| HS Code | 619492 |
| Density | 0.930 g/cm³ |
| Bulkdensity | 0.45 g/cm³ |
| Molecularweight | 5.5 million g/mol |
| Averageparticlesize | 150 µm |
| Tensilemodulus | 700 MPa |
| Tensilestressatyield | 17 MPa |
| Tensilestrainatyield | 20 % |
| Tensilestressatbreak | 40 MPa |
| Tensilestrainatbreak | 350 % |
| Charpynotchedimpactstrength | No break |
| Shoredhardness | 62 |
| Abrasionresistance | 100 mm³ |
| Meltingtemperature | 135 °C |
| Vicatsofteningtemperature | 80 °C |
| Thermalconductivity | 0.41 W/m·K |
| Coefficientoflinearthermalexpansion | 200 µm/m·°C |
| Volumeresistivity | >10^14 ohm·cm |
| Dielectricstrength | 45 kV/mm |
| Dielectricconstant | 2.3 |
| Waterabsorption | <0.01 % |
| Coefficientoffriction | 0.15 |
| Chemicalresistance | Excellent to acids, bases, and solvents |
As an accredited Celanese UHMW-PE 4150 ECO-B factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | Celanese UHMW-PE 4150 ECO-B packaging: 25 kg multiwall paper bags, palletized and shrink-wrapped for safe transport. |
| Container Loading (20′ FCL) | Celanese UHMW-PE 4150 ECO-B loaded in 20′ FCL containers, palletized bags, securely stowed for ocean transport. |
| Shipping | Celanese UHMW-PE 4150 ECO-B generally ships as a non-hazardous polymeric powder. It is typically packaged in 25 kg moisture-resistant bags, palletized and shrink-wrapped. Transport by truck, rail, or container without dangerous-goods classification. Store dry, cool, ventilated, away from ignition sources and moisture. Follow local regulations and supplier SDS. |
| Storage | Store Celanese UHMW-PE 4150 ECO-B in a cool, dry, well-ventilated area, away from direct sunlight, heat, sparks, and open flames. Keep original packaging closed, clean, and off the floor to prevent contamination or moisture pickup. Avoid strong oxidizing agents and prolonged UV exposure. Maintain ambient conditions, follow FIFO stock rotation, inspect containers regularly, and avoid excessive stacking. |
| Shelf Life | Store in a cool, dry, well-ventilated area; shelf life is typically 24 months in unopened original packaging, away from direct sunlight. |
Wet-gel microporous separator lines for lithium-ion cells use Celanese UHMW-PE 4150 ECO-B as the primary polyolefin solids fraction in a paraffin-oil plasticizer matrix. The typical compounding floor is 22–28 wt% UHMW-PE, 72–78 wt% paraffin oil, and 0–5 wt% inorganic filler, with silica addition restricted to the upper band only when shutdown-temperature dimensional stability above 130 °C is specified. The ECO-B mass-balance grade retains a molecular weight in the 9.2×10⁶ g mol⁻¹ range; therefore the gel-state chain entanglement density requires a co-rotating twin-screw kneader with a screw L/D ratio of ≥40:1, barrel set points from 180 °C to 230 °C, and vacuum devolatilisation below 20 mbar absolute to prevent pinhole-generating volatile recondensation in the cast web.
Downstream, the gel is filtered through a continuous screen changer, metered by a gear pump, and cast through a T-die with a lip gap of 0.5–1.0 mm onto a chilled roll at 20–40 °C. The cooled gel film is drawn in two directions, with typical machine-direction draw ratios of 4×–6× and transverse-direction draw ratios of 5×–7×; pinhole density becomes the dominant rejection mode when the gel web is drawn beyond 6× MD without a homogeneous gel sub-structure. Solvent extraction in methylene chloride or n-hexane reduces residual paraffin oil to below 1.0 wt%, and heat setting at 120–130 °C stabilises the micro-ribbon architecture. The finished separator typically measures 5–25 μm in thickness and is slit to customer-width rolls for prismatic, cylindrical, and pouch cells. Compliance anchors include ASTM D882-18 for tensile strength and elongation, ISO 15901-1:2016 for porosity by mercury intrusion, IEC 62660-2:2018 for cell-level mechanical and electrical validation, and UN 38.3 transport testing when the separator is integrated into a finished battery pack.
