| HS Code | 848544 |
| Polymer Type | Ultra-high molecular weight polyethylene (UHMW-PE) |
| Density | 0.93 g/cm³ |
| Bulk Density | 0.45 g/cm³ |
| Molecular Weight | 4.5 × 10^6 g/mol |
| Particle Size D50 | 150 µm |
| Melting Point | 135 °C |
| Crystallization Temperature | 118 °C |
| Thermal Conductivity | 0.41 W/(m·K) |
| Specific Heat Capacity | 1.8 J/(g·K) |
| Coefficient Of Linear Thermal Expansion | 200 µm/(m·K) |
| Tensile Modulus | 720 MPa |
| Tensile Stress At Yield | 17 MPa |
| Elongation At Break | 350% |
| Charpy Notched Impact Strength | No break |
| Shore D Hardness | 60 |
| Water Absorption | <0.01% |
| Volume Resistivity | >10^15 Ω·cm |
| Dielectric Constant | 2.3 |
| Dissipation Factor | 0.0002 |
| Coefficient Of Friction | 0.15 |
| Abrasion Resistance | Very high |
As an accredited Celanese UHMW-PE 2122 M ECO-B factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | Typically supplied in 25 kg polyethylene-lined paper bags, palletized at 40 bags per pallet, totaling 1,000 kg net. |
| Container Loading (20′ FCL) | Container Loading (20′ FCL): Celanese UHMW-PE 2122 M ECO-B, palletized bags, securely loaded and braced in a 20-foot container. |
| Shipping | Celanese UHMW-PE 2122 M ECO-B is shipped as a non-hazardous, inert thermoplastic powder in sealed, moisture-resistant bags, cartons, or bulk containers. Transport in cool, dry, clean conditions away from ignition sources and strong oxidizers. No special DOT/IMDG/ADR hazard classification typically applies; follow local regulations and SDS guidance. |
| Storage | Store Celanese UHMW-PE 2122 M ECO-B in a cool, dry, well-ventilated warehouse, away from direct sunlight, heat, ignition sources, and strong oxidizers. Keep original packaging closed, palletized, and off the floor to prevent moisture and contamination. Avoid dust generation and static discharge. Use first-in-first-out stock rotation. Follow local regulations. Maintain clean, dry conditions and protect from ultraviolet light. |
| Shelf Life | Typically two years from date of delivery when stored in original unopened packaging, cool, dry, away from direct sunlight and moisture. |
Celanese UHMW-PE 2122 M ECO-B is an ultra-high-molecular-weight polyethylene powder intended for non-screw plastication processes such as compression molding, ram extrusion, gel spinning, and sintering. The downstream scenarios below are restricted to industrial segments with published processing data for UHMW-PE powders of this class. Each scenario identifies the governing compliance framework, the formulation loading, the production route, and the finished article type. Lot-specific values for average particle size, bulk density, and molecular weight must be confirmed against the manufacturer’s certificate of analysis before line qualification. The ECO-B designation does not alter the processing windows below unless stated in the lot-specific technical data sheet.
Compliance matrix for selected downstream routes.
