| HS Code | 957382 |
| Density | 0.946 g/cm³ |
| Melt Flow Rate | 13 g/10 min (190°C, 2.16 kg) |
| Tensile Yield Strength | ≥24 MPa |
| Elongation At Break | ≥500% |
| Flexural Modulus | ≥900 MPa |
| Notched Izod Impact Strength | ≥40 kJ/m² |
| Vicat Softening Temperature | ≥120°C |
| Melting Point | 130-135°C |
| Brittleness Temperature | ≤ -70°C |
| Hardness | ≥60 Shore D |
| Water Absorption | <0.01% |
| Heat Deflection Temperature | ≥75°C (0.45 MPa) |
| Volume Resistivity | >10^16 Ω·cm |
| Dielectric Strength | ≥20 kV/mm |
| Ul Flammability | HB |
As an accredited Sinopec Maoming HDPE 4613 factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | Sinopec Maoming HDPE 4613 packaging: 25 kg PP woven bags, palletized and stretch-wrapped for industrial shipment. |
| Container Loading (20′ FCL) | 20' FCL loaded with Sinopec Maoming HDPE 4613 resin, 25 MT in 25 kg bags, palletized, shrink-wrapped, securely stowed and sealed. |
| Shipping | Sinopec Maoming HDPE 4613 is shipped as a non-hazardous thermoplastic in 25 kg woven bags or 1000 kg jumbo bags, palletized and stretch-wrapped. It is transported by truck or sea freight in 20-/40-foot containers. Store dry, cool, ventilated, away from direct sunlight, moisture, and ignition sources. |
| Storage | Store Sinopec Maoming HDPE 4613 in a cool, dry, well-ventilated area, away from direct sunlight, heat, flames, and strong oxidizers. Keep original bags sealed and palletized off the floor. Avoid moisture, contamination, and prolonged UV exposure. Store at ambient temperature. Do not stack excessively. Use first-in, first-out inventory. Follow supplier SDS and local regulations. |
| Shelf Life | Sinopec Maoming HDPE 4613 typically has a 24-month shelf life when stored cool, dry, ventilated, and away from direct sunlight. |
Sinopec Maoming HDPE 4613 is positioned as an extrusion blow-molding high-density polyethylene for rigid hollow articles; open literature on this specific grade is limited, so the operating windows cited below are drawn from fractional-melt HDPE blow-molding practice and require confirmation against the batch certificate of analysis. On a twin-station shuttle machine with a 65 mm barrier screw at L/D 25:1, production of 750 mL to 2 L household detergent bottles typically uses feed-zone temperatures of 170–175°C, mid-barrel temperatures of 185–195°C, and a die-head set point of 200–205°C. The die tooling is configured with a converging flow channel, a die-pin land length ratio of 18:1–22:1, and a die gap of 1.2–1.8 mm; these dimensions control parison swell, which for low-melt-index HDPE is commonly 10–30% depending on shear rate and die-head pressure. A parison programmer with at least 20 points is applied because detergent bottles of 150–250 mm height develop wall thinning at the shoulder and pinch-off zones when a constant parison profile is used. Blow air pressure is maintained between 0.55 MPa and 0.75 MPa, and chilled mold water is held at 10–15°C to reduce sink marks and keep cycle time below 18 s on a single-cavity 1 L bottle. For bleach-containing products with 4–6% sodium hypochlorite, the clean plant regrind level is capped at 20 wt% because higher regrind fractions have been observed to accelerate environmental stress cracking on production-scale bottle drop tests. ESCR acceptance is evaluated according to ASTM D1693 Condition B using 10% Igepal CO-630 at 50°C, with a commonly imposed threshold of ≥24 h for detergent bottles. Final bottle weights are controlled to ±0.5 g on a 1 L container. EU/REACH compliance is addressed through the resin’s SVHC screening and through the downstream packaging article’s conformity to the Packaging and Packaging Waste Directive; food-contact declarations are not assumed because the household detergent application does not require FDA 21 CFR 177.1520 or EU 10/2011, but export documentation may still request them.