Gel spinning formulations for ballistic and cut-resistant textiles are leaner than separator gels. The typical spinning dope contains 5–10 wt% UHMW-PE 4150 ECO-B, 90–95 wt% decalin or high-purity paraffin oil, and an antioxidant stabiliser loading of 0.1–0.5 wt%; at concentrations above 10 wt%, die-swell instability and spinneret plate fouling increase because the high-molecular-weight grade elongates as a semi-solid gel rather than a viscous solution. The extrusion line is configured around a parallel twin-screw or co-rotating kneader operating at 150–180 °C, followed by a gear pump and a spinneret with 390–780 holes of 0.5–1.0 mm diameter. The extruded gel filaments pass through an air gap of 5–25 mm into a chilled water or ethanol bath, after which the gel yarn is extracted to remove residual solvent and drawn in at least two stages to total draw ratios of 30×–60×.
Denier variability in production is controlled less by draw ratio than by powder bulk density and particle-size distribution entering the kneader; a shift from 0.40 g cm⁻³ to 0.48 g cm⁻³ in feedstock bulk density can alter feed factor by several percent and produce measurable thickness variation in downstream UD laminate. Pre-drying of the powder is required at 80 °C for 4 h when storage RH exceeds 60%, and the grade should not be combined with amine-based stabiliser packages because decomposition residues accelerate gel discoloration. Product-level compliance is demonstrated by ASTM D885-19 for tensile properties of man-made filaments, EN 388:2016+A1:2018 for cut resistance in gloves, and NIJ 0101.06 for ballistic panels; processor quality systems are typically audited to ISO 9001:2015 for traceability. Finished product types include UD prepreg sheets for ballistic vests, cut-resistant gloves, high-tenacity ropes, and composite reinforcement fabrics.
Sintered porous plates, tubes, and discs use 100 wt% UHMW-PE 4150 ECO-B powder with no solvent or binder; interparticle sintering across the 9.2×10⁶ g mol⁻¹ molecular-weight distribution creates the fused neck network that determines permeability. Pore-structure tuning is achieved through particle-size selection rather than formulation additives: finer cuts with a \(d_{50}\) below 100 μm yield mean flow pore diameters in the 5–20 μm band, while coarser cuts extend mean flow pore diameters toward 80 μm, although published data for this specific ECO-B configuration is limited. The powder is cold-compacted in hydraulic platen presses at 5–15 MPa, then sintered in hot-air or nitrogen ovens at 160–190 °C, with soak time scaled at 10–20 min per 10 mm of part thickness. Demoulding is delayed until core temperature falls below 60 °C to prevent thermal contraction cracks.
Fabricated porous elements must demonstrate compliance with FDA 21 CFR 177.1520 for repeat-contact olefin polymers, EC 1935/2004 for food-contact articles, and, where potable-water contact is involved, EU Regulation 10/2011 migration limits; mechanical qualification uses ASTM D790-17 flexural modulus and ISO 178:2019 flexural strength. The terminal product range includes wastewater aeration spargers, vacuum-chuck porous plates, filter discs for pneumatic conveying, and gas-liquid contactor sheets.
Ram extrusion converts the powder directly into stock rods, plates, and near-net profiles at 100 wt% resin loading; internal processing aids are not required, and die-wall lubrication is applied externally only during start-up to prevent early sticking. The single-ram extruder uses a heated die barrel maintained at 200–230 °C and a reciprocating ram pressure of 10–25 MPa; each stroke advances the compacted sinter front by 5–20 mm, and the profile exits the die as a continuous fused section that is cut to length after cooling. The critical process boundary is dwell-time control at the die centreline: short dwell at temperatures above 240 °C causes surface melt fracture, while insufficient pre-compaction below 10 MPa leaves axial micro-voids that appear only after machining.
