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Inner Mongolia Baofeng LLDPE DFDA7042

    • Product Name: Inner Mongolia Baofeng LLDPE DFDA7042
    • 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 592341
    Polymer Type Linear Low-Density Polyethylene (LLDPE)
    Comonomer Butene-1
    Form Pellets
    Color Natural
    Density 0.918-0.922 g/cm³
    Melt Flow Rate 190 C 2 16 Kg 1.7-2.3 g/10 min
    Melting Point 120-125 °C
    Vicat Softening Point ≥90 °C
    Tensile Strength At Yield ≥8 MPa
    Tensile Strength At Break ≥17 MPa
    Elongation At Break ≥500%
    Dart Impact Strength ≥80 g
    Haze ≤12%
    Gloss ≥45%
    Coefficient Of Friction 0.2-0.4
    Brittleness Temperature ≤ -70 °C
    Ash Content ≤0.03%
    Moisture Content ≤0.05%
    Bulk Density ≥0.55 g/cm³
    Fish Eyes ≤20 pcs/1200 cm²

    As an accredited Inner Mongolia Baofeng LLDPE DFDA7042 factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing Inner Mongolia Baofeng LLDPE DFDA7042 is packed in 25 kg PP woven bags, usually 1,000 kg per pallet.
    Container Loading (20′ FCL) 20′ FCL container loading: Inner Mongolia Baofeng LLDPE DFDA7042, packed in 25kg bags, 25MT loose, no pallets, moisture-protected.
    Shipping Inner Mongolia Baofeng LLDPE DFDA7042 is a non-hazardous linear low-density polyethylene resin. Not classified as dangerous goods; UN number not applicable, no hazard class. Packed in 25 kg bags or jumbo bags. Ship as general cargo by sea, road, or rail. Keep dry and away from heat.
    Storage Store Inner Mongolia Baofeng LLDPE DFDA7042 in a cool, dry, well-ventilated warehouse, away from direct sunlight, heat, ignition sources, and moisture. Keep bags sealed and palletized; avoid contact with oils, acids, alkalis, and other contaminants. Do not stack excessively to prevent deformation. Rotate stock first-in, first-out, and follow the supplier’s SDS and local regulations.
    Shelf Life Inner Mongolia Baofeng LLDPE DFDA7042 shelf life: typically 24 months stored cool, dry, ventilated, away from sunlight, moisture, and heat.
    Application of Inner Mongolia Baofeng LLDPE DFDA7042

    In monolayer agricultural greenhouse cover film lines, Inner Mongolia Baofeng DFDA7042 is incorporated at 65–85 wt%, LDPE 2420H at 10–20 wt%, and a HALS/UV stabiliser masterbatch at 1.5–3.0 wt% to meet multi-season exposure requirements. The resin shows a melt flow rate of 2.0 g/10 min at 190°C/2.16 kg per ISO 1133-1:2022 and a density of 0.918–0.922 g/cm³ per ISO 1183-1:2019. For greenhouse and low-tunnel covering films, the applicable product standard is EN 13206:2017; when the same film is used as a silage cover or bale wrap in contact with animal feed, migration assessment under (EU) No 10/2011 is required for food-producing environments. On a 75 mm grooved-feed blown film extruder with L/D 30:1 and Maddock mixing section, the resin is processed at melt temperature 185–210°C, die gap 1.8–2.4 mm, blow-up ratio 2.0:1–3.0:1, and frost line height 8–10 die diameters. Terminal products are greenhouse covers at 80–200 µm and low-tunnel films at 40–80 µm. The operational boundary is set by the butene-copolymer chain structure: above 85 wt% DFDA7042, bubble stability on wide die lips declines when line speed exceeds 15 m/min per metre of die circumference, and below 1.5 wt% HALS, high-UV sites exhibit tensile strength loss of more than 25% after 18 months. At storage relative humidity above 60%, the stabiliser and anti-drip masterbatch is pre-dried at 60–70°C for 4 h to prevent hydrolysis and bubble-stability loss from vapour. Incompatibilities include unneutralised acid scavengers in certain EVA blends, which can deactivate HALS and reduce thermo-oxidative stability. Published data for the specific silage-conversion configuration is limited, but EN 13206:2017 classification does not cover biodegradable films and does not replace agronomic UV dose testing for single-season versus multi-season coverings.

