| HS Code | 748864 |
| Density | 0.93 g/cm³ |
| Bulkdensity | 0.45 g/cm³ |
| Averageparticlesize | 150 µm |
| Molecularweight | 10.5 × 10^6 g/mol |
| Viscositynumber | 2400 ml/g |
| Meltingpoint | 135 °C |
| Crystallinity | 50% |
| Tensilemodulus | 700 MPa |
| Tensilestrengthatbreak | 17 MPa |
| Elongationatbreak | >300% |
| Charpynotchedimpactstrength | no break |
| Waterabsorption | <0.01% |
| Coefficientoffriction | 0.15 |
| Shoredhardness | 60 |
| Thermalconductivity | 0.41 W/mK |
| Chemicalresistance | excellent to acids, alkalis, and solvents |
| Biobasedcarboncontent | 100% |
As an accredited Celanese UHMW-PE 4022 ECO-B factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | Celanese UHMW-PE 4022 ECO-B comes in 25 kg moisture-resistant paper bags, palletized for industrial handling and storage. |
| Container Loading (20′ FCL) | 20′ FCL container loading: Celanese UHMW-PE 4022 ECO-B bags are palletized, shrink-wrapped, evenly distributed, and properly secured for ocean transport. |
| Shipping | Celanese UHMW-PE 4022 ECO-B is shipped as a non-hazardous, solid polyethylene resin, typically in moisture-resistant bags, drums, or bulk containers. It is not classified as dangerous goods for DOT, IMDG, or IATA transport. Keep dry, clean, and away from ignition sources; use standard industrial handling. |
| Storage | Store Celanese UHMW-PE 4022 ECO-B in a cool, dry, well-ventilated area, away from direct sunlight, heat, flames, and strong oxidizing agents. Keep containers sealed to prevent moisture, dust, and contamination. Avoid prolonged UV exposure. Maintain clean, labelled packaging; stack securely to prevent deformation. No special temperature control is normally required, but follow supplier SDS and local regulations. |
| Shelf Life | Celanese UHMW-PE 4022 ECO-B has no finite shelf life if stored dry in original packaging, away from direct sunlight and excessive heat. |
On a continuous wet-process lithium-ion battery separator casting line equipped with a co-rotating twin-screw extruder at L/D 48 and a 40 µm sintered metal melt filter, Celanese UHMW-PE 4022 ECO-B is metered into paraffin oil at 20–25 wt% of the total blend, with gravimetric dosing maintained within ±0.2 wt% per hopper. The powder feed hopper is padded with dried air at a dew point below −20 °C, because moisture uptake above 150 ppm increases the gel-particle population in the cast film and shortens melt-filter service intervals. The compliance architecture for this segment includes IATF 16949:2016 clause 8.5.1.1 for process control plans, ISO 9001:2015 clause 8.5.1 for production control, and end-product testing under ASTM D882-18 for tensile strength at 5–25 µm film thickness, ASTM D792-20 for density-based porosity, ASTM F316-03 for bubble-point pore size, and TAPPI T460 for Gurley air permeability; automotive cell suppliers typically add IEC 62660-3:2016 for mechanical abuse and UN 38.3 for transport safety at pack or cell level. The extrusion compound is processed at 160–180 °C through a T-die onto a chilled casting drum held at 25–40 °C, followed by sequential stretching at machine-direction ratios of 5:1–8:1 and transverse-direction ratios of 5:1–9:1. Paraffin oil is then extracted with methylene chloride or n-heptane to a residual level of ≤0.1 wt%, heat-set at 100–130 °C, and slit into separators for prismatic, cylindrical, and pouch lithium-ion cells in electric vehicle, energy-storage, and consumer electronics packs. Because solvent recovery capacity and residual metal particle counts above 25 µm are recurring rejection points on full-scale lines, the powder lot must be screened for coarse particles and the extraction bath solvent ratio controlled within ±3% by weight; published data specific to 4022 ECO-B in this exact separator configuration is limited, so the loading window is typically transferred from UHMWPE grades of 2–6 million g·mol⁻¹ molecular weight during line qualification.