Compliance for food-machinery wear strips and conveyor guides is anchored to FDA 21 CFR 177.1520 for the base polymer, EN 1672-2:2020 for hygienic equipment design, and 3-A Sanitary Standard 20-24 where dairy conveyor contact is specified. Finished product types include bottle-handling star wheels, chain guides, wear strips, and bushing profiles for beverage and pharmaceutical conveying lines.
Compression moulding of UHMW-PE 4150 ECO-B into thick-section industrial liners uses a two-stage pressure-temperature cycle that differs from ram extrusion in its ability to produce sheets from 10 mm to 200 mm thickness. The press charge is 100 wt% UHMW-PE powder; if coloured identification is required, a non-peroxide pigment masterbatch may be added at 2–5 wt%, but glass fibre, graphite, or amine-based stabiliser packages are avoided because they disrupt particle fusion and may generate internal porosity. Cold pre-compaction is carried out at 5–10 MPa until the charge reaches a density of 0.60–0.70 g cm⁻³, after which heating to 190–200 °C under 10–15 MPa fuses the particles. Soak time follows 15–30 min per 10 mm of final sheet thickness, and cooling is controlled at ≤15 °C h⁻¹ to avoid reduced-density core zones.
Finished liners are machined to flatness tolerances of ±0.2 mm m⁻¹ for hopper and silo discharge surfaces, dump-truck body liners, and bulk-materials impact pads. Compliance testing references ASTM D4020-18 for molecular weight verification, ISO 11542-1:2018 for UHMW-PE sheet classification, and ASTM D790-17 for flexural modulus; abrasive-wear testing for mining applications is typically performed according to ASTM G65-16 using a dry-sand rubber-wheel apparatus.
Lead-acid battery separator backwebs are a separate processing route from lithium-ion separators despite using the same base resin. A representative formulation for automotive SLI separator compound consists of 10–18 wt% UHMW-PE 4150 ECO-B, 25–35 wt% precipitated silica, 45–55 wt% naphthenic process oil, and 0.5–2.0 wt% additives including antioxidant and carbon black. The high filler loading requires a co-rotating twin-screw extruder with oil injection at the mid-barrel position, followed by calendering into backweb thicknesses of 0.15–0.40 mm and embossing ribs of 0.5–1.5 mm. Extraction in counter-current solvent removes the process oil to below 0.5 wt% residual, and the resulting microporous structure provides acid-fill retention and ionic conductance.
Acceptance testing for separator envelopes and sleeves references IEC 60896-21:2021 for stationary valve-regulated lead-acid battery performance, EN 50342-1:2015 for automotive battery dimensions and general requirements, and IATF 16949:2016 for production traceability in automotive supply chains. Finished products are formed separator envelopes, sleeves, and leaf separators for automotive, e-bike, and stationary lead-acid cells.
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Celanese UHMW-PE 4150 ECO-B is a high-molar-mass polyolefin grade positioned within the GUR 4000 series of ultra-high-molecular-weight polyethylene resins. The base grade is characterized by a viscosity-average molecular weight near 9.0 × 10⁶ g/mol determined by solution viscosity according to ISO 1628-3, with density reported at 0.930 g/cm³ under ISO 1183-1. Unlike conventional linear HDPE grades, the material exhibits no practical melt flow under the standard 190 °C and 21.6 kg condition of ISO 1133-1; the melt-state deformation resistance is therefore specified through solution viscosity and molar mass rather than melt flow rate. The ECO-B suffix denotes a mass-balance chain-of-custody variant that incorporates bio-circular feedstock into the ethylene polymer chain, as indicated by the supplier’s material declaration; independent quantitative bio-content values are not supplied in generic grade literature and must be obtained from a batch-specific certificate of analysis. The product is supplied as a free-flowing powder for ram extrusion, compression molding, and sintering operations. Published data for this specific configuration is limited when compared with the fossil-naphtha GUR 4150 control, so first-lot qualification should include full mechanical testing under ISO 527-2 and ISO 11542-2. Because the grade is supplied as powder, storage conditions are a release parameter; moisture regain in humid air remains below 0.01%, but electrostatic charging can reduce bulk-flow consistency. Silo design should account for the powder’s low bulk density, typically 0.40–0.50 g/cm³; the exact value varies with particle size distribution and should not be taken from pellet data. The supplier’s certificate of analysis should therefore include viscosity-average molecular weight, bulk density, and particle size distribution.
