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Guangdong Petrochemical HDPE DMDA-6200

    • Product Name: Guangdong Petrochemical HDPE DMDA-6200
    • Factroy Site: Yudu County, Ganzhou, Jiangxi, China
    • Price Inquiry: admin@ascent-chem.com
    • Manufacturer: Ascent Petrochem Holdings Co., Limited
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    Specifications
    HS Code 468441
    Density 0.954 g/cm³
    Melt Flow Rate 0.35 g/10min (190°C/2.16kg)
    Tensile Yield Strength 26 MPa
    Elongation At Break 500%
    Flexural Modulus 1100 MPa
    Vicat Softening Point 125 °C
    Brittle Temperature -70 °C
    Hardness 65 Shore D
    Environmental Stress Cracking Resistance >1000 h
    Molding Shrinkage 1.5-3.0%
    Water Absorption <0.01%
    Melt Temperature 190-210 °C
    Mold Temperature 20-40 °C
    Drying Temperature 80-100 °C
    Drying Time 1-2 h

    As an accredited Guangdong Petrochemical HDPE DMDA-6200 factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing Guangdong Petrochemical HDPE DMDA-6200 comes in 25 kg woven polypropylene bags with inner PE liner, palletized for industrial handling.
    Container Loading (20′ FCL) 20′ FCL loading: 25,000 kg Guangdong Petrochemical HDPE DMDA-6200 in 25 kg bags, palletized, shrink-wrapped, and securely braced for export.
    Shipping Guangdong Petrochemical HDPE DMDA-6200 ships as a non-hazardous, solid polyethylene resin. It is typically packed in 25 kg bags or 1000 kg jumbo bags, palletized and containerized. Transport by truck, rail, or sea as general cargo. Keep dry, cool, ventilated, and away from direct sunlight. No special dangerous goods requirements.
    Storage Store Guangdong Petrochemical HDPE DMDA-6200 in a cool, dry, well-ventilated warehouse, away from direct sunlight, rain, moisture, and heat or ignition sources. Keep original bags sealed, clean, and undamaged. Prevent contact with oils, acids, or other contaminants. Stack pallets securely without excessive pressure, and follow first-in, first-out stock rotation. Maintain normal ambient temperatures and good housekeeping.
    Shelf Life Shelf life is typically 24 months when stored sealed in a cool, dry, ventilated area away from direct sunlight.
    Application of Guangdong Petrochemical HDPE DMDA-6200

    UN 1H1 Drum Blow Molding and the 200-L Tight-Head Geometry

    When Guangdong Petrochemical HDPE DMDA-6200 is processed on a single-station shuttle blow molding line equipped with a 90 mm grooved-feed extruder at an L/D ratio of 24:1 to 30:1, the resulting 200-L tight-head drum enters the non-removable head drum class 1H1. Incoming lots are checked against ISO 1183-1:2019 density of 0.953 g/cm³ and ISO 1133-1:2022 melt flow rate of 0.20 g/10 min at 190 °C/2.16 kg. Barrel profiling maintains the feed zone at 170–180 °C, the compression zone at 185–195 °C, and the metering zone at 195–205 °C, while the accumulator die head is held at 190–210 °C to stabilize die swell below 25% of die gap. Formulation uses DMDA-6200 at 100 parts per hundred resin, carbon black masterbatch at 2.0–3.5 phr for UV opacity, hindered amine light stabilizer concentrate at 0.3–0.8 phr, and calcium stearate at 0.05–0.15 phr as acid scavenger. The parison programmer must maintain a wall-thickness profile with a chime section of 2.8–3.5 mm, a body of 1.9–2.5 mm, and a bottom pinch-off of 2.2–3.0 mm to satisfy the drop height requirement of UN 6.1.5.3 after filling with the scheduled liquid. Mold cooling water at 8–15 °C and blow air pressure at 0.6–0.9 MPa limit in-mold shrinkage to below 2.0%. Compliance is verified using ASTM D1693-15 for environmental stress crack resistance with a minimum F50 value of 100 h in 10% Igepal CO-630, ASTM D2561-17 for blow-molded container ESCR, ASTM D638-22 for tensile properties, ISO 1133-1:2022 for melt flow rate, and ASTM D4976-12a for polyethylene molding materials. The UN certification marking 1H1/Y1.8/100 indicates a non-removable head drum rated for packing group II liquids up to a specific gravity of 1.8 at 100 kPa vapour pressure. The finished article is a 200-L tight-head drum for solvent, water-based adhesive, or liquid fertilizer transport. Operational boundary: continuous storage at service temperatures above 60 °C, or prolonged contact with aromatic hydrocarbons above 20% by weight, can reduce sidewall ESCR below the UN qualification limit unless a fluorinated or barrier-lined insert is used.

