| HS Code | 921394 |
| Density | 0.959 g/cm3 |
| Melt Flow Rate 190 C 2 16 Kg | 0.35 g/10 min |
| Tensile Yield Strength | >=28 MPa |
| Tensile Strength At Break | >=30 MPa |
| Elongation At Break | >=600% |
| Flexural Modulus | >=1200 MPa |
| Vicat Softening Temperature | >=125 °C |
| Brittleness Temperature | <=-70 °C |
| Environmental Stress Cracking Resistance | >=1000 h |
| Hardness Shore D | >=65 |
| Melting Point | 130-136 °C |
| Water Absorption | <0.01% |
| Dielectric Constant | 2.3 |
| Volume Resistivity | >10^16 Ω·cm |
| Dielectric Loss Tangent | <0.0005 |
| Thermal Conductivity | 0.4 W/m·K |
| Specific Heat Capacity | 1.9 kJ/kg·K |
| Coefficient Of Linear Thermal Expansion | 1.2×10^-4 /°C |
| Molding Shrinkage | 1.5-3.0% |
| Charpy Notched Impact Strength 23 C | 20 kJ/m2 |
| Charpy Notched Impact Strength 30 C | 8 kJ/m2 |
As an accredited Ningxia Baofeng Energy HDPE BM593 factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | Ningxia Baofeng Energy HDPE BM593 is typically packed in 25 kg bags or 1,000 kg jumbo bags. |
| Container Loading (20′ FCL) | 20′ FCL loading: Ningxia Baofeng Energy HDPE BM593, supplied in 25 kg bags, palletized or loose, about 25 MT net per container. |
| Shipping | Ningxia Baofeng Energy HDPE BM593 ships as a non-hazardous, free-flowing polyethylene resin. Standard packaging: 25 kg PP woven bags, 500–1500 kg jumbo bags, palletized. Transport in 20'/40' containers via sea, rail, or truck. Keep dry, cool, away from sunlight, moisture, and contamination. Handle with standard cargo precautions. Store under cover. |
| Storage | Store Ningxia Baofeng Energy HDPE BM593 in a cool, dry, well-ventilated warehouse, preferably in original sealed bags on pallets. Keep away from direct sunlight, heat, flames, moisture, and strong oxidizers. Avoid contamination and dust; use first-in-first-out rotation. Maintain safe stacking heights, protect from mechanical damage, and follow the manufacturer’s SDS and local regulations. |
| Shelf Life | Ningxia Baofeng Energy HDPE BM593 shelf life: typically 24 months in unopened original packaging, stored cool, dry, away from sunlight. |
A frequent production-scale observation in tight-head 20-L polyethylene jerrican lines is that a loss of parison melt strength during the extrusion phase produces thickened pinch-off seams and an undersized handle wall section, which in turn raises the rejection rate at the UN leakproofness test. The BM593 lot in this application is therefore evaluated for melt mass-flow rate under ISO 1133-1:2022 at 190°C/21.6 kg and for density under ISO 1183-1:2019 before dry-blending. The shipping classification is governed by the UN Model Regulations Chapter 6.1; design-qualification tests for plastic jerricans and tight-head drums include drop testing under 6.1.5.2, leakproofness under 6.1.5.3, internal pressure under 6.1.5.4, and stacking under 6.1.5.5, with additional modal references in ADR 6.1.5, IMDG Code Part 6, and ICAO TI Part 6. On the formulations side, BM593 is introduced at 70.0–100.0 wt% with clean in-plant regrind of the same certified formula allowed up to 30.0 wt%; a polyethylene-compatible colour masterbatch is metered at 1.0–3.0 wt%, and a zinc stearate or calcium stearate process aid is limited to 0.05–0.15 wt% to reduce plate-out on the head tooling without creating surface migration that could compromise torque-retention on the closure neck. The processing line is typically an accumulator-head extrusion blow moulding machine with screw L/D 25–30, a grooved-feed or barrier screw design, melt temperature 180–220°C, mould temperature 12–28°C, blow pressure 0.6–0.9 MPa, and cycle times of 60–120 s for 60-L shot sizes. Terminal product types are 1H1 tight-head drums and 3H1 jerricans in 20-L, 25-L, 30-L, and 60-L nominal capacities, used for lubricants, solvents, industrial detergents, and corrosive liquid transport under Packing Group II and III assignments.