    PropertyTest methodCommercial window
    Melt flow rate, 190°C/2.16 kgISO 1133-1:20222.0 ± 0.3 g/10 min
    DensityISO 1183-1:20190.918–0.922 g/cm³
    Tensile strength at break, MD/TDASTM D882, ISO 527-3≥35 / ≥30 MPa at 50 µm, BUR 2.5:1
    Elongation at break, MD/TDASTM D882, ISO 527-3≥500 / ≥600%
    Dart impact, Method AASTM D1709≥120 g at 50 µm
    Elmendorf tear, MD/TDASTM D1922≥3.5 / ≥4.5 N
    HazeASTM D10035–12%

    What Limits Hot-Tack Strength in Dry-Food Lamination Sealants?

    Dry-food lamination sealant webs based on DFDA7042 are formulated at 70–85 wt% DFDA7042, 10–20 wt% LDPE 2420H, and 1–3 wt% silica/erucamide slip-antiblock masterbatch. The web is extruded as a monolayer or coextruded sealant layer of 25–60 µm on blown film equipment with die gap 1.5–2.0 mm, blow-up ratio 2.5:1–3.0:1, and melt temperature 190–215°C; in adhesive lamination, the film is corona-treated in-line to 38–42 dyn/cm and laminated against BOPET or OPP using a two-component polyurethane adhesive. Food-contact status is governed by FDA 21 CFR 177.1520(c), which includes density and extractable-fraction requirements for olefin polymers, and by (EU) No 10/2011 with an overall migration limit of 10 mg/dm² and specific migration limits for Annex I additives. Terminal product types include bread bags, frozen vegetable pouches, cereal liners, and dry snack pre-made pouches. The critical limitation is hot-tack strength: butene-copolymer LLDPE typically exhibits 2.0–3.5 N/25 mm at 120–140°C per ASTM F1921, which restricts vertical form-fill-seal speed and leads to seal contamination if the seal-bar temperature exceeds 145°C. Unlike C6 or C8 LLDPE, the butene branch distribution produces a lower hot-tack plateau and a narrower seal-integrity window, so the formulation cannot be used for retort or high-temperature pasteurisation pouches. Erucamide concentration is matched to the lamination curing cycle: at 0.3 wt% or above, post-lamination bond strength can decline from 2.5 N/15 mm to below 1.5 N/15 mm after 48 h of polyurethane curing at 40°C because migration to the corona-treated surface competes with adhesive wetting. Coefficient of friction is measured by ASTM D1894 with a target of 0.25–0.45; tensile properties are checked by ASTM D882 or ISO 527-3 using 25.4 mm wide specimens at a crosshead speed of 500 mm/min.

    ApplicationCompliance instrumentQuantitative limitation
    Dry-food sealantFDA 21 CFR 177.1520(c)Polymeric olefin conditions; extractable fraction per sub-clause
    EU dry food(EU) No 10/2011Overall migration ≤10 mg/dm²; Annex I SMLs
    Agricultural coverEN 13206:2017Covering film classification; UV performance classes
    Surface protectionRoHS 2011/65/EUPb ≤0.1 wt%, Cd ≤0.01 wt%, Hg ≤0.1 wt%, Cr(VI) ≤0.1 wt%, PBB/PBDE ≤0.1 wt%
    Household refuse sacksEN 13592:2017Dart impact and tear requirements by class