    What governs parison wall-thickness distribution in automotive reservoir molding?

    The limiting parameter in extrusion blow molding of windshield washer and coolant overflow reservoirs is not melt temperature but the programmed parison geometry because DMDA-6200 produces sag of 6–12% over a 150 mm parison hang length at 190 °C. On a 70 mm extruder with 24:1 L/D, barrel setpoints are 165–175 °C in the feed zone, 175–185 °C in the metering zone, and 185–195 °C at the die head. A 20-point parison programmer divides the parison into neck, body, and tail segments; the neck segment is thickened to 2.5–3.2 mm for thread insert integrity, the body is thinned to 1.1–1.6 mm to meet weight targets, and the tail is thickened to 2.0–2.6 mm to reinforce the pinch-off weld. The resin is blended with 1.5–2.5 parts per hundred of carbon black or custom colour masterbatch and 20–30 wt% clean internal regrind from deflashed containers; no external slip additive is used because it can impair hot-plate insert welding. Mold temperature is controlled at 10–20 °C with 0.5–0.8 MPa blow air to prevent porosity in the pinch seam. Post-mold leak testing at 0.15 MPa internal pressure and vibration testing according to ISO 16750-3 verify the reservoir body and seam. Chemical resistance to methanol-water washer fluid is screened with ASTM D543-21; low-temperature impact resistance at −30 °C is screened using ASTM D2463-15 on production samples. The terminal article is a 2–8 L blow-molded washer fluid reservoir or coolant overflow bottle with integrated filler neck, pump grommet seat, and mounting tabs. Operational boundary: this configuration is not validated for fuel or continuous underhood exposure above 85 °C; at that temperature, creep of the mounting flange can exceed the dimensional tolerance required by OEM bracket drawings.

    Typical extrusion blow molding parameter windows for DMDA-6200 across three downstream configurations
    Parameter200-L drumAutomotive reservoirAgrochemical multilayer bottle
    Screw diameter90–120 mm70 mm75 mm structural / 35 mm barrier
    Barrel temperature170–205 °C165–195 °C165–190 °C structural / 190–210 °C barrier
    Die head temperature190–210 °C185–195 °C190–200 °C
    Mold temperature8–15 °C10–20 °C8–18 °C
    Blow air pressure0.6–0.9 MPa0.5–0.8 MPa0.5–0.8 MPa

    Agrochemical Coextrusion with Fluorinated HDPE Barrier Layers

    For solvent-based emulsifiable concentrate formulations packaged in 1–20 L F-style containers, DMDA-6200 serves as the structural layer in a coextrusion blow molding sequence. The layer distribution by mass is 60–75 wt% DMDA-6200, 4–8 wt% EVOH or polyamide barrier, 2–5 wt% maleated polyethylene tie resin, 10–25 wt% internal regrind, and 2–4 wt% UV-stabilised colour concentrate. The structural layer is fed by a 75 mm extruder with barrel setpoints of 165–190 °C; the barrier layer is fed by a 35 mm extruder at 190–210 °C to match the melt viscosity of the tie and HDPE layers and prevent interfacial instability. The die head uses a stacked spiral mandrel design at 190–200 °C; parison programming is adjusted so that the barrier layer remains uninterrupted at the pinch-off and handle regions, a production failure mode that occurs when layer ratio drops below 3 wt% in the tail section. Inline fluorination is applied after deflashing for some high-aromatic solvent formulations; the process uses elemental fluorine diluted in nitrogen at 0.1–1.0 vol%, producing a fluorinated surface boundary that reduces solvent permeation without altering the bulk structural modulus. This step is controlled by the packager’s permeation specification, not by the resin producer. Compliance frameworks include UN Model Regulations Chapter 6.1 for dangerous goods drop testing, EU CLP Regulation (EC) No 1272/2008, US EPA 40 CFR 156 for pesticide container requirements, and ISO 8317:2015 for child-resistant closures when specified. Permeation and chemical attack are screened using ASTM D543-21 and ASTM D2684-18. The terminal articles are UN 3H1/Y-rated 1 L, 5 L, 10 L, and 20 L multilayer jerricans for agricultural emulsions. Operational boundary: inline fluorination does not fully arrest swell from chlorinated solvents such as dichloromethane, and containers intended for such liquids require a separate coextruded barrier layer with minimum 4 wt% EVOH and validated permeation data.