| Design-qualification test | UN Model Regulations clause | Variable monitored on production line | Typical packaging code |
|---|---|---|---|
| Drop | 6.1.5.2 | Closure restraint, weld seam integrity, handle section cracking | 3H1 |
| Leakproofness | 6.1.5.3 | Neck/closure interface, pinch-off seal, wall pinhole count | 3H1/1H1 |
| Internal pressure | 6.1.5.4 | Creep deformation, burst threshold, weld line thinning | 1H1 |
| Stacking | 6.1.5.5 | Top-load deflection, sidewall buckling, environmental conditioning | 3H1/1H1 |
Crop protection container production on shuttle blow moulding equipment introduces a different failure mode than UN-certified industrial packaging: stress cracking at the handle pinch-off, aggravated by contact with solvent-based emulsifiable concentrate formulations. The compliance framework includes UN Model Regulations 6.1.5 for dangerous goods packaging when the pesticide formulation is classified for transport, US EPA 40 CFR 156.10 for container design and residue removal expectations, and Regulation (EC) No 1272/2008 for supplement labelling and child-resistant closure requirements where applicable. In coextrusion blow moulding, BM593 typically functions as the outer structural and inner contact layer at 60.0–95.0 wt% of the total container mass; an EVOH barrier layer is set at 2.0–5.0 wt%, maleic-anhydride tie layers at 1.0–3.0 wt%, and ground bottle scrap from the same line up to 25.0 wt% of the structural layer after three-pass drying in a closed-loop granulator system. The downstream process is a six-layer coextrusion shuttle blow moulding machine, with main extruder L/D 30:1, melt temperature 190–220°C, EVOH extruder temperature 210–220°C, mould cooling 8–18°C, and cycle times of 10–16 s for 1-L bottles. Finished container geometries include 0.5-L, 1-L, and 5-L high-density polyethylene crop protection bottles, measuring containers with peel-back labels, and closed-transfer system couplers for liquid pesticide handling.
In oral solid dose packaging, the pharmacopoeial extractables profile is dominated by low-molecular-weight polyethylene oligomers and additive migration rather than by the main polymer architecture. BM593 is therefore used at 99.0–100.0 wt% in pharmaceutical bottle formulations only when the supplied lot carries a pharmacopoeial certificate of analysis; titanium dioxide white masterbatch is restricted to 0.5–1.0 wt%, and slip agents, antistatic additives, and ester-based processing aids are excluded unless explicitly declared and validated under the finished drug product stability protocol. The applicable standards are USP <661.1> for plastic packaging systems, Ph. Eur. 3.1.3 for polyolefins, and FDA 21 CFR 177.1520 when the package is marketed for food-adjacent or dual-use oral solid dose applications; extractables screening is commonly performed under ICH Q3D risk-assessment procedures. On the production floor, continuous extrusion blow moulding machines with polished screws and barrels are operated at melt temperatures of 180–210°C, mould temperatures of 10–20°C, and in-line wall-thickness inspection using near-infrared or x-ray gauge systems; leak testing is run at 100% of filled bottles by pressure decay. Terminal packaging categories comprise 30-mL to 500-mL tablet and capsule bottles, desiccant canisters, dry powder oral dosage containers, and bulk dispensing containers for clinical trial materials.
