| HS Code | 484623 |
| Product Name | EQUATE HDPE EGDM-6888 |
| Polymer Type | High Density Polyethylene (HDPE) |
| Cas Number | 9002-88-4 |
| Density | 0.954 g/cm³ |
| Melt Flow Rate | 0.08 g/10 min (190°C/2.16 kg) |
| Melt Flow Ratio | 100 |
| Tensile Strength At Yield | 26 MPa |
| Elongation At Break | 600% |
| Flexural Modulus | 1100 MPa |
| Vicat Softening Point | 126°C |
| Environmental Stress Crack Resistance | >1000 h (100% Igepal) |
| Hardness | 65 Shore D |
| Melting Point | 130°C |
| Form | Pellets |
| Color | Natural |
As an accredited EQUATE HDPE EGDM-6888 factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | EQUATE HDPE EGDM-6888 is supplied in 25 kg polyethylene-lined woven bags on pallets, or 1,000 kg jumbo bags for bulk shipment. |
| Container Loading (20′ FCL) | EQUATE HDPE EGDM-6888 loaded in 25 kg bags, palletized, stretch-wrapped, and securely braced inside a 20′ FCL container for export. |
| Shipping | EQUATE HDPE EGDM-6888 is a non-hazardous high-density polyethylene resin, typically shipped in 25 kg bags, octabins, or bulk containers. Store in a cool, dry, ventilated area. Protect from moisture and direct sunlight. No special DOT, IMDG, or IATA dangerous goods classification applies. |
| Storage | Store EQUATE HDPE EGDM-6888 in a cool, dry, well-ventilated warehouse. Keep containers tightly closed, off the ground on pallets, and protected from direct sunlight, heat, moisture, and contamination. Avoid strong oxidizing agents and ignition sources. Prevent dust accumulation and static buildup. Use original packaging, store separately from incompatible materials, maintain good housekeeping, and follow local fire codes and the SDS. |
| Shelf Life | Typically two years when stored in original, sealed packaging in a cool, dry, well-ventilated area away from direct sunlight. |
EQUATE HDPE EGDM-6888 is specified for extrusion blow moulding of industrial, agrochemical, and intermediate bulk containers where the primary process variables are parison melt strength, resistance to slow crack growth, and dimensional stability under stacked transport loads. The resin is characterized by a nominal density of 0.954 g/cm³ when measured according to ISO 1183-1, and a high-load melt index in the 7–9 g/10 min range under ISO 1133-1:2022 at 190 °C/21.6 kg. That high-load melt index places the grade in the high-molecular-weight blow-moulding segment, where accumulator-head production of containers from 5 L to 220 L is feasible without excessive parison sag. On production-scale single-screw extruders with screw diameters between 60 mm and 120 mm and 24:1–30:1 L/D ratios, melt temperatures are maintained at 190–210 °C; higher settings reduce melt viscosity and increase the risk of thin-wall banding, while lower settings raise backpressure and generate unmelted gel particles at throughputs above 180 kg/h. Accumulator-head die temperatures should be held within 5 °C of the adapter temperature to avoid parison curl. Because high-density polyethylene is not hygroscopic, pre-drying is not required for resin taken directly from sealed packaging; however, cold pellets stored at ambient relative humidity above 60% can develop surface condensation that produces pinhead porosity in the pinch-off seam. A hopper purge with dry air is therefore required when condensation is visible. The addition of low-viscosity hydrocarbon waxes above 0.5 wt% is not recommended for this resin because those additives depress melt elasticity and increase parison sag in large-sheet parison configurations.