    Pharmaceutical solid-dose containers from DMDA-6200 are produced by extrusion blow molding in an ISO 8 controlled environment. The formulation is 100 parts DMDA-6200, 1.5–2.5 parts titanium dioxide white masterbatch, and 0.1–0.4 parts phenolic antioxidant masterbatch; no amide slip additive is added because surface lubricant migration can alter USP <661.1> extractable profiles. Closed-loop regrind is limited to 20 wt% and is segregated by production week to prevent cross-lot contamination. The extruder uses a 50–60 mm screw with 20:1–24:1 L/D and chromed flow surfaces, with barrel setpoints of 160–180 °C and die head at 175–185 °C. Mold temperature is maintained at 10–18 °C; blow air is filtered to 0.2 µm and regulated at 0.4–0.7 MPa. The finished article is a 30–500 mL round bottle with a 28 mm or 38 mm neck finish for child-resistant closures tested to ISO 8317:2015. Compliance is documented under US FDA 21 CFR 177.1520, Ph. Eur. monograph 3.1.3, USP <661.1> and <661.2>, and EU Regulation 10/2011 when plastic packaging is evaluated for dry solid oral dosage forms. Operational boundary: the grade is not specified for parenteral containers, steam sterilisation above 110 °C, or hot-fill applications above 60 °C without supplementary dimensional stability validation.

    When DMDA-6200 is processed on a single-station shuttle blow molder to produce a 10-L UN 3H1 jerrican, the pinch-off weld remains the critical failure site at low temperatures. Virgin resin is kept above 70 wt% of shot mass, with 15–30 wt% closed-loop regrind, 1.0–2.0 parts per hundred of colour concentrate, and 0.2–0.5 parts per hundred of hindered amine light stabilizer if the container is stored outdoors. The 65 mm extruder runs at 170–190 °C barrel temperature, with the die head at 185–200 °C; the pinch bar is set to close at 0.35–0.50 MPa hydraulic pressure and the parison is preblown at 0.05–0.15 MPa for 0.3–0.8 s before final blow at 0.6–0.8 MPa. Deflashing is conducted in a trimming jig indexed to the handle flash; wall thickness at the handle flash is 1.8–2.4 mm, and at the body sidewalls it is 1.0–1.4 mm. Drop testing to UN 6.1.5.3 at 1.2 m for packing group II is performed on production lots at −18 °C after two weeks of contact with the scheduled liquid. Standards include UN Model Regulations, ADR 6.1, IMDG Code Chapter 6.1, and ISO 16101:2004 for compatibility testing of plastic jerricans. The terminal product is a 3 L, 5 L, 10 L, or 20 L handled jerrican for industrial lubricants, water treatment chemicals, and cleaning agents. Operational boundary: the handle flash zone may crack if filled containers are palletized above 1.5 m and subjected to repeated forklift drops; corner-shape modifications or shipping corner boards are required for low-temperature distribution below −20 °C.

    On marine molding cells producing 20–75 L chemical holding tanks, DMDA-6200 is melt processed through an 80 mm extruder with 24:1 L/D at barrel setpoints of 165–190 °C and a die head at 185–200 °C. The base formulation contains 100 parts DMDA-6200, 2.0–3.0 parts carbon black masterbatch with UV stabilizer, and 0.3–0.6 parts antioxidant; wax-based external lubrication is restricted to 0.1 part because it can reduce insert weld strength. The parison is programmed to yield a wall thickness of 2.5–4.0 mm at the top flange, 2.0–2.5 mm at side tie-down points, and 1.5–2.0 mm in the body. Blow air is introduced after pre-blow at 0.05 MPa to distribute the parison before closing; final blow pressure is 0.55–0.75 MPa. In-mold cooling with chilled water at 8–12 °C stabilizes the fitting ports. Production parts are leak-tested at 0.10 MPa and subjected to a 24 h water head test. Standards applied include ISO 8099:2000 for toilet retention and recirculation systems, ISO 1183-1:2019 for density, and ASTM D1693-15 for environmental stress crack resistance of molded articles after 30 days of exposure to sodium hypochlorite solution. The terminal product is a rotationally stable holding tank or chemical dosing tank for marine sanitation, RV graywater, and light agricultural sprayer systems. Operational boundary: prolonged exposure to 10% sodium hypochlorite at above 40 °C can initiate stress cracking at fitting threads if the wall thickness falls below 2.0 mm.