    Heavy-Duty Sack Film Tear-Propagation Resistance and Blown Film Line Parameters

    On high-output blown film lines equipped with internal bubble cooling, DFDA7042 is compounded for heavy-duty shipping sacks at 40–60 wt% DFDA7042, 30–40 wt% HDPE, 10–20 wt% LDPE, and carbon black masterbatch at 2–4 wt% where UV stability is required. The terminal film thickness is 80–180 µm, with product types such as fertiliser sacks, polymer resin sacks, and mineral aggregate sacks. Processing occurs with screw L/D 28:1–32:1, die gap 2.0–2.8 mm, blow-up ratio 2.0:1–4.0:1, and melt temperature 200–230°C. For industrial shipping sacks used in non-food distribution, the governing instruments are performance acceptance standards ASTM D1709 Method A, ASTM D1922, and ISO 527-3, with no food-contact compliance required unless the sack is used for direct agricultural produce. The process conflict is that raising DFDA7042 content above 60 wt% improves dart impact energy but reduces flexural stiffness and bubble stability, and at 65 wt% the film approaches a property cliff-edge where top-load creep under stacked pallet loads increases. To prevent melt fracture at high shear rates, a PPA processing aid is added at 400–800 ppm when die gap is below 1.6 mm; butene-copolymer LLDPE has a reported critical shear stress for melt fracture at approximately 0.25 MPa, and visually detectable sharkskin on the inner bubble wall indicates that line speed must be reduced or the die gap widened.

    When DFDA7042 is converted into consumer refuse sacks and drawstring can liners, the formulation is typically compounded at 60–80 wt% DFDA7042, 10–25 wt% post-industrial LDPE, and calcium carbonate masterbatch at 5–15 wt%. The product standard for household waste sacks is EN 13592:2017, with dart impact and tear resistance classified by sack size and film thickness; no food-contact migration assessment is required for non-food refuse bags. The extrusion line is a monolayer blown film system with die gap 1.5–2.0 mm, blow-up ratio 3.0:1–4.0:1, melt temperature 185–210°C, and automatic gauge control with ±5% tolerance around the 25–45 µm target. Terminal products include star-seal refuse sacks, drawstring kitchen can liners, and janitorial waste bags. The filler addition reduces polymer cost but decreases dart impact and increases the probability of pinhole defects when the film is drawn below 20 µm; calcium carbonate grades with surface treatment should be dispersed in a separate masterbatch and not dry-blended at high shear, because agglomerates cause gel-like specks in the bubble.

    Surface Protection Webs Are Coextruded Over EVA-Based Tack Layers

    In temporary surface protection for aluminium profile, stainless steel sheet, and furniture panel lines, DFDA7042 is used as the backing layer at 60–80 wt%, coextruded with an EVA tack layer at 20–40 wt% based on EVA with vinyl acetate content of 14–18%. The two-layer blown film line uses die gap 1.6–2.2 mm, blow-up ratio 2.0:1–3.0:1, melt temperature 190–210°C for the LLDPE layer and 160–180°C for the EVA layer, with total film thickness of 40–60 µm. Terminal product types are temporary protective films for high-gloss metal surfaces, furniture edging, and glass or electronics assembly. Compliance for electrical and electronic substrate protection requires RoHS 2011/65/EU with lead ≤0.1 wt%, cadmium ≤0.01 wt%, mercury ≤0.1 wt%, hexavalent chromium ≤0.1 wt%, and PBB/PBDE ≤0.1 wt%; peel adhesion is measured by ASTM D3330, and tensile properties by ISO 527-3. A processing limitation is that EVA tack-layer migration under high-temperature storage above 45°C can leave visible residue on polished surfaces, and the DFDA7042 backing has no inherent UV-blocking unless carbon black or a REACH-compliant UV absorber is added at 2–4 wt%.

    When Thin-Gauge Garment Film Requires a Butene-Copolymer Melt

    Thin-gauge garment bags and checkout/produce bags based on DFDA7042 are formulated at 70–85 wt% DFDA7042, 10–20 wt% LDPE, and a slip/antiblock masterbatch at 1–3 wt%. The resin is run on high-stalk blown film towers, where the die gap is 0.8–1.2 mm, blow-up ratio is 2.0:1–4.0:1, stalk height is maintained at 8–10 die diameters, and melt temperature is 190–210°C. The resulting film thickness is 12–25 µm, with terminal product types including garment bags, produce bags, and lightweight checkout bags. Food-contact status for produce bags is governed by FDA 21 CFR 177.1520(c); mechanical verification uses ASTM D882 and ASTM D1922. The process window narrows below 12 µm because internal bubble cooling and automatic air-ring control are required to prevent bubble flutter and neck-in; above 25 µm, the high-stalk process confers no yield advantage over low-stalk conversion. When anti-block masterbatch is omitted or falls below 1 wt%, film blocking on the collapsing frame can cause web tears on the winder at speeds above 60 m/min.