| Compliance domain | Standard or regulation | Relevant clause or method | Requirement for EGDM-6888 blow-moulded containers |
|---|---|---|---|
| US food-contact olefin polymers | 21 CFR 177.1520 | Paragraph (c) | Density not less than 0.94 g/cm³; extractable fraction limits depend on simulated food type and temperature conditions. |
| EU plastic food-contact materials | Regulation (EU) 10/2011 | Article 12, Annex II | Overall migration limit 10 mg/dm²; specific migration limits apply to additives used in the compound. |
| UN dangerous goods packaging | UN Model Regulations, 49 CFR 178.509 / 178.506 | Drop, stack, leakproofness | Container must pass drop at 0.6–1.2 m depending on filling level and density; stack 28 days at 40 °C without leakage. |
| REACH SVHC content | Regulation (EC) 1907/2006 | Article 33, Annex XVII | No SVHC above 0.1 wt% in supplied compound; restricted phthalates and heavy metals below Annex XVII limits. |
In extrusion blow moulding of 220-L tight-head drums, EGDM-6888 is processed on accumulator-head machines with die diameters in the 250–350 mm range and parison programming that ramps wall thickness from the top closure to the bottom chime. The limiting defect is pinch-off flash splitting at the bottom seam, where two semi-molten parison surfaces are welded under clamp force before blowing; insufficient melt temperature or excessive mould closing speed produces a cold weld line with low interdiffusion across the parison interface. On a two-platen shuttle press with clamp force above 800 kN, blow pressure is set at 0.7–1.0 MPa, and pinch-off bar temperature is held at 40–60 °C to prevent quench cracking in the flash. Wall thickness is controlled non-uniformly: the bottom chime is programmed to 3.5–4.5 mm, the sidewall to 2.0–2.8 mm, and the top shoulder to 3.0–3.5 mm because the top closure must withstand drop impact without distortion. Thickness distribution is verified by ultrasonic gauge with a minimum single-wall tolerance of 2.0 mm at the sidewall. Drop testing is performed under 49 CFR 178.509 with a 0.6 m drop height and 100% fill at −18 °C; the bottom chime must not show stress whitening or through-cracking. The high-molecular-weight tail of EGDM-6888 improves slow crack growth resistance at the pinch-off seam; however, the use of regrind above 30 wt% narrows the melt-temperature window and increases the incidence of parison sag under accumulator-head conditions.
Batch-to-batch variation in high-load melt index should be monitored because a shift of 0.5 g/10 min changes the parison elongation rate at the same die gap. Screw speed is normally set to 30–50 rpm on a 90 mm extruder, giving a melt pressure of 18–25 MPa at the die entrance; higher melt pressure indicates insufficient melt homogeneity or a blocked screen pack. The screen pack is normally 20/40/60 mesh to remove carbonized particles from recycled material. The base resin should meet environmental stress cracking resistance testing according to ASTM D1693-21, condition A, with F50 above 200 h in 100% Igepal CO-630; if F50 falls below 150 h, seam cracks are likely after UN stacking tests. For each batch of drums, a hydraulic proof test at 250 kPa internal pressure is common before top-handling impact evaluation.
For 15–20-L agricultural chemical jerry cans, the controlling process variable shifts from pinch-off integrity to resistance against cyclic internal pressure and stacking deformation. These containers are produced with an integrated handle pinch-off, and the handle attachment area must maintain a minimum wall thickness of 1.5–2.0 mm to prevent premature stress cracking when the container is subjected to repeated toggling between −5 °C and 35 °C. Mould closing speed and pinch bar temperature determine the degree of polymer orientation at the handle pinch; slow closing creates thicker flash but increases residual stress. The container is tested under ASTM D2463-20b drop impact using 3–5 specimens per cavity at 1.2 m drop height. The finished container must also pass UN packaging certification under 49 CFR 178.506 for stack pressure, which places a load of 400 kg over 28 days at 40 °C without yielding. EGDM-6888 provides a balance between swell ratio and die swell uniformity; the parison weight for a 15-L jerry can is normally 260–300 g, with a wall thickness of 1.2–1.5 mm over the sidewalls. The cap neck is normally compression moulded or injection moulded from a lower-melt-index HDPE, and the weld line of the neck insert carries a potential failure locus if insufficient melt temperature is applied at the insert.
Drop impact resistance of 25-L stackable carboys produced from EGDM-6888 is governed not only by base resin toughness but also by the residual stress distribution frozen into the sidewall during mould cooling. The ductile-to-brittle transition of high-density polyethylene in notched impact testing is typically below −40 °C, but moulded-in stresses can raise the apparent transition temperature to −10 °C or higher in the top shoulder and bottom chime. Carboys stored at sub-zero ambient temperatures must meet drop tests from 1.2–1.5 m at −18 °C with water or glycol-water mixture fills; the failure mode observed on production lines is usually a circumferential crack at the top shoulder where the parison was stretched over the blow pin. To reduce this risk, the blow pin is heated to 60–80 °C, and mould cooling water temperature is set at 10–15 °C for the pinch-off and chime areas while the sidewall is cooled at 20–25 °C. The resulting crystallinity gradient reduces residual stress at the shoulder. Impact testing is supplemented by ISO 6603-2 puncture impact at −20 °C and by slow crack propagation evaluation according to ISO 16770 with a notch depth of 1.0 mm. Published data for EGDM-6888 under ISO 16770 is limited, so container-level drop testing remains mandatory.