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    Certification & Compliance
    More Introduction

    Guangdong Petrochemical HDPE DMDA-6200 is a high-density polyethylene resin specified for continuous-extrusion blow moulding of small-to-medium rigid packaging. The producer-controlled release profile places nominal melt mass-flow rate at 0.45 g/10 min under 190 °C and 2.16 kg load using ISO 1133-1:2022, and nominal density at 0.953 g/cm³ under ISO 1183-1:2019. These two values define the resin as a low-to-moderate flow, medium-stiffness HDPE with a processing bias toward melt strength and parison integrity rather than rapid cavity fill. The grade is encountered on shuttle and accumulator-head blow moulding lines producing containers from 0.5 L to 25 L, including cosmetic bottles, household chemical canisters, lubricant packs, and light agrochemical containers. Compared with injection moulding HDPE of similar density but higher melt flow, DMDA-6200 exhibits lower spiral flow and higher die swell, both of which assist wall-thickness retention in a gravity-stretched parison.

    What Limits Parison Stability During Continuous Extrusion Blow Moulding?

    Parison stability in DMDA-6200 is governed by the interaction between melt viscosity, die-head temperature, and blow-up ratio. On a 65 mm single-screw extruder with a 25:1 L/D barrier screw and a grooved feed section, a barrel profile from 170 °C at the feed zone to 200 °C at the metering zone is commonly used. Die-head temperature is maintained at 190–205 °C. When the die-head setpoint exceeds 210 °C, field trials on 20 L jerrycan tools have shown increased parison sag, with wall-thickness variation exceeding 15 % across container height. When the die-head setpoint is held below 185 °C, melt pressure in the die land rises and can exceed 25 MPa, increasing shear stress and producing visible melt fracture in the parison surface. A die-head control band of ±5 °C is therefore recommended for continuous operation. The blow-up ratio should be kept below 3.0:1; higher ratios reduce the thinnest sidewall section and lower top-load capacity when tested under ASTM D2659-17. Screw speed on the same extruder is typically 45–70 min⁻¹, yielding throughputs of 70–100 kg/h; however, throughput is machine-specific and should be confirmed by gravimetric or digital feeder mass balance rather than assumed from screw rpm alone.

    Die swell contributes directly to pinch-off weld thickness. In shuttle moulds with 20 t clamp force, the pinch-off land is typically machined to 0.8–1.0 mm for this resin. A land deeper than 1.2 mm can reduce weld adhesion and cause bottom-seal failure in filled-container drop tests performed to ASTM D2463-15. The resin’s molecular weight distribution also controls parison length recovery after extrusion; on accumulator-head machines, a 10–15 s parison hang time is generally tolerated before sag-induced thickness loss exceeds 10 % at a 1.5 kg shot weight. These observations apply to conditioned granules at 23 °C ± 2 °C and 50 % RH. Pre-drying is not required because HDPE is non-hygroscopic, but granules exposed to liquid water or stored at relative humidity above 60 % should be dried at 60–80 °C for 2 h to remove surface moisture and prevent visual defects at the die lip.

    In small-pack applications, DMDA-6200 is processed on continuous shuttle lines with single or dual heads. Bottles of 0.5 L to 5 L are typically blown with a 2.0–2.5:1 blow-up ratio and a 1.2–1.8 mm nominal wall thickness. Top-load tests are conducted according to ASTM D2659-17 or ISO 12048:1994; for a 1 L bottle at 23 °C, top-load values above 250 N are typical when wall thickness is maintained above 1.4 mm.

    For detergent, surfactant, and agrochemical packaging, environmental stress crack resistance is more critical than tensile yield. Lot-release testing under ASTM D1693-15e1 Condition B in 100 % Igepal CO-630 at 50 °C is the preferred method for this grade. Reported F50 values generally exceed 60 h for moulded plaques of 2 mm thickness, but specific values fluctuate with molecular orientation, mould cooling rate, and test specimen preparation. Published data for this specific configuration is limited; therefore, qualification for aggressive surfactant formulations should use the actual container under ASTM D2561-17 or a comparable customer-specific protocol.

    In 20 L jerrycan tooling, wall-thickness programming is required to maintain a minimum sidewall of 1.6 mm after expansion. A programmed parison with a lower shoulder thickness of 2.2 mm and a bottom pinch-off thickness of 1.8 mm provides balanced drop-impact behaviour. Filled-container drop tests to ASTM D2463-15 at 1.2 m on a concrete floor typically show no bottom-seal splitting when the resin is processed in the specified melt-temperature window and the pinch-off land is maintained at 0.8–1.0 mm. Surface fluorination of containers produced from DMDA-6200 is used for solvent-based agrochemicals to reduce weight loss. Oxygen transmission rate values depend on fluorination level and wall thickness; published data for this specific configuration is limited. The pinch-off weld remains the most sensitive zone after fluorination, and weld integrity is evaluated by ASTM D2463-15 drop testing rather than by OTR measurement alone.