| Application route | Representative standard or regulation | Scope of verification |
|---|---|---|
| Orthopedic bearing stock | ISO 5834-1:2019, ISO 5834-2:2019, ASTM F648-21, ISO 10993-1:2018 | Powder, molded form, and biological evaluation |
| Lithium-ion separator film | ISO 527-3:2018, ISO 4593:2018, RoHS 2011/65/EU | Tensile, thickness, restricted substances |
| Porous sintered filtration | ISO 4590:2016, ASTM D792-20, FDA 21 CFR 177.1520 | Open-cell content, density, food contact |
| Ram-extruded wear profiles | ASTM D4020-18, ASTM D638-14, FDA 21 CFR 177.1520 | Material specification, tensile properties, food contact |
| Gel-spun fiber | ISO 2062:2009, EN 388:2016+A1:2018, ISO 13997:2018 | Yarn tenacity, cut resistance |
| Food-contact conveyor components | FDA 21 CFR 177.1520, EU 10/2011 Annex V, ISO 9001:2015 | Migration, batch traceability |
Production of implantable bearing blanks from 2122 M ECO-B is applicable only where the specific lot is certified to ISO 5834-1:2019 for virgin powder, ISO 5834-2:2019 for molded forms, and ASTM F648-21 for fabricated UHMW-PE forms, with ISO 10993-1:2018 biological evaluation required for any patient-contact component. In a typical charge, the resin is used at 100 phr; where oxidative stability is required for crosslinked inserts, d,l-alpha-tocopherol is admixed at 0.05–0.30 phr prior to consolidation. The consolidation route uses a vacuum-capable hydraulic compression press with platen uniformity ±3 °C, mold pressure 5–15 MPa, plateau temperature 190–220 °C, and controlled cooling at ≤5 °C/min through the crystalline transition to reduce fusion defects and residual stress. Stock shapes are then machined into acetabular liners, tibial inserts, and patellar components. Pre-drying at 80 °C for 2–4 h is applied when ambient RH exceeds 60%; processing above 250 °C or hold times beyond the supplier-defined dwell window must be avoided because chain scission and oxidation can produce subsurface yellowing detectable only after machining.
In lithium-ion separator film extrusion, 2122 M ECO-B functions as the high-molecular-weight fraction in a wet-process polymer phase that is compounded with HDPE. Formulation ratios for UHMW-PE of this class typically fall at 10–25 wt% of the polymer phase, with HDPE at 75–90 wt%; the polymer phase is then mixed with paraffin oil at a 2:1–4:1 plasticizer-to-polymer mass ratio to enable membrane formation. The downstream production sequence uses a co-rotating twin-screw extruder with L/D 40–65, melt temperature 160–230 °C, screen pack filtration to 40–100 µm, and a T-die with lip gap 0.5–2.0 mm to cast a gel film. Biaxial stretching at 90–120 °C with draw ratios 4:1–7:1 in both machine and transverse directions is followed by solvent extraction in n-hexane or methylene chloride and heat setting at 120–135 °C. The terminal product is a microporous separator film of 5–25 µm thickness with porosity 35–55% and a Gurley air permeability value that must be controlled within the cell manufacturer’s specification. Mechanical film properties are verified according to ISO 527-3:2018, thickness per ISO 4593:2018, and electrolyte wetting per the battery producer’s internal method; REACH and RoHS Directive 2011/65/EU compliance is required for EU market entry. Published data for 2122 M ECO-B in this specific separator configuration are limited; the ratios above are industrial operating windows that must be re-established on the target line.
Pore size distribution in pressureless-sintered elements is controlled by sieve fraction, mold packing density, and sintering temperature rather than by a sacrificial porogen. The formulation for porous tubes, discs, and silencer elements is 100 phr 2122 M ECO-B powder selected in the 100–400 µm particle fraction, with 0.1–0.3 phr hindered phenolic antioxidant added when prolonged exposure to hot air is expected. Consolidation uses vented steel molds heated at 180–210 °C for 20–60 min depending on wall thickness, with no applied compaction pressure beyond the weight of the upper mold plate; small parts may be sintered in convection ovens, while production-scale flat stock is formed on multi-daylight presses. The sintered billet is then machined or skived into filter tubes, aeration discs, and pneumatic mufflers. Permeability and open-cell content are tested according to ISO 4590:2016 and density according to ASTM D792-20; food-contact grades are evaluated under FDA 21 CFR 177.1520 and EU Regulation 10/2011 when used in potable water or beverage lines. The process boundary is narrow: a temperature excursion above 210 °C collapses the porous structure, while under-sintering below 175 °C leaves powder particles only weakly fused and causes particulate release.