Batch-to-batch variation in comonomer distribution affects low-temperature impact response more than high-load melt index variation. Processors should request a comonomer type and distribution statement from the supplier; for EGDM-6888, the high-molecular-weight fraction is the main carrier of short-chain branching, which controls tie-molecule density. When regenerated material is added above 20 wt%, tie-molecule population is reduced by chain scission in the high-molecular-weight fraction, and low-temperature drop failures become more frequent even when high-load melt index and density remain within specification. A practical control limit is to keep regrind particle size above 8 mm and to screen out fines below 3 mm before re-extrusion. Container wall thickness at the shoulder of a 25-L carboy is normally held at 2.0–2.5 mm; if the shoulder thins below 1.8 mm, impact failure probability increases non-linearly under sub-zero conditions.
Multi-parison extrusion blow moulding of 5-L narrow-neck bottles places a different demand on EGDM-6888: uniform parison length and thickness across two to four cavities. On a rotary wheel machine with 4 to 8 stations, the parison drop time is shorter than in accumulator-head processing, and the melt must retain enough elasticity to resist sag during the transfer step. Melt temperature is set at 200–215 °C, slightly higher than in large drums, to ensure flow through the manifold fills all die heads at equal pressure. Die gap is usually 1.0–1.5 mm, and parison programming adjusts each cavity to compensate for manifold pressure drop. The main processing defect is unequal shot weight; a variation above 2% between cavities produces thin-wall areas that can fail leak testing at 30 kPa internal pressure. Because the bottle dimension is small, mould closing speed is high and the pinch-off line is narrow; this requires a resin with a controlled melt flow ratio between 190 °C/5 kg and 190 °C/21.6 kg to maintain melt strength. Drop impact for these bottles is normally conducted at 1.5 m on the flat side and the bottom seam at 23 °C according to ASTM D2463-20b.
In coextruded barrier containers for solvent-based agrochemicals or industrial fluids, EGDM-6888 serves as the structural high-density polyethylene layer, while a polyamide or EVOH barrier layer provides reduced solvent permeation. The process is more demanding than monolayer because the parison consists of 3–6 layers with different melt viscosities and because interfacial instabilities produce layer breakup or weld line separation. The HDPE skin layer is set to 50–70% of total wall thickness, with tie layers at 4–8% each and the barrier layer at 3–8% depending on the target permeation rate. Melt temperature of EGDM-6888 in this coextrusion is held at 200–210 °C, while the barrier layer is run at its own recommended temperature; the die head must be designed for layer thickness programming over a parison length of 0.8–1.2 m. Published data for EGDM-6888 specifically in EVOH coextruded structures is limited; processors should verify layer adhesion on a pilot line before committing to full moulds. The main HDPE-related failure mode is parison sag in the centre of the drop, which thins the HDPE outer layer and exposes the barrier layer to impact damage. A wall-thickness profile that increases sidewall thickness to 1.8–2.2 mm reduces this risk. Permeation testing uses ASTM D3985 or DIN 53380-3 depending on the target chemical.
For 1000-L intermediate bulk container inner bottles, the processing window for EGDM-6888 is defined by parison programming across a drop length of 1.5–2.0 m and by the need for a uniform sidewall thickness near 3.0–4.0 mm. The bottle is typically moulded as a one-shot blown liner on a large-platen shuttle press with clamp force above 2500 kN, and mould cooling water is maintained at 8–15 °C to obtain a cycle time near 180–240 s. The main defect is localised thinning at the top corner radius where the parison stretches before contact with the mould; this area is programmed to 4.5–5.5 mm using a 50-point parison programmer. After moulding, the liner must pass a leak test at 20 kPa and a hydraulic burst test above 350 kPa. Because the liner is later placed inside a galvanised steel frame, surface damage from folding or insertion can initiate slow crack growth; resistance to that damage is evaluated by environmental stress cracking resistance on notched specimens according to ASTM D1693-21, condition A, with an F50 above 500 h being desirable. Regrind content is normally limited to 10–15 wt% for intermediate bulk container liners because of the thickness and long-term contact with aggressive chemicals.
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EQUATE HDPE EGDM-6888 is a high-density polyethylene resin produced by EQUATE Petrochemical Company for injection molding of thin-walled packaging, closures, housewares, and industrial pails. The grade is specified by a nominal melt flow rate of 8.0 g/10 min under ISO 1133-1:2022 at 190 °C and 2.16 kg, and a nominal density of 0.956 g/cm³ under ISO 1183-1:2019. These two properties place the material in the medium-flow segment of high-density polyethylene, between fractional-melt blow molding grades and very high-flow thin-wall injection molding grades.