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    Certification & Compliance
    More Introduction
    The linear low-density polyethylene resin designated DFDA7042 and manufactured at the Inner Mongolia Baofeng Energy polyolefin complex is a butene-1 copolymer film grade supplied as free-flowing pellets. The polymerization system utilizes gas-phase fluidized-bed technology with a Ziegler-Natta catalyst platform, producing a polymer characterized by short-chain ethyl branching derived from butene-1 comonomer incorporation. Under standardized melt index testing at 190°C and 2.16 kg load per GB/T 3682.1-2018 (equivalent to ISO 1133-1:2022), the resin exhibits a melt flow rate specification band of 1.8 to 2.2 g/10 min. Density measured at 23°C per GB/T 1033.2-2008 (equivalent to ISO 1183-2:2019) falls within 0.918 to 0.922 g/cm³. The crystalline melting peak, determined by differential scanning calorimetry per ISO 11357-3:2018 at a heating rate of 10 K/min, occurs in the range of 120°C to 125°C. Crystallinity derived from heat of fusion measurements falls between 45% and 55%, based on the 293 J/g reference enthalpy for fully crystalline polyethylene. These primary specification parameters position the grade within the medium-melt-index class of linear low-density polyethylene resins suited for blown film extrusion, where its balance of melt processability and film toughness is industrially established.

    What Melt Flow, Density, and Mechanical Specifications Define This Grade?

    The specification profile for DFDA7042 is anchored to the classification requirements for linear low-density polyethylene resins established under Chinese national standard GB/T 15182. Property limits tabulated below represent published specification data for this grade designation across domestic producers; individual production lot certificates of analysis commonly exhibit narrower internal control bands.
    PropertyTest MethodUnitSpecification Range
    Melt flow rate (190°C, 2.16 kg)GB/T 3682.1-2018 / ISO 1133-1:2022g/10 min1.8 – 2.2
    Density (23°C)GB/T 1033.2-2008 / ISO 1183-2:2019g/cm³0.918 – 0.922
    Tensile yield stress (50 mm/min)GB/T 1040.2-2022 / ISO 527-2:2012MPa≥ 8.3
    Tensile break stressGB/T 1040.2-2022 / ISO 527-2:2012MPa≥ 12.0
    Elongation at breakGB/T 1040.2-2022 / ISO 527-2:2012%≥ 500
    Dart drop impact (50 µm film)GB/T 9639.1-2008 / ASTM D1709 Method Ag≥ 80
    Tensile testing is performed on compression-molded plaques per GB/T 1040.2-2022 at the specified crosshead speed. Plaque-derived tensile values are understood to differ from blown film tensile measurements, which are governed by melt orientation, cooling rate, and frost line dynamics. Film mechanical performance is evaluated additionally through Elmendorf tear strength per GB/T 16578.2-2009 (equivalent to ISO 6383-2:2003) and haze per GB/T 2410-2008. Fish-eye count and gel content, while not typically included in resin specification sheets, are routinely monitored as film-grade quality indicators. Extrusion of DFDA7042 on conventional single-screw blown film lines requires attention to melt temperature profile, screw geometry, and die configuration. The resin's nominal melt index of 2.0 g/10 min supports throughput on lines with screw diameters from 45 mm to 120 mm, provided the screw includes a barrier section or Maddock mixing element with length-to-diameter ratios between 25:1 and 33:1. Recommended barrel temperature profiles range from 160°C in the feed section to 200°C at the die head, with adaptor temperature maintained at 180°C to 200°C. Melt temperature measured at the die should not exceed 230°C, as prolonged exposure above this threshold accelerates antioxidant depletion and increases gel formation from oxidative crosslinking. Die gap settings of 1.0 to 2.5 mm are industrially common; wider die gaps reduce shear heating and are preferred for high-output lines, while narrower gaps enhance melt orientation for film gauge reduction. Blow-up ratios ranging from 2.0:1 to 3.5:1 provide an optimal balance of transverse and machine direction mechanical properties. Frost line height is typically maintained between 6 and 10 die diameters to allow sufficient melt relaxation before crystallization; higher frost lines favor improved tear strength in the machine direction, while lower frost lines increase transparency at the expense of toughness. Bubble stability for this butene-1 copolymer is adequate within these blow-up ratios, though collapse at ratios above 4:1 may occur without internal bubble cooling or auxiliary stabilization equipment.