Tall oval shampoo and conditioner bottles in the 300–500 mL range expose the 4613 melt to high gravitational stress because the parison hang time on a single-station continuous extrusion blow molder frequently exceeds 6 s when the part length-to-width ratio is above 3:1. With a 45 mm grooved-feed extruder at L/D 24:1, melt temperature at the die exit is held at 195–200°C; raising the head above 205°C reduces melt viscosity and increases sag, while lowering below 185°C raises die-head pressure above 25 MPa and triggers melt fracture on the bottle surface. The parison programmer is set with 30–40 control points, increasing wall thickness at the bottom tail and shoulder zones to 1.2–1.4 mm while holding the central body at 0.7–0.9 mm after blow-up. A die gap of 1.0–1.4 mm with a blow-up ratio of 2.2:1–2.8:1 is used, and mold temperature is controlled at 8–12°C with turbulent chilled water flow to freeze the high-gloss surface before shrinkage produces orange-peel defects. Color is introduced as 2 wt% white or pearl masterbatch in a polyethylene carrier; masterbatch selection is restricted to carriers with melt flow rate below 4 g/10 min at 190°C/2.16 kg to avoid local viscosity dilution and surface streaking. Post-molding flame treatment raises surface energy to >40 mN/m according to ASTM D2578, allowing pressure-sensitive labels and shrink-sleeve adhesives to wet the surface without delamination. Compliance for personal care packaging is evaluated under EC 1223/2009 for cosmetic product contact, with batch documentation typically requiring REACH registrations for masterbatch pigments and carrier resins. The terminal article is a 400 mL tall oval pack weighing 18–22 g with a wall-thickness distribution of ±0.15 mm, measured by magnetic wall-thickness gauges at 10 fixed points after sectioning.
In six-layer barrier bottle lines producing 400–1000 mL food and industrial barrier containers, HDPE 4613 is assigned to the outer and inner skins as well as to the regrind-bearing core layer. The coextrusion head runs six extruders into a single die; the HDPE layers are fed by 50 mm screw extruders at 190–205°C, while the EVOH barrier layer is held at 210–225°C and the adhesive tie layers at 190–210°C. Layer distribution is controlled by gear-pump flow rates rather than by screw speed alone because viscosity mismatch between EVOH and HDPE can cause interfacial flow instability when the HDPE layer falls below 15% of total thickness. The table below lists one qualified layer structure with thickness shares and control set points.
| Layer sequence | Material function | Thickness share | Control set point |
|---|---|---|---|
| 1 | HDPE 4613 outer skin | 18–22% | 195–205°C melt |
| 2 | Anhydride-modified tie | 2–3% | 190–210°C melt |
| 3 | EVOH barrier | 4–6% | 210–225°C melt |
| 4 | Anhydride-modified tie | 2–3% | 190–210°C melt |
| 5 | Regrind/HDPE core | 40–46% | 190–205°C melt |
| 6 | HDPE 4613 inner skin | 18–22% | 195–205°C melt |
Post-consumer recyclate is not introduced into the skin layers unless the recyclate has been batch-tested for ESCR under ASTM D1693 Condition A and for melt flow stability under ISO 1133-1:2022; in-plant trim regrind of known HDPE 4613 is commonly reused in the core at 40–46% of bottle thickness. The terminal barrier bottle is used for oxygen-sensitive sauces and for industrial liquid concentrates where the oxygen transmission rate must remain below 0.5 cm³/(m²·day·0.21 atm) as measured by ASTM D3985; the HDPE skins provide water-vapour resistance and drop strength while the EVOH layer supplies oxygen barrier. Food-contact status must be confirmed through EU 10/2011 overall migration testing and, for U.S. markets, FDA 21 CFR 177.1520 olefin polymer clearance of the specific 4613 batch, because not all Sinopec HDPE grades are produced with identical additive packages.