When ram extrusion replaces injection molding for high-wear guide profiles, the zero-shear viscosity of 2122 M ECO-B prevents screw plastication and imposes a discontinuous displacement process. The formulation for monolithic profiles is 100 phr; where a compounded formulation is specified, 0.5–1.5 phr calcium stearate or zinc stearate is used as internal lubricant, and 0.5–1.5 phr carbon black is added only for UV-exposed outdoor profiles. In blends with HDPE for injection-molded wear parts, 10–25 wt% of 2122 M ECO-B is dry-blended with 75–90 wt% HDPE to raise abrasion resistance without exceeding the melt flow window of the base resin. The ram extrusion process runs barrel zones at 200–235 °C, die temperature 190–210 °C, and ram pressure 1.5–3.5 MPa, with intermittent ram displacement of 2–10 mm per stroke through a converging die; the profile is then cooled in a water trough and cut in-line. Terminal parts include chain guides, conveyor wear strips, guide rails, and marine fender pads. Conformity to ASTM D4020-18 for UHMW-PE material and ASTM D638-14 for tensile properties is verified on machined specimens from the extruded profile; FDA 21 CFR 177.1520 applies when the profile contacts food during processing.
Gel spinning converts 2122 M ECO-B into high-tenacity fiber only when the powder dissolves into a high-boiling solvent without gel specks. The spinning dope is prepared at 5–15 wt% polymer in decalin or paraffin oil, with 0.1–0.5 wt% antioxidant relative to polymer to protect the solution during residence at 150–180 °C. The solution is extruded through a spinneret with capillary L/D 10–20, passed through an air gap of 5–20 mm, and quenched in a water bath to form a gel fiber. Extraction with n-hexane or dichloromethane removes the solvent, and the yarn is then hot-drawn at 120–150 °C in two or three stages to a total draw ratio of 20–60. The resulting yarn diameter and tenacity are governed by draw ratio; batch-to-batch variation in powder particle size can shift solution viscosity by more than 5% if the concentration is not held within ±0.5 wt%. Terminal products are cut-resistant gloves, ropes, nets, and woven ballistic fabrics. Yarn tensile properties are tested according to ISO 2062:2009, and cut resistance of finished gloves is classified under EN 388:2016+A1:2018 and ISO 13997:2018. Published data for the gel-spinning response of 2122 M ECO-B is limited; pilot-scale trials are required before committing to multi-hole production spinnerets.
When consolidated stock is machined into food-contact conveyor components, 2122 M ECO-B is first formed into plate, rod, or profile by compression molding or ram extrusion, then CNC-machined into star wheels, guide rails, and wear shoes. The formulation is 100 phr, with no processing aids except where a food-contact-listed internal lubricant is required at 0.5–1.0 phr. Compliance is established under FDA 21 CFR 177.1520 for olefin polymers and EU Regulation 10/2011 with migration testing according to EU 10/2011 Annex V; material certification under ISO 9001:2015 is used for batch traceability. The operating temperature range for food contact is limited to the supplier’s published continuous-use temperature, typically below 80 °C for load-bearing components, because creep accelerates above 60 °C under continuous load. No additional additive or colorant should be used unless explicitly cleared for the intended food-contact simulant.
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Celanese UHMW-PE 2122 M ECO-B is a powder-grade ultra-high molecular weight polyethylene in which the numeric suffix 2122 defines a nominal viscosity-average molecular weight of 2.2 × 10^6 g/mol by solution viscosity according to ISO 1628-3. The material belongs to the specification class covered by ASTM D4020 and ISO 11542-1. The M suffix denotes a milled or micronized powder form supplied for ram extrusion and compression moulding; the ECO-B suffix is a mass-balance designation for bio-based or bio-circular ethylene feedstock, not a chemical modification of the polymer backbone. Because the repeat-unit chemistry is identical to that of conventional 2122 M, the grade shares a density of 0.930–0.934 g/cm³ (ISO 1183-1) and an apparent bulk density near 0.42–0.46 g/cm³ (ISO 60). A melt flow rate is not obtainable under ISO 1133-1 because the entangled network prevents measurable flow under standard conditions.