Household bleach lines run with water-based and hypochlorite-containing fills at pH 12.0–13.0, and the bottle wall is simultaneously exposed to oxidative degradation, surfactant-induced environmental stress cracking, and intermittent top-load stacking. In this application, BM593 is blended at 96.0–99.0 wt% with a white or coloured polyethylene masterbatch at 1.0–3.0 wt% and a hindered phenolic antioxidant / phosphite stabilizer package at 0.05–0.15 wt%; post-consumer recyclate is excluded unless the filling operation has completed sensory and stress-crack validation on the specific recycle lot. The mechanical acceptance path includes tensile yield strength under ASTM D638-14 Type IV specimens, Izod impact under ASTM D256-10, and environmental stress crack resistance under ASTM D1693-15 Condition B; published ESCR data for this specific grade under Condition B is limited to the manufacturer's certificate of analysis, so incoming lot release testing should measure the same parameter before production approval. Processing equipment is typically a reciprocating-screw shuttle blow moulding machine with clamp force 80–180 kN, melt temperature 180–210°C, mould temperature 10–25°C, blow pressure 0.5–0.8 MPa, and cycle time 8–15 s for 500-mL to 5-L bottle geometries. The resulting container set spans household bleach bottles, fabric softener containers, all-purpose cleaner bottles, and institutional surface sanitizer dispensing bottles.
Food-ingredient overpacks differ from household chemical containers in that the lot-specific certificate of conformance must demonstrate overall migration below 10 mg/dm² under EU 10/2011, and the polymer must be manufactured under a hygiene audit acceptable to the buyer's food safety system. For BM593 in this segment, the addition ratio is 100.0 wt% virgin resin; only internal regrind generated from the same food-contact production run is allowed, and it is capped at 20.0 wt% with a documented control of residence time and moisture. Food-contact masterbatch, if used for colour or opacity, is metered at 0.5–1.0 wt% and must comply with FDA 21 CFR 177.1520(c) and EU 10/2011 positive list requirements; post-consumer recyclate is prohibited in this segment. The downstream process is extrusion blow moulding on polished screw and barrel assemblies, with melt temperature 180–210°C, mould temperature 10–20°C, and an organoleptic control programme based on volatile content reduction; mould release agents and external lubricants are not used unless they are approved food-contact additives. Applicable standards include FDA 21 CFR 177.1520, EU 10/2011, China GB 4806.6-2016, and ISO 1183-1:2019 for density verification. End-use pack configurations are 5-L, 10-L, and 20-L food-ingredient containers, edible oil bottles, viscous sauce and dressing bottles, and bulk dispensers for dry food powders.
At -20°C to 40°C, windshield washer fluid and coolant containers are subjected to palletized top-load, occasional drop impact, and sustained contact with methanol- or ethylene-glycol-containing fills. The grade is blended at 95.0–100.0 wt% BM593 with a UV-stabilized masterbatch at 0.5–2.0 wt% and colour or carbon black masterbatch at 0.5–3.0 wt%; for diesel exhaust fluid containers, the material pack must additionally pass compatibility testing under ISO 22241-1:2019 and ISO 22241-3:2019 when the finished container is placed into the AUS 32 supply chain. Cold impact is assessed by drop testing conditioned bottles at -20°C using the drop heights specified by transportation or automotive OEM standards; top-load strength is measured on a universal testing machine with crosshead speed 10 mm/min to simulate 3-high pallet stacking. The process line is a high-output accumulator-head blow moulding machine with screw L/D 25–30, melt temperature 180–215°C, mould temperature 10–25°C, blow pressure 0.6–0.9 MPa, and cycle times of 12–30 s for 1-L to 20-L geometries. The manufactured article range includes windshield washer fluid bottles, coolant and antifreeze jugs, diesel exhaust fluid containers, and concentrated antifreeze dispensing packs.
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Ningxia Baofeng Energy HDPE BM593 is a high-density polyethylene resin supplied as natural-colour pellets for extrusion blow molding of rigid containers, jerry cans, and industrial packaging. The grade designation BM593 identifies a high-molecular-weight HDPE in which the melt mass-flow rate and density are controlled for parison stability rather than high-flow injection moulding. Typical lot data from supplier technical documentation place the density between 0.955 g/cm³ and 0.959 g/cm³ when conditioned at 23 °C and tested according to ISO 1183-1, and the melt mass-flow rate between 0.25 g/10 min and 0.40 g/10 min at 190 °C under 2.16 kg load according to ISO 1133-1:2022. These values place HDPE BM593 in the low-flow, high-melt-strength segment of HDPE blow molding resins, separate from HDPE film grades and injection molding grades.