Agricultural chemical containers between 3 L and 10 L for emulsifiable concentrates and solvent-borne pesticides are extrusion blow-molded on accumulator-head machines with 80 mm screws at L/D 25:1 and shot capacities of 2.5–4.0 kg. The die-head temperature is kept at 200–205°C, and the accumulator drop speed is profiled so that the parison reaches 80% of final length before the mold halves meet; this prevents pinch-off thinning at the bottom corners of a 5 L jerrycan. Wall thickness is specified at 1.2–1.6 mm in the body and 2.0–2.4 mm at the handle and pinch-off zones. The mold chiller is held at 12–16°C, and blow air at 0.6–0.8 MPa is introduced through the blow pin in two stages: 0.2 MPa for 0.5 s to pre-shape the parison, then full pressure for 12–15 s. Clean plant regrind is limited to 20 wt% because UN certification tests include a drop test at −18°C from 1.2 m on the handle seam, and higher regrind content has been reported to reduce impact toughness at the pinch-off weld. The finished container is tested under the UN Manual of Tests and Criteria, Part III, for tightness, internal hydraulic pressure, and stacking; drop and stacking results must be reproduced on the exact 4613 formulation and mold, not extrapolated from a similar grade. Chemical resistance is screened using method ASTM D543 for swell and weight loss after 7-day immersion in the actual formulated product, not a model solvent. The terminal article is a UN 3H1 jerrycan with a three-layer structure if barrier is required, or a monolayer container for non-flammable formulations where permeation below the regulatory threshold can be demonstrated.
Under-hood reservoir tooling differs from consumer bottle tooling because the part must survive continuous vibration, internal pressure, and cold-start impact; for washer-fluid reservoirs and coolant overflow bottles molded from HDPE 4613, wall thickness is increased to 1.8–3.0 mm and the blow-up ratio is reduced to 1.5:1–2.0:1 to maintain consistent wall cross-section. The parison is dropped from a 90 mm accumulator head at 195–205°C, the mold is maintained at 10–14°C, and cooling time is extended to 25–35 s to limit dimensional warpage after demolding. The part is leak-tested at an internal air pressure of 40 kPa submerged in water, and burst pressure is checked at 200–250 kPa for washer reservoirs; these values are derived from general HDPE blow-molded technical part practice because published data for 4613 in automotive service is limited. UV resistance is obtained with 2.0–2.5 wt% high-pigment carbon black masterbatch dispersed in an HDPE carrier; dispersion is verified by a 25 µm microtome film and transmitted-light inspection under ISO 18553. Long-term heat ageing is screened by ISO 188 at 100°C for 168 h, and dimensional change is measured against the customer’s warm-seam alignment fixture; any shrine line or injection gate must be removed without introducing stress-whitening. OEM validation for under-hood components typically includes thermal cycling from −40°C to 100°C for 200 cycles and a 1 m cold drop at −30°C. Batch documentation includes REACH SVHC compliance and, where requested, ISO 11469 material marking on the part.
For solid oral dosage bottles in the 60–250 mL range, HDPE 4613 is processed in an ISO Class 8 cleanroom on a 45 mm single-station extrusion blow molder with a polished stainless-steel trim-and-deflash system. Melt temperature is held at 190–200°C, and the mold cooling water is kept at 8–10°C to produce a smooth interior surface that reduces powder adhesion. High-density polyethylene for such packs must resist permeability to water vapour; a 0.6 mm wall bottle is tested according to USP ⟨671⟩ for water vapour transmission and must meet the monograph limits for the specific drug product, with test results tied to the 4613 batch number. Incoming resin release includes melt flow rate under ISO 1133-1:2022 at 190°C/2.16 kg and density under ISO 1183-1:2019; the resulting data are retained in the batch record. Opacity is controlled with 1.0–1.5 wt% titanium dioxide masterbatch for light-sensitive formulations, and the masterbatch is qualified under USP ⟨661.1⟩ and EP 3.1.3 for polyolefin packaging components. Regrind is limited to 15 wt% and only from the same cleanroom operation; no recycled material from outside the room is introduced because particulate contamination and unknown additive history violate pharmaceutical change-control. The terminal closure-compatible bottle neck is dimensioned to the customer drawing and sampled at 2 h intervals with go/no-go plug gages, while cap torque is measured as removal torque on a torque meter referenced in ASTM D2063. Pharmaceutical qualification of HDPE 4613 is batch-specific and requires drug master file support or change-control equivalence from the resin manufacturer; published data for this specific configuration is limited.
Competitive Sinopec Maoming HDPE 4613 prices that fit your budget—flexible terms and customized quotes for every order.
For samples, pricing, or more information, please contact us at +8618136850665 or mail to admin@ascent-chem.com.
We will respond to you as soon as possible.
Tel: +8618136850665
Email: admin@ascent-chem.com
Flexible payment, competitive price, premium service - Inquire now!