    Blown Film Equipment Configuration and Die Gap Effects

    Processing of DFDA7042 at film gauges from 20 µm to 150 µm is industrially established, with the widest production experience concentrated in the 25 µm to 80 µm range for general packaging and agricultural film. Haul-off speed is dictated by the line's cooling capacity and die output; for a 90 mm extruder with a 30 kg/h output rate producing 50 µm film at a 2.5:1 blow-up ratio and 1.5 m lay-flat width, haul-off speed typically ranges from 12 to 18 m/min. This operating point assumes a die diameter of 200 to 250 mm and effective air-ring cooling sufficient to maintain a stable frost line. Winder tension control is critical: the grade exhibits lower melt strength than conventional LDPE due to the absence of long-chain branching, and excessive winding tension above 15 N per meter of web width can induce permanent set in the film roll, leading to telescoping defects and downstream converting problems. Film blocking tendency is moderate; antiblock additive masterbatches at 2% to 5% letdown ratios are commonly employed when required by downstream printing or bag-making operations. Corona treatment of the film surface to 38 to 42 dyn/cm is standard practice for subsequent flexographic or gravure printing adhesion. The primary application domain for DFDA7042 is monolayer and coextruded blown film for general-purpose packaging, agricultural uses, and industrial liners. In agricultural greenhouse film, the resin is typically blended with LDPE at ratios of 20:80 to 50:50 by weight to improve tensile strength and puncture resistance while retaining the optical clarity contributed by the LDPE component. Mulch film applications commonly use the grade at 18 µm to 25 µm gauge, where dart drop impact resistance reduces tearing during mechanical laying. In heavy-duty shipping sacks, the resin is often coextruded as a core or skin layer in three-layer structures, where its elongation at break specification of ≥500% provides energy absorption capacity during drop loading. Industrial liners for chemical packaging utilize the grade in gauges of 100 µm to 150 µm, where conformance to GB/T 11115-2009 for polyethylene resin quality is typically required. The resin's heat seal initiation temperature, determined by differential scanning calorimetry, is approximately 100°C to 105°C, which supports heat sealing operations on form-fill-seal lines operating at seal bar temperatures of 115°C to 130°C. In comparison with hexene-1 and octene-1 comonomer LLDPE grades, the butene-1 structure of DFDA7042 provides a lower cost position while accepting reduced dart impact and tear resistance at equivalent density.

    When Substitution of Conventional LDPE Grades Is Evaluated on Existing Lines

    The comparison between DFDA7042 and conventional low-density polyethylene produced via autoclave or tubular free-radical polymerization is defined by fundamental differences in molecular architecture. LDPE contains long-chain branching that imparts high melt elasticity and strain-hardening behavior in extensional flow; DFDA7042, as a linear short-chain-branched polymer, lacks this extensional thickening mechanism. On blown film lines equipped with low-pressure die heads optimized for LDPE, direct substitution with 100% DFDA7042 commonly produces higher melt temperatures due to increased viscous dissipation, reduced bubble stability at blow-up ratios above 3:1, and a more pronounced tendency toward melt fracture at apparent shear rates exceeding 1,000 s⁻¹. Equipment modifications that mitigate these effects include installation of wider die gaps (2.0 to 2.5 mm), addition of internal bubble cooling, and use of screw designs with lower compression ratios. In terms of finished film performance, DFDA7042 provides substantially higher tensile break strength and puncture resistance at equivalent gauge. Dart drop impact values for 50 µm film are typically 50% to 100% higher than comparable LDPE film due to greater chain entanglement and linear architecture. Elmendorf tear strength in the transverse direction is also superior, though machine-direction tear strength may be lower than LDPE under equivalent orientation conditions. Optical properties are inferior: haze values for monolayer film typically range from 10% to 20% per GB/T 2410-2008, compared to 5% to 8% for LDPE. A systematic comparison against adjacent grades is tabulated below:
    Comparative ParameterDFDA7042DFDA7047LDPE 2426HMetallocene Hexene-1 LLDPE
    Comonomer typeButene-1