On production-scale shuttle blow molders with grooved-barrel extruders of 65 mm to 90 mm screw diameter and 24:1 L/D ratio, the grade is conventionally processed at melt temperatures from 190 °C to 210 °C. Industrial observations indicate that melt temperatures above 220 °C reduce parison load-bearing strength and increase wall-thickness variation in containers larger than 5 L. Die head temperatures are normally held within 10 °C of the extruder melt temperature to avoid cold die lip freeze-off or excessive surface oxidation. The low MFR contributes to reduced parison sag during gravity extrusion, but the final wall distribution depends on die gap programming, mold cooling rate, and screw speed.
Regulatory status for HDPE BM593 is assessed under REACH and RoHS 2011/65/EU for heavy metal restrictions. The base resin is not classified as a dangerous substance under CLP; however, specific additive packages and color concentrates must be confirmed by the converter. For food-contact containers, compliance with FDA 21 CFR 177.1520 and EU Regulation 10/2011 is possible only when the finished article is tested for overall migration and specific migration limits for the intended food type.
Accumulator-head blow molders impose a different thermal and shear history on the melt than continuous shuttle machines. In accumulator discharge, the melt is compressed in the head before being pushed through the die gap at high strain rate. For HDPE blow molding resins in the same low-MFR class as BM593, die swell is commonly observed between 20% and 40% at die gap shear rates near 100 s⁻¹. The die gap is therefore adjusted from 1.5 mm to 3.0 mm depending on container size and parison length. If the melt temperature is too low, sharkskin or rough parison surfaces appear at the die exit; if too high, parison sag increases nonlinearly and can produce unacceptable wall thinning in the container shoulder area.
Pre-drying is not routinely required for HDPE BM593 when pellets remain in sealed packaging. Exposure to relative humidity above 60% can introduce surface moisture sufficient to create splay or pinhole defects in blow-molded parts. Under such conditions, hopper drying at 80 °C to 90 °C for 1 hour to 2 hours is used before extrusion. The grade should not be blended with polypropylene or LLDPE regrind above 10 wt% without verifying parison layer uniformity and weld-line integrity.
Environmental stress crack resistance is the principal property governing the use of BM593 in containers that hold surfactants, detergents, light hydrocarbons, and aqueous agricultural chemicals. Under ASTM D1693 Condition B, F50 notation, high-molecular-weight HDPE blow molding grades in this class typically exceed 600 h in 100% Igepal CO-630 at 50 °C. Grade-specific ESCR values for BM593 should be requested from the supplier, because ESCR is influenced by comonomer content, cooling rate, molded-in stress, and wall thickness. Containers produced from BM593 are used for industrial packaging, jerry cans, and small intermediate bulk containers; the grade is not recommended for prolonged contact with strong oxidizing acids or aromatic solvents without validation on the finished article.
The molecular architecture that provides ESCR also reduces melt flow. As a result, BM593 is unsuitable for thin-wall injection molding applications requiring HDPE grades with MFR values of 4 g/10 min to 20 g/10 min. In extrusion blow molding, the flow limitation is offset by the high shear rate at the die lip. Single-screw extruders with compression ratios between 2.5:1 and 3.5:1 are typically used for this grade, with grooved feed sections preferred for stable output control.
For BM593, die swell and parison sag jointly determine the wall thickness distribution of the finished container. A weight swell of 150% to 250% relative to the die gap is common in this melt index range. The processor compensates by programming the die gap from approximately 0.8 mm at the top of the parison to 2.5 mm at the bottom for tapered containers. Mold temperature is controlled at 10 °C to 30 °C for rapid dimensional stabilization, with chilled water at 8 °C to 15 °C circulated through mold channels. On a single-station shuttle machine, the cycle time for a 10 L jerry can is typically 50 s to 70 s, depending on wall thickness, mold material, and machine clamp force.