| Segment | Standard | Property or test | Clause or method |
|---|---|---|---|
| Wet-process separator | IATF 16949:2016 | Production control plan | 8.5.1.1 |
| Wet-process separator | ASTM D882-18 | Tensile strength of thin film | Test method |
| Wet-process separator | ASTM F316-03 | Bubble-point pore size | Test method |
| Gel-spun fibre | NIJ Standard-0101.07 | Ballistic resistance | Test method |
| Gel-spun fibre | EN 388:2016 | Cut-resistant glove performance | Test method |
| Sintered porous part | ISO 2738:1999 | Density and open porosity | Test method |
| Sintered porous part | ISO 4003:1977 | Bubble-point pore size | Test method |
| Food-contact ram extrusion | FDA 21 CFR 177.1520 | Olefin polymer food contact | (c) |
| TIPS membrane | NSF/ANSI 61 | Drinking water system component | Test method |
When decalin-based spin dope enters a gear-pump-controlled spinneret at 130–145 °C, 4022 ECO-B is already dissolved at 7–10 wt% polymer solids in high-boiling paraffin oil/decalin after antioxidant addition at 0.1–0.5 wt% of the polymer mass. The solution is prepared in an inerted high-shear dissolving vessel, filtered through a 20–50 µm depth pack, and forced through a spinneret of 500–1,000 holes into a water/ethanol quench bath held at 5–15 °C to fix the gel state; the air gap between die face and bath, typically 5–20 mm, controls surface oxidation and filament coalescence. After solvent extraction and drying, the gel yarn is hot-drawn in multiple stages at 140–150 °C to total draw ratios of 30:1–60:1, which raises modulus and tenacity while reducing residual solvent below 0.05 wt%. The downstream product profile includes continuous filament yarn converted into uni-directional laminate layers, cut-resistant sleeves, offshore mooring ropes, slings, and fishing line; material acceptance is normally anchored to ASTM D885-16 for tensile properties, EN 388:2016 for cut-resistant glove performance, and NIJ Standard-0101.07 for ballistic panel subassemblies. Because oxygen concentration above 0.5 vol% in the drying and drawing tunnels produces surface oxidation and measurable tenacity loss, the line must maintain nitrogen blanketing and solvent-recovery pressure control; published data for 4022 ECO-B in this specific draw ratio and solvent system is limited, so first-article qualification against a reference UHMWPE grade is used to establish the operating band.
Manufacture of porous filter tubes and fluidizing plates from 4022 ECO-B uses free-sintering compression molds in which powder is filled to a specified bulk density and heated to 200–220 °C under 3–10 MPa hydraulic compaction. The base charge is 100 wt% virgin powder; clean regrind from downstream machining is limited to 10–20 wt% and must be re-screened to maintain particle size distribution within 90–250 µm because broader fractions create bimodal pores and reduce bubble-point pressure. The sintered body is heated at 4–6 K·min⁻¹, held at peak temperature for 30–90 min, and cooled at 2–4 K·min⁻¹ to avoid internal shrinkage cracks. Pore structure is inspected against ISO 2738:1999 for open porosity, ISO 4003:1977 for bubble-point pore size, and ASTM D792-20 for density; food-contact grades are evaluated under FDA 21 CFR 177.1520(c) and EC 1935/2004 Article 3 for overall migration. Converted parts include aerator diffusers, sparging stones, silencer discs, and fluidizing plates used in water treatment, chemical process filtration, and powder handling. Because sintered UHMWPE is thermally constrained above 220 °C and oxidation-sensitive in prolonged air heating, the mold must be sealed or purged with inert gas during the hold period, and regrind-lot bubble-point testing is mandatory since published data for 4022 ECO-B with this exact regrind level is limited.
Food-processing conveyor line components are manufactured by ram extrusion from 4022 ECO-B powder pre-dried at 80–100 °C for 2–4 h when ambient relative humidity exceeds 60%, since residual moisture forms steam porosity in the consolidated rod. The ram extrusion barrel is held at 200–230 °C and the reciprocating ram compresses the powder at 20–40 MPa, producing continuous rod, plate, or profile that is cut to length after slow cooling. The formulation is 100 wt% 4022 ECO-B; a food-compliant colour masterbatch may be used at ≤3 wt% only when the carrier resin is an olefin polymer conforming to FDA 21 CFR 177.1520(c). Compliance documentation for this segment is anchored to FDA 21 CFR 177.1520(c), EC 1935/2004 Article 3, and NSF/ANSI 51-2019 for food equipment materials. Finished components include chain guides, wear strips, star wheels, guide rails, and bottle-handling parts used in beverage, bakery, and packaging lines. Because ram extrusion consolidates powder without plasticating shear, the process cannot disperse high filler loadings or moisture-tolerant regrind above 20 wt%, and the lot certificate must document the ISCC PLUS mass-balance attribute of the ECO-B grade separately from the food-contact compliance statement.