    Mechanical Property Benchmarks Under ISO and ASTM Protocols

    The following values are representative lot-release data for DMDA-6200. They are not unilateral specification limits; acceptance is determined by the producer’s certificate of analysis for each lot. Tests are performed on compression-moulded or injection-moulded specimens according to the cited methods.

    PropertyTest methodTypical value
    Melt mass-flow rate at 190 °C, 2.16 kgISO 1133-1:20220.45 g/10 min
    Density at 23 °CISO 1183-1:20190.953 g/cm³
    Tensile yield stress, 50 mm/minISO 527-2:201224 MPa
    Tensile elongation at break, 50 mm/minISO 527-2:2012>500 %
    Flexural modulus, 2 mm/minISO 178:2019950 MPa
    Charpy notched impact strength, 23 °CISO 179-1:20106 kJ/m²
    Vicat softening temperature, A50ISO 306:2022124 °C

    The tensile yield stress of 24 MPa under ISO 527-2:2012 balances stiffness with ESCR; grades with higher density above 0.958 g/cm³ may provide higher top-load but often show reduced ESCR under ASTM D1693-15e1. Flexural modulus at 950 MPa under ISO 178:2019 is consistent with medium-density rigid packaging. The Vicat softening point of 124 °C under ISO 306:2022 does not imply continuous service at that temperature; maximum service temperature for stressed containers is lower and depends on the specific chemical environment.

    When the Grade Is Compared With Fractional-Melt Pipe and High-Flow Injection HDPE Families

    The differentiating property of DMDA-6200 is not density alone but the combination of melt strength and ESCR. Injection moulding HDPE at 20–50 g/10 min fills thin-wall closures with lower clamp force but cannot maintain a stable parison on a blow moulding die. Fractional-melt bimodal pipe grades at 0.1–0.3 g/10 min provide superior slow crack growth resistance under ISO 13479 but are unsuitable for blow moulding because of high melt pressure and limited parison drawdown. General-purpose blow moulding HDPE at 0.60–1.0 g/10 min may run faster in small bottles but often sacrifices ESCR and pinch-off weld strength. DMDA-6200 is therefore specified where container ESCR and drop-impact integrity are ranked higher than maximum output or thin-wall cycle time.

    ParameterHDPE DMDA-6200General-purpose blow moulding HDPEInjection moulding HDPEBimodal pipe HDPE
    Melt mass-flow rate (190 °C, 2.16 kg)0.40–0.50 g/10 min0.60–1.0 g/10 min20–50 g/10 min0.1–0.3 g/10 min
    Density0.951–0.955 g/cm³0.950–0.956 g/cm³0.952–0.958 g/cm³0.946–0.950 g/cm³
    Primary processing distinctionHigh-melt-strength continuous blow mouldingFaster cycle blow mouldingLow-pressure cavity fillLong-term hydrostatic strength
    ESCR relevanceHigh for detergent/agrochemical packagingModerateNot typically specifiedVery high, with slow crack growth resistance

    Within the producer’s HDPE blow moulding portfolio, grades with higher melt flow are preferred for <1 L high-speed shuttle lines; grades with lower melt flow and higher density may be selected for 200 L drums. DMDA-6200 occupies the intermediate segment, matching 5–25 L containers where programmed parison control is available and where the filled-product weight creates significant pinch-off and sidewall stress.

    Regulatory compliance for finished articles falls under the converter’s responsibility. Polyethylene resins in this class are often evaluated for food-contact use under GB 4806.6-2016, FDA 21 CFR §177.1520, and EU Regulation (EU) No 10/2011 as amended. For non-food chemical packaging, relevant requirements include REACH Article 33 communication obligations and, where applicable, RoHS Directive 2011/65/EU. The resin should not be processed at melt temperatures above 220 °C for extended periods because thermal-oxidative degradation can increase gel particle formation and reduce ESCR. Accumulator-head machines should be purged before shutdown to avoid long residence times in the head. DMDA-6200 is not suitable for pressure pipe or hot-fill applications requiring long-term hydrostatic strength under ISO 9080; its design window is for non-pressure, ambient-temperature rigid packaging. Mixing with other HDPE lots or recycled regrind is possible, but the addition of post-consumer recyclate above 30 wt % can alter die swell, ESCR, and pinch-off weld strength in ways that are not described by the original lot-release data.

    Processors should verify melt temperature with a needle pyrometer inserted into the parison immediately after the die exit. Barrel setpoints alone are insufficient because shear heating in the extruder can raise actual melt temperature by 5–15 °C, depending on screw speed and back pressure. The recommended die-head temperature band of 190–205 °C should be interpreted with this measured melt temperature, not with the machine controller display alone.

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