Because the ECO-B variant preserves the polymer backbone of conventional 2122 M, industrial practice treats its processing envelope as equivalent to the conventional grade. Published data for this specific ECO-B designation as a separate datasheet is limited, so substitution in qualified articles should be confirmed by producing first-article parts on the target line and comparing sintered density, tensile properties, and abrasion index against the incumbent material.
Ram extrusion of this molecular-weight class is controlled by compaction and sintering rather than viscous melt pumping. A production ram machine with a barrel diameter of 50 mm to 250 mm typically operates at axial pressures of 25 MPa to 50 MPa for 2.2 × 10^6 g/mol UHMW-PE. The powder is compacted at ambient temperature and then passes through a heated die section in which the surface temperature is maintained between 180°C and 220°C. At the upper end of this range, inter-particle diffusion accelerates but thermo-oxidative chain scission also becomes measurable; sustained barrel temperatures above 230°C reduce molecular weight and lower sand-slurry abrasion resistance under ISO 15527 conditions. Pressure above 50 MPa can generate shear heating at the die wall, producing die-wall slip defects or internal weld lines, while pressure below 25 MPa may leave residual powder boundaries that act as crack-initiation sites.
Pressure transducers and differential scanning calorimetry are used to establish the line-specific window. The melting endotherm for the grade is observed at approximately 133°C to 135°C by ISO 11357-3 at 10 K/min; the sintering temperature must exceed the crystallite melting point but remain below the degradation threshold. Because the ECO-B feedstock allocation does not shift the endotherm, existing ram-extrusion profiles for 2122 M can serve as a starting point. Ram extrusion barrels are typically built with a heated length-to-diameter ratio below 20:1, and the thermal profile is divided into compaction, sintering, and cooling zones. A centreline temperature lag of 10 K to 20 K behind the die wall is common for thick sections and must be accounted for when setting zone temperatures.
Compression moulding of sheet stock for chemical containment is a second route. The powder is filled into a steel or aluminium tool, compacted at 10–15 MPa, and heated to a peak tool temperature of 200–215°C. Sintering time in production practice is commonly estimated at 10–15 min per 10 mm of part thickness. Cooling is performed under maintained pressure at 0.5–1.0 K/min through the crystallisation region; depressurisation while the core remains above 120°C can create internal cavitation. Moisture uptake at 23°C and 50% relative humidity is below 0.01%, so pre-drying is not normally required unless surface condensation has formed after cold storage.
The ECO-B mass-balance variant is compared with conventional 2122 M and higher-molecular-weight UHMW-PE grades in the table below. Because the polymer backbone is unchanged, the expected property profile for 2122 M ECO-B is identical to the conventional 2122 M class; published data for the ECO-B designation as a separate datasheet is limited. The table therefore uses conventional 2122 M typical values as the reference and identifies the structural differences against a 4.3 × 10^6 g/mol to 4.5 × 10^6 g/mol UHMW-PE grade.
| Parameter | Test method | 2122 M ECO-B expected | Conventional 2122 M typical | 4.5 × 10^6 g/mol UHMW-PE typical |
|---|---|---|---|---|
| Viscosity-average molecular weight | ISO 1628-3 | 2.2 × 10^6 g/mol | 2.2 × 10^6 g/mol | 4.3–4.5 × 10^6 g/mol |
| Density | ISO 1183-1 | 0.930–0.934 g/cm³ | 0.930–0.934 g/cm³ | 0.930–0.934 g/cm³ |
| Tensile yield stress | ISO 527-2 | 20–22 MPa | 20–22 MPa | 20–22 MPa |
| Tensile strain at break | ISO 527-2 | >300% | >300% | >300% |
| Notched Charpy impact | ISO 11542-2 | no break | no break | no break |
| Vicat softening temperature | ISO 306/A50 | 80°C | 80°C | 80°C |
In sliding wear, the lower-molecular-weight 2122 M grade typically exhibits a higher wear rate than 4.5 × 10^6 g/mol grades under identical sand-slurry conditions; the advantage of 2122 M is faster sintering response at lower compaction pressure and less die wear in ram extrusion. For wear strips in dry contact, laboratory ranking should be generated using the end-use load and speed rather than relying solely on molecular weight because boundary lubrication and counterface roughness can invert the ranking.
