higher stiffness than lower-density LLDPE but lower thermal expansion stress than HDPE. The hexene comonomer introduces C6 short-chain branches; these are longer than the ethyl branches produced by butene and therefore improve tie-molecule mobility during slow crack propagation. This molecular feature is reflected in environmental stress crack resistance values above 1,000 h as measured by ASTM D1693 Condition A, 100 % Igepal.
The melt index of 6.5 g/10 min indicates a molecular weight low enough for flow into complex mold features but high enough to retain tensile yield strength of approximately 18 MPa and flexural modulus of approximately 700 MPa. Differential scanning calorimetry in accordance with ASTM D3418 typically shows a peak melting temperature between 122 °C and 128 °C. Specific molecular weight distribution parameters are not published in standard datasheets; therefore, processability adjustments are based on melt index and shear response measured by ISO 1133-1 or ASTM D1238 rather than on complete rheology curves.
| Property | Test method | Nominal value |
|---|---|---|
| Density | ASTM D1505 | 0.935 g/cm³ |
| Melt index | ASTM D1238 | 6.5 g/10 min at 190 °C/2.16 kg |
| Tensile yield strength | ASTM D638 | 18 MPa |
| Flexural modulus | ASTM D790 | 700 MPa |
| Elongation at break | ASTM D638 | >700 % |
| Environmental stress crack resistance, F50 | ASTM D1693 | >1,000 h |
Manufacturer-published nominal values are not specification limits. Lot-to-lot variation and conditioning history should be controlled through incoming inspection and retained-sample testing under the same standard designations.
The limiting variables in shuttle-type rotational molding ovens are heat transfer through the powder bed, peak internal air temperature, and the thermal stability of the pre-compounded UV stabiliser system. Commercial rotational molding grades are ground to a powder with not more than 10 % retained on a 35-mesh (500 μm) sieve. Coarser fractions extend the fusion stage and may produce microvoids at the inner wall. The melt index of 6.5 g/10 min permits shorter heating time than fractional-melt HDPE but does not eliminate the need for a uniform wall thickness distribution.
Oven air temperature is commonly set between 260 °C and 320 °C. Peak internal air temperature should reach 200 °C to 230 °C for complete particle coalescence. If the peak internal air temperature remains below 180 °C, residual powder and pinholes are observed in field rotomolding operations. Conversely, extended exposure above 280 °C can consume ultraviolet stabiliser additives and shift the long-term weathering response; process qualification should include accelerated weathering according to ISO 4892-2 or ASTM G155 on parts taken from the upper and lower oven temperature limits.
Cooling rate after fusion affects warpage and shrinkage. Forced-air cooling followed by water mist is typical on production machines; demolding should occur after the part surface temperature falls below the Vicat softening point. Because the grade has a density of 0.935 g/cm³, shrinkage is lower than HDPE and higher than LLDPE, which must be accounted for in tool dimensions.
In outdoor tank and agricultural equipment production, the use of a pre-compounded UV stabiliser eliminates the let-down ratio associated with external additive masterbatches. On twin-screw extruders with L/D ratios of 36:1 to 44:1, distributive mixing of the pellet is less critical than for concentrates, reducing the risk of UV-protection voids in thin-walled tank corners. However, screw speeds above 300 rpm and die temperatures above 240 °C may increase shear heating and reduce stabiliser effectiveness; published data for this specific configuration is limited, so process robustness should be verified by notched impact testing after accelerated weathering.
Injection molding thick-walled storage tanks and caps is feasible at melt temperatures between 220 °C and 260 °C. Clamp force calculations for the 6.5 g/10 min melt index resin typically fall below those for 0.945 g/cm³ HDPE at equal wall thickness, but the lower density also reduces part weight and load-bearing capacity, so load-bearing designs should use ISO 527-2 tensile data rather than direct substitution from HDPE.
The primary structural differentiation from unstabilised MDPE is the pre-compounded ultraviolet stabiliser package. Unstabilised MDPE exposed to continuous xenon-arc weathering can lose tensile elongation before 1,000 h; Baystar MDPE HL 3563UV is intended for longer outdoor service, although the actual service life depends on UV dose, part thickness, pigment system, and chemical contact. Accelerated weathering should be conducted according to ISO 4892-2 or ASTM G155; pass/fail criteria are commonly defined as retention of at least 50 % of original elongation at break.
Compared with butene-copolymer MDPE at similar density, the hexene comonomer in HL 3563UV increases the intrinsic resistance to slow crack growth without requiring a reduction in density or an increase in molecular weight. A butene-based MDPE often requires a density near 0.930 g/cm³ or lower to match the ESCR of a 0.935 g/cm³ hexene copolymer, sacrificing tensile yield strength and creep resistance. This difference is important in rotationally molded tanks where chemical stress cracking occurs at the inner surface.
| Verification objective | Primary standard | Alternative standard |
|---|---|---|
| Density | ISO 1183-1 | ASTM D1505 |
| Melt mass-flow rate | ISO 1133-1 | ASTM D1238 |
| Tensile yield strength | ISO 527-2 | ASTM D638 |
| Flexural modulus | ISO 178 | ASTM D790 |
| Environmental stress crack resistance | ASTM D1693 | No direct ISO equivalent |
| Accelerated weathering | ISO 4892-2 | ASTM G155 |
| Chemical compatibility | ISO 175 | ASTM D543 |
The pre-compounded UV stabiliser system in HL 3563UV is appropriate for applications where weathering failure would create functional or environmental risk, including agricultural chemical storage, water tanks, outdoor electrical enclosures, and solar equipment housings. The stabiliser is distributed during pellet production, so wall thickness variations do not produce the concentration gradients that can occur with hand-blended or poorly dispersed external masterbatch.
However, the grade is not a universal outdoor material. Natural and translucent parts may require carbon black or opaque pigments for extended service in high-UV deserts or at altitudes above 2,000 m. Contact with strong oxidising agents, aromatic solvents, or chlorinated water may reduce service life; chemical compatibility must be tested under ASTM D543 or ISO 175 conditions for the specific chemical and service temperature. Continuous service above 60 °C under load may exceed the practical limits of medium-density polyethylene, regardless of UV stabilisation. Published data for this specific configuration is limited, and field validation under the intended exposure environment is required before large-scale deployment.