Water-treatment flat sheets are produced by thermally induced phase separation, in which 4022 ECO-B is compounded with a high-boiling diluent at 20–35 wt% polymer, extruded through a flat die at 180–210 °C, cooled on chill rolls to induce liquid-liquid or solid-liquid phase separation, and passed through solvent extraction to remove the diluent. The resulting membrane is heat-set at 100–120 °C and surface-treated for hydrophilicity, with pore-size distribution measured by ASTM F316-03 and tensile properties by ASTM D882-18. Drinking water contact parts are supplied under NSF/ANSI 61 and ISO 9001:2015, with extractables testing performed according to the end-user’s potable water certification scheme. The finished product range includes membrane bioreactor flat sheets, potable-water microfiltration elements, and industrial wastewater or chemical recovery membranes with pore-size classes from 0.01 µm to 0.4 µm. Because the TIPS process depends on diluent solubility and cooling-rate control, the extruder barrel must maintain dissolved oxygen below 0.5 vol% and the chill-roll temperature within ±2 °C; amine-based wetting agents are avoided due to extractables risk. Published data for 4022 ECO-B in this specific TIPS configuration is limited, so membrane qualification requires a diluent-solubility and cooling-rate screening on a pilot flat-die line before production scale-up.
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Celanese UHMW-PE 4022 ECO-B is an ultra-high-molecular-weight polyethylene powder supplied as a bio-attributed grade through a mass-balance allocation. The base resin is a homopolymer with a nominal molecular weight of 4.0 × 10⁶ g/mol; because the melt does not flow under standard melt-flow test conditions, the grade is specified by solution viscosity in ISO 1628-3 rather than by melt flow rate. The material is intended for ram extrusion and compression moulding of wear parts, guide rails, bearing segments, chain wear strips, star wheels, and hopper linings. Compression-moulded sheet from this grade is characterised by density in the 0.930–0.940 g/cm³ range under ISO 1183-1, tensile yield stress in the 20–22 MPa range under ISO 527-2, and double-notched Charpy impact behaviour that produces no break at 23°C under ISO 11542-2. The ECO-B designation does not denote a polymer composition change; it indicates bio-circular or renewable feedstock accounting assigned to the ethylene stream.
Differential scanning calorimetry under ISO 11357-3 places the crystalline melting peak between 130°C and 135°C. The bio-attributed monomer does not shift this peak because the polymer backbone is identical to fossil-based polyethylene. Sintering in ram extrusion and compression moulding requires plate or barrel temperatures of 190°C to 220°C. Below 190°C, interparticle diffusion is incomplete and a white, porous core is observed in sections greater than 40 mm. Above 220°C, oxidative chain scission dominates; published oxidation induction time data for this specific ECO-B configuration is limited, so end users should run ISO 11357-6 OIT verification on incoming powder batches. The powder particle size distribution influences sintering uniformity. Laser diffraction data for the 4022 series typically show a median particle size of 120–180 µm, with fines below 63 µm controlled to maintain hopper flow. The bio-attributed grade is blended to the same particle-size specification as fossil 4022, which permits direct replacement on existing production lines without altering compaction ratio or feed auger geometry.
On single-ram extruders with 50–120 mm barrel diameters and effective length-to-diameter ratios of 20:1 to 30:1, the barrel is divided into feeding, compaction, and sintering zones. The powder is compacted at room temperature, then sintered in a heated die land. Industrial machine set-points are usually 180°C to 230°C. If the sintering zone exceeds 230°C for more than 20 min, the surface of the extrudate develops yellowing and melt fracture, and the elongation at break measured on the finished profile can fall below 200%. The process window around the optimum set-point is typically ±5°C. Throughput is controlled by cycle rate and back-pressure rather than screw speed. On a 63 mm single-ram machine, profiles with cross-sections between 500 mm² and 3 000 mm² typically run at 5–15 kg/h. Feed bridging occurs when powder bulk density falls outside 0.40–0.45 g/cm³; vibratory hoppers and storage at 20–25°C are used to maintain consistent flow. Condensation on cold powder exposed to relative humidity above 60% can create steam pitting in the sintered product, so pre-conditioning of the powder is specified when silo discharge temperature is below the dew point.