The melt flow rate controls injection pressure and fill time in multicavity tools, while the density affects flexural stiffness, mold shrinkage, and permeability. Because EGDM-6888 carries a density near 0.956 g/cm³, it is classifiable as a high-density polyethylene rather than a medium-density polyethylene; the higher density contributes to a higher flexural modulus and greater top-load strength in finished closures and containers compared with linear low-density polyethylene at equivalent wall thickness.
The resin is supplied as pellets and is suitable for natural, white, and color masterbatch production on conventional single-screw injection molding machines. Application performance is not established by pellet property data alone; gate location, wall thickness distribution, cooling rate, and weld line formation in the molded article alter the crystalline morphology and the resulting mechanical response.
Since the melt flow rate is measured at 190 °C and 2.16 kg, it does not describe the full shear-thinning response encountered in injection molding. Cavity filling occurs at shear rates commonly above 1000 s⁻¹, where the effective viscosity of the high-density polyethylene is substantially lower than the low-shear value implied by MFR. If a tool requires precise pressure drop prediction, a capillary rheometer curve under ISO 11443 should be generated on production lot material, because catalyst residues, molecular weight distribution, and additive package influence the shear sensitivity.
Published datasheet values are summarized in Table 1. These values are generated on molded specimens conditioned under ISO 291:2008 at 23 °C ± 2 °C and 50% ± 5% relative humidity for at least 40 hours. They are engineering values for short-term mechanical performance and are not to be used as long-term design allowables.
| Property | Nominal value | Test method |
|---|---|---|
| Melt flow rate | 8.0 g/10 min | ISO 1133-1:2022, 190 °C / 2.16 kg |
| Density | 0.956 g/cm³ | ISO 1183-1:2019 |
| Tensile yield stress | 26.0 MPa | ISO 527-2:2012, 50 mm/min |
| Flexural modulus | 1100 MPa | ISO 178:2019, 2 mm/min |
| Notched Izod impact strength, 23 °C | 4.0 kJ/m² | ISO 180:2020 |
| Vicat softening temperature | 126 °C | ISO 306-A50 |
| Shore D hardness | 65 | ISO 868:2003 |
The tensile yield stress is the first point on the stress-strain curve where strain increases without an accompanying increase in stress. The flexural modulus is a short-term secant modulus measured under three-point bending; long-term creep resistance requires separate testing under the application load and temperature. Notched Izod impact strength is a bulk plaque measurement and does not account for weld lines, gate blush, sharp corners, or frozen-in stress in deep-draw parts.
Heat deflection temperature data for EGDM-6888 under ISO 75-2/B is limited in the published literature. High-density polyethylene grades with a density of 0.956 g/cm³ and a melt flow rate in the 7–9 g/10 min range typically exhibit heat deflection temperatures near 70–80 °C at 0.45 MPa, but hot-fill or hot-contact applications require a separate assessment of part deformation under the specific thermal profile rather than reliance on the neat resin value.
On a production injection molding machine with a single screw having an L/D ratio of 20:1 to 24:1 and a compression ratio of 2.5:1 to 3.0:1, EGDM-6888 is processed at melt temperatures of 200–240 °C measured at the nozzle. Barrel temperatures are normally set with a rising profile from rear to front: 180–200 °C in the feed zone, 200–230 °C in the compression zone, and 220–240 °C in the metering zone. Mold temperature is maintained at 15–40 °C with turbulent water flow. Lower mold temperatures shorten cycle time, while higher mold temperatures improve surface finish and reduce frozen-in stress in flat lids.
At ambient relative humidity below 60%, pre-drying is not required because high-density polyethylene is not hydroscopic. However, resin stored in outdoor silos or exposed to rapid temperature swings can accumulate surface condensation. In that case, drying at 70–80 °C for 2–3 hours is applied before the resin enters the feed throat. Surface moisture is capable of generating splay and surface voids in thin wall sections, although the saturated polyethylene backbone is not subject to hydrolytic degradation.
Thin-wall packaging with nominal wall thicknesses of 0.6–1.0 mm requires low melt viscosity to fill the cavity before freeze-off. EGDM-6888 provides a higher melt flow rate than fractional-melt HDPE grades used in blow molding and large-part injection molding. The higher MFR reduces cavity pressure demand at equivalent fill time, which is particularly useful in multicavity hot-runner tools where pressure balancing across gates is critical. However, exact pressure reduction is tool-specific and is governed by gate diameter, runner geometry, mold temperature, and injection speed. Published universal values for EGDM-6888 cavity pressure drop are not available; validation on the target production tool is required.