The principal differences between the grades are molar mass and the resulting resistance to cold flow and abrasive wear. In the published GUR series hierarchy, GUR 4120 is typically described with a viscosity-average molecular weight near 4.5 × 10⁶ g/mol, GUR 4150 near 9.0 × 10⁶ g/mol, and GUR 4170 near 10.5 × 10⁶ g/mol; these values are supplied as typical, not specification limits. Increasing molar mass reduces melt-state diffusion and raises the compression force and dwell time required for void-free sintering. The 4150 position is therefore selected when abrasive wear in sliding contact and low-temperature impact resistance are required, but where the extended cycle time and higher backpressure of a 4170-type material would overload a ram extruder or slow a multi-cavity compression press. Compared with a lower-molecular-weight 4120 material, the 4150 ECO-B grade offers a more entangled network, which is associated with lower measured abrasion loss under sand-slurry testing and higher notched impact energy under ISO 11542-2. The ECO-B designation itself does not alter the mechanical property class; it is a feedstock credential that places the grade in a bio-circular supply chain. Processors should not assume that existing dryer, vent, or reclaim systems tuned for fossil GUR 4150 will behave identically with the mass-balance grade until the first production lot is evaluated, because published data for this specific configuration is limited.
Ram-extrusion and compression-molding equipment used for 4150 ECO-B operate within narrow thermal boundaries because the ultra-high molar mass prevents convective mixing and limits heat transport. Industrial practice for UHMW-PE ram extrusion sets the barrel and die zones between 190 °C and 210 °C, with die-land pressure generated by a reciprocating plunger rather than a screw; die-land length-to-diameter ratios between 10:1 and 30:1 are common for round profiles and solid wear strips. Compression molding is conducted at platen temperatures of 200–220 °C and pressures staged from 5 MPa to 10 MPa. Because the powder particles consolidate by diffusion rather than viscous flow, hold times must be extended relative to lower-molecular-weight HDPE, and premature pressure removal produces microvoids that lower Izod impact predictability. Pre-drying is typically unnecessary because water absorption is below 0.01% by ISO 62; surface condensation from cold storage should be removed with dry air below 60 °C before feeding. Sustained processing above 230 °C or localized frictional overheating promotes thermo-oxidative chain scission, shifting the molar-mass distribution and degrading abrasion resistance. The material is not a practical injection-molding grade because the melt will not fill conventional runners at standard injection pressures; attempts to raise melt temperature above 230 °C produce oxidation-related gelling and black specks. Batch-to-batch variation in oxidation induction time should be monitored under ISO 11357-6 when extended sintering dwells are used.
The typical values below are derived from GUR 4150 documentation and should be treated as comparative engineering benchmarks, not guaranteed design limits. The ECO-B mass-balance variant is produced to the same base grade specification, but first-lot verification is required.
| Property | Typical Value | Test Method |
|---|---|---|
| Density | 0.930 g/cm³ | ISO 1183-1 |
| Tensile stress at yield | 21 MPa | ISO 527-2 |
| Tensile elongation at break | >200% | ISO 527-2 |
| Shore D hardness | 61 | ISO 868 |
| Notched Charpy impact at 23 °C | no break | ISO 11542-2 |
| Vicat softening temperature A50 | 80 °C | ISO 306 |
| Melting temperature | 133 °C | ISO 11357-3 |
| Water absorption at saturation | <0.01% | ISO 62 |
| Melt flow rate at 190 °C/21.6 kg | not measurable | ISO 1133-1 |
Single-point values do not capture creep at elevated service temperatures. For bearing applications, design calculations should use compressive creep modulus curves obtained under ISO 899-2 and wear rates measured under ISO 15527 or ASTM G65, because the ratio of wear life to initial tensile yield can change sharply when applied surface pressure exceeds 5 MPa at ambient temperature. For components operating below -40 °C, low-temperature Charpy data should be requested, since published data for this specific configuration is limited. Tribological qualification for 4150 ECO-B requires distinguishing between two-body and three-body abrasive wear. In dry sliding against a polished steel counterface, the material exhibits a dynamic coefficient of friction that is strongly velocity-dependent; standard pin-on-disk data under ASTM G99 may not correlate with plant experience when the counterface temperature exceeds 40 °C. Three-body wear involving sand, coal fines, or crystalline particulates is better evaluated with the sand-slurry test under ISO 15527 or the rubber-wheel dry-sand test under ASTM G65. Published data for this specific configuration is limited, so wear-rate comparisons to fossil GUR 4150 should be generated on the same lot and the same test equipment. In conveyor wear-strip service, the practical failure mode is not always mass loss; it is often the formation of a burr or lip at the strip edge. This burr initiation is governed by the shear yield stress and the local temperature rise from frictional heating, not solely by molar mass. Therefore the ratio of Shore D hardness to elongation at break is sometimes a better early screening parameter than a single abrasion index. Reports from production lines with reciprocating ram extruders indicate that batch-to-batch variation in powder particle size distribution below 100 µm can shift extrusion backpressure by 5–10% and alter surface finish; incoming powder should be checked by sieve analysis or equivalent laser diffraction according to ISO 13320 before switching lots.