The following values are representative of compression-moulded sheet produced from 4022 ECO-B; they are not batch-level specification limits.
| Density | ISO 1183-1 | 0.930–0.940 g/cm³ |
| Viscosity number | ISO 1628-3 | 2800–3200 mL/g |
| Tensile yield stress | ISO 527-2 | 20–22 MPa |
| Nominal tensile strain at break | ISO 527-2 | >300% |
| Double-notched Charpy impact | ISO 11542-2 | no break at 23°C |
| Shore D hardness | ISO 868 | 60–65 |
| Crystalline melting peak | ISO 11357-3 | 130–135°C |
The crystalline superstructure of 4022 ECO-B after slow cooling produces a Shore D hardness of 60–65. The polymer has a dynamic coefficient of friction against polished steel of approximately 0.10–0.20 under dry sliding conditions; the coefficient rises when wet or when stainless steel is replaced with carbon steel. In sand-slurry abrasion testing under ISO 15527, UHMW-PE grades of this molecular weight generally exhibit volume loss between 75 mm³ and 100 mm³, but the exact value depends on abrasive particle angularity and test duration. The ECO-B bio-attribution does not alter the crystalline lamellar thickness or the wear mechanism, which is micro-ploughing and fatigue delamination. On production lines, the wear rate of 4022 ECO-B guide rails is highest during the first 50 h of operation as the surface skin is removed, after which the wear rate stabilises. This burn-in behaviour is identical to fossil 4022 and should be accounted for in dimensional inspection schedules.
Compared with fossil-based 4022, the ECO-B grade exhibits no statistically measurable shift in tensile yield stress, Shore D hardness, or double-notched Charpy impact. The bio-attribution is an accounting property, not a mechanical one. Compared with lower-molecular-weight UHMW-PE grades intended for screw plasticating and injection moulding, 4022 ECO-B has higher abrasion resistance and higher impact toughness but cannot be injected because the melt viscosity is outside the range of conventional injection units. Compared with higher-molecular-weight GUR grades such as GUR 4150, 4022 ECO-B shows a lower sintering viscosity, which improves core consolidation in thick sections above 80 mm; the trade-off is a slightly lower three-body abrasion resistance under ISO 15527 sand-slurry conditions. Published data for this specific grade configuration is limited, but the relative ranking of molecular weight and slurry wear resistance is consistent with the UHMW-PE literature. A direct replacement of fossil 4022 with 4022 ECO-B on a ram extrusion line does not require tooling changes or new temperature profiles when bulk density and particle-size distribution are within the same specification band.
Machining of 4022 ECO-B sheet and rod is performed with carbide or polycrystalline diamond tooling at surface speeds of 200–400 m/min, with air cooling to prevent local melting. Thermal expansion is approximately 1.5 × 10⁻⁴ K⁻¹, roughly one order of magnitude higher than structural steel; bearing clearances must be designed to accommodate this movement. Creep under load occurs at room temperature, so clamping forces should be distributed over large washers or metal backup plates.
The ECO-B grade is positioned within an ISCC PLUS-certified mass-balance accounting framework. Renewable or bio-circular feedstock is allocated to the ethylene cracker, and the attribution is transferred to the polyethylene powder. The final polymer is not necessarily composed molecule-for-molecule of renewable-carbon monomers; the mass-balance system assigns a defined portion of the output to the bio-attributed product. Under REACH, polyethylene is exempt from polymer registration under Article 2(9), while monomers and additives must be registered. The grade is typically below the maximum concentration values in RoHS 2011/65/EU for lead, mercury, cadmium, hexavalent chromium, PBB, and PBDE when unfilled. Food-contact suitability must be verified by the converter against 21 CFR 177.1520 or EU 10/2011; the ECO-B designation does not automatically confer food-contact status. The bio-attributed feedstock should not be confused with biodegradability; UHMW-PE 4022 ECO-B is not biodegradable under ambient or marine conditions.
| REACH polymer exemption | Article 2(9) |
| RoHS restricted substances | 2011/65/EU |
| US food-contact olefin polymer | 21 CFR 177.1520 |
| EU plastic food-contact | EU 10/2011 |
| Bio-circular mass balance | ISCC PLUS |
Compression moulding of 4022 ECO-B requires platens heated to 190–210°C, consolidation pressure of 5–10 MPa on the projected part area, and controlled cooling below 0.5 K/min through the crystallisation range from 120°C to 80°C. Cooling too rapidly produces warpage and residual stress. Thick-section parts above 100 mm require extended dwell to avoid core porosity, but residence times longer than 30 min at 220°C should be avoided because chain degradation reduces elongation at break. Conventional single-screw plasticating extruders are not suitable for this grade; the powder does not form a continuous melt pump, and screw friction can generate local temperatures above 280°C. Pigments and fillers such as graphite, carbon black, or glass powder can be dry-blended before sintering at loadings up to 10 wt%, but their presence increases internal friction and lowers double-notched Charpy impact. Amine-based additives and metal stearates are not required for this polyolefin and can exude to die surfaces during long ram-extrusion runs; they should be avoided unless supported by compatibility data.