Table 2 presents a recommended starting window for injection molding the grade. The values are not absolute process guarantees; they require optimization because barrel capacity, screw geometry, and nozzle design shift the effective melt temperature.
| Parameter | Recommended range | Measurement point |
|---|---|---|
| Melt temperature | 200–240 °C | Nozzle thermocouple or infrared pyrometer |
| Mold temperature | 15–40 °C | Mold surface at cavity wall |
| Rear barrel zone | 180–200 °C | Furthest from nozzle |
| Middle barrel zone | 200–230 °C | Compression zone |
| Front barrel zone | 220–240 °C | Metering zone |
| Back pressure | 0.5–1.5 MPa | Hydraulic or electric screw drive |
| Screw surface speed | 0.2–0.5 m/s | Peripheral screw speed |
Screw surface speeds above 0.5 m/s can generate shear heating that raises melt temperature beyond the barrel setpoint, causing yellowness and odor. Melt temperatures below 200 °C may leave unmelted pellets in the metering zone when recovery times are short. A mold temperature of 15 °C is acceptable for simple geometries but can create excessive differential shrinkage in parts with abrupt thick-to-thin transitions; mold temperatures of 30–40 °C are preferred for warpage-sensitive flat lids. Gate seal time should be established by incrementally increasing hold pressure time and weighing the part until a plateau is achieved; for a 1.0 mm wall section at 20 °C mold temperature, gate seal often occurs at 2–4 seconds, but the value is gate-diameter dependent.
Compared with a notional high-density polyethylene blow molding grade having an MFR of 0.30 g/10 min under ISO 1133-1, EGDM-6888 has a substantially lower melt viscosity and a shorter molecular weight distribution tail. The processing consequence is improved flow length and lower injection pressure. The mechanical trade-off is a reduction in environmental stress crack resistance as measured by ASTM D1693 or ISO 22088-2, and a reduction in notched impact strength. This relationship is governed by the inverse dependence of ESCR on melt flow rate for high-density polyethylene and is not specific to EGDM-6888.
Against a lower-flow injection molding HDPE with an MFR near 0.7 g/10 min, EGDM-6888 permits shorter fill times at identical wall thickness but may show lower weld-line strength. Applications with heavy thread loading in closures or repeated snap-fit assembly therefore require weld-line testing under ISO 19095-2 or equivalent, because the bulk notched Izod value does not capture the morphological discontinuity at the weld line.
Against a linear low-density polyethylene grade with a density near 0.920 g/cm³, EGDM-6888 offers higher flexural modulus and lower oxygen and water vapor transmission at equivalent thickness, but lower puncture and impact resistance. The higher density also increases part weight at the same cavity volume, which can be a cost and logistics consideration. Against a medium-density polyethylene with a density near 0.934 g/cm³, EGDM-6888 has higher top-load strength but lower ESCR under fatty or alcoholic environments.
When evaluated as a replacement for a high-flow polypropylene injection molding grade, EGDM-6888 offers lower processing temperature and lower flexural modulus. It is not a direct substitute in parts designed for polypropylene shrink characteristics; high-density polyethylene of this density typically exhibits higher mold shrinkage than polypropylene, and the dimensional allowance must be adjusted before cavity cutting. Published product-specific shrinkage data under ISO 294-4 for EGDM-6888 is limited; tooling decisions should use test mold data under the intended gate configuration.
Melt temperatures above 260 °C or residence times longer than 15 minutes at those temperatures can initiate chain scission and lead to viscosity reduction, yellowing, and odor. The grade should not be combined with acid-functional additives that attack catalyst residues or with excessive amide slip additives that can migrate to the mold surface and generate plate-out. For colored applications, dispersive mixing capability is more important than the resin choice; high color masterbatch loadings above 4 wt% should be evaluated for screw recovery time and color homogeneity.
For food-contact applications, the final article must comply with FDA 21 CFR §177.1520 and, where applicable, EU Regulation 10/2011 with the intended food simulants and temperature conditions. The olefin polymer may be covered by the regulation, but the converter is responsible for verifying that additives, colorants, and contamination from the production line do not violate migration limits. REACH and RoHS compliance must be confirmed from supplier documentation for the finished component, as compositional data for the resin pellet does not automatically cover the final article.
In sub-zero drop impact applications, full-article testing under the target distribution protocol is required rather than extrapolation from plaque notched Izod values. The ranking of EGDM-6888 against other HDPE grades in such tests is sensitive to part thickness, gate location, and cooling rate; published comparative data for this specific product under sub-zero container drop conditions is limited.