Wear strips, chain guides, filter press plates, pump wear plates, and dry-bulk handling screw flights represent the principal application space for 4150 ECO-B. In these applications the high molar mass and low coefficient of friction against polished steel reduce surface erosion when fine-particle slurries or granulated solids are conveyed at low surface velocities. Food-contact uses such as cutting boards, guide rails, and FDA-compliant wear components are permitted only when the specific grade is listed under 21 CFR §177.1520; the fabricator must verify the supplied certificate because the ECO-B mass-balance feedstock must not affect final food-contact test results. The geometric design should account for the material’s high coefficient of linear thermal expansion relative to steel, typically near 1.5 × 10⁻⁴ K⁻¹, by providing slotted or oversized fasteners. Continuous service under load above 80 °C should be avoided because creep accelerates and the material loses bearing clearance; steam sterilization above 121 °C is outside the recommended range. The polymer resists many dilute acids, alkalis, and salt solutions, but strong oxidizing acids such as concentrated nitric acid cause oxidative attack at elevated temperature. Hot-gas welding should not be used; joining should be done by butt fusion, spin welding, or mechanical fastening. UV exposure without carbon black or hindered-amine stabilization leads to surface embrittlement within a few thousand hours of outdoor exposure; unstabilized natural-grade material is intended for indoor or non-UV service. The final part specification should be controlled under ASTM D4020 or ISO 11542-2 for UHMW-PE materials. In filter press plates, resistance to hydraulically loaded deformation is governed by flexural modulus and creep, not tensile yield; plates should be machined from compression-molded sheet rather than extruded profile to minimize weld-line porosity. In pump wear plates, edge-gating of the original molding blank can create anisotropic wear behavior; the fabricator should orient the machined wear face such that the primary sliding direction is parallel to the blank surface, not through the thickness.
Compliance statements for 4150 ECO-B must be product-specific and supported by the supplier’s material declaration. The following matrix identifies the standard designations most often referenced in requests for quotations and incoming-material release.
| Regulatory or Technical Area | Designation |
|---|---|
| Food contact, United States | 21 CFR §177.1520 |
| Food contact, European Union | Regulation (EU) No 10/2011 |
| Registration, evaluation, authorization of chemicals | REACH Regulation (EC) No 1907/2006 |
| Hazardous substances in electrical equipment | Directive 2011/65/EU |
| UHMW-PE material specification | ASTM D4020 / ISO 11542-2 |
| Tensile properties | ISO 527-2 |
| Density | ISO 1183-1 |
| Molar mass by solution viscosity | ISO 1628-3 |
The ECO-B mass-balance claim introduces an additional documentary obligation: users who publish renewable-content statements must obtain the supplier’s third-party mass-balance certificate and a batch-specific attestation. Absent that documentation, only the base UHMW-PE mechanical specification should be communicated. Regulatory compliance is not automatic; fabricators must validate migration limits specific to their part geometry, food simulant, and temperature conditions under Regulation (EU) No 10/2011 or 21 CFR §177.1520 as applicable.