Production-scale equipment behaviour indicates that grooved-barrel extruders provide stable melt output for BM593 at screw speeds between 40 rpm and 70 rpm for an 80 mm screw diameter. A typical barrel zone profile is set at 170 °C feed, 190 °C compression, 200 °C metering, and 200 °C head. These settings are not universal; screen pack pressure and screw design require adjustment. Increasing screw speed above 80 rpm can generate melt temperatures above 220 °C, producing surface defects and reduced parison strength.
The following table summarizes representative property data for HDPE BM593 as presented in supplier technical documentation and class-typical values where grade-specific values are not published. Lot-specific certificates may vary.
| Property | Test Method | Unit | Value/Range |
|---|---|---|---|
| Density | ISO 1183-1 | g/cm³ | 0.955–0.959 |
| Melt mass-flow rate, 190 °C/2.16 kg | ISO 1133-1:2022 | g/10 min | 0.25–0.40 |
| Tensile yield stress | ISO 527-2 | MPa | 24–28 |
| Elongation at break | ISO 527-2 | % | >500 |
| Flexural modulus | ISO 178 | MPa | 900–1100 |
| ESCR, F50, 100% Igepal, 50 °C | ASTM D1693-B | h | >600 |
| Vicat softening temperature, 10 N | ISO 306/A50 | °C | 124–128 |
| Notched Izod impact, 23 °C | ISO 180/A | kJ/m² | 6–10 |
The primary difference between HDPE BM593 and general-purpose injection molding HDPE is melt mass-flow rate. Injection molding grades intended for thin-wall applications typically exhibit MFR values of 4 g/10 min to 20 g/10 min, permitting long flow paths at moderate pressure. BM593 at 0.25 g/10 min to 0.40 g/10 min would require elevated melt temperature and injection pressure, increasing cycle time and warpage risk in thin-wall moulds. Compared with HDPE film grades, which often have densities of 0.948 g/cm³ to 0.952 g/cm³ and MFR values of 0.7 g/10 min to 1.2 g/10 min, BM593 has higher density and melt strength, producing greater stiffness and improved parison hang time but lower bubble stability in film blowing.
The molecular weight distribution and comonomer placement of BM593 are not identical to pipe-grade HDPE. BM593 is not specified for long-term hydrostatic pressure piping; it is specified for blow-molded industrial containers, automotive fluid reservoirs, and jerry cans. The comparison table below presents class-level differences for material selection purposes.
| Resin Class | Typical MFR, 190 °C/2.16 kg | Typical Density | Primary Processing |
|---|---|---|---|
| HDPE BM593 blow molding | 0.25–0.40 g/10 min | 0.955–0.959 g/cm³ | Extrusion blow molding |
| HDPE injection molding | 4–20 g/10 min | 0.950–0.965 g/cm³ | Injection molding |
| HDPE film | 0.7–1.2 g/10 min | 0.948–0.952 g/cm³ | Film extrusion |
Processing of BM593 on twin-station shuttle machines introduces a different thermal control problem because accumulated melt can dwell in the head for longer periods. When the head is idle, degradation of the outer melt layer can occur if temperatures exceed 200 °C for more than 5 minutes. Start-up and shutdown procedures should include purging with a lower-MFR HDPE or a dedicated purging compound to displace stagnant resin from the die lip and mandrel. During colour change, the die head is disassembled and cleaned because carbonized material at the die gap alters parison surface roughness and promotes gel formation.
Batch-to-batch variation in BM593 is managed on blow molding lines by monitoring die swell and parison sag as indirect indicators of molecular weight distribution. If parison sag increases while melt temperature and die gap remain constant, the incoming lot may have lower viscosity. The melt temperature can then be reduced by 5 °C to 10 °C or the die gap narrowed to restore dimensional control. These adjustments are standard on lines equipped with parison programming control. Published data for this specific grade across all machine types is limited, so process conditions should be established on the target mould and production line.