On production ram-extrusion lines, batch-to-batch variation in the sub-63 µm fines fraction has been observed to shift ram pressure by up to 5% at constant temperature and feed shoe stroke. This is not specific to the ECO-B grade but to milled UHMW-PE powders generally. Incoming powder should be sampled from each lot and tested for bulk density and particle size distribution before charging silos. The fine fraction controls dusting and packing density; it also determines the minimum ignition energy of a polyethylene dust cloud, which can fall below 30 mJ. Facility controls should follow ATEX Directive 2014/34/EU and the relevant dust explosion standard EN 60079-10-2 for hazardous area classification. Transfer lines should be grounded and inerted where high fines are generated.
The chemical resistance of 2122 M ECO-B follows the known UHMW-PE pattern. It resists dilute acids, alkalis, brines, and many polar solvents at temperatures below 60°C, but it is attacked by strong oxidising acids, free halogens, and certain chlorinated solvents at elevated temperature. Continuous load-bearing service is not recommended above 80°C because creep modulus declines and wear rate accelerates. Immersion testing under ISO 175 should be used to qualify the material for any continuous chemical exposure at the service temperature and stress state.
If a conversion is planned from a 4.3 × 10^6 g/mol grade to 2122 M ECO-B for food-contact guide rails, the lower molecular weight will reduce the sintering time required for a fully fused cross-section but may lower notched impact and wear life. The material must meet the extraction requirements of FDA 21 CFR 177.1520 for olefin polymers and the specific migration limits of EU 10/2011; these certifications are carried by the base UHMW-PE chemistry, but the mass-balance certification chain must be reviewed to confirm that the food-contact statement applies to the ECO-B variant. In practice, a first-article comparison under ISO 527-2 and ISO 11542-2 is recommended because published data for this specific configuration is limited.
The presence of the ECO-B suffix does not automatically transfer all conventional 2122 M regulatory clearances to the mass-balance grade in every jurisdiction. The table below lists the standard designations commonly associated with UHMW-PE grades in this molecular-weight class; end-use suitability remains application-specific.
| Requirement | Designation | Relevance to 2122 M ECO-B |
|---|---|---|
| Food-contact olefin polymer | FDA 21 CFR 177.1520 | Base polymer; verification required for ECO-B mass balance |
| Plastic food-contact migration | EU 10/2011 | Overall migration and specific migration limits |
| Monomer registration | REACH Regulation (EC) No 1907/2006 | Ethylene registration; polymer exemption applies |
| Heavy metal restrictions | RoHS Directive 2011/65/EU | Not expected above maximum concentration values |
| Material specification | ISO 11542-1 | UHMW-PE moulding and extrusion materials |
| Density test | ISO 1183-1 | Routine batch release |
| Bulk density | ISO 60 | Powder handling |
| Melt transition | ISO 11357-3 | DSC quality control |
| Tensile properties | ISO 527-2 | First-article validation |
| Impact properties | ISO 11542-2 | Notched Charpy validation |
Machining of sintered stock requires low cutting speed and adequate chip removal. Carbide or polycrystalline diamond tooling reduces surface fuzzing compared with high-speed steel. After rough machining, parts should be stress-relieved at 23°C for 24 h before finish passes because residual sintering stress causes dimensional movement. The grade is not a candidate for conventional screw extrusion or injection moulding because the entangled network cannot be made to flow without inducing chain scission. Standard melt-index instruments register no value under ISO 1133-1 at 190°C with 21.6 kg. For gel-spinning or microporous membrane processing, higher molecular weight grades in the 4 × 10^6 g/mol range are generally preferred because the chain network survives the high draw ratios required to develop oriented tensile properties. The 2122 M grade is used in pressed block and selected additive-compounded forms where a balance of processability and solid-state mechanical properties is required; however, any additive package containing metallic stearates or low-molecular-weight olefin waxes must be evaluated for changes in inter-particle diffusion and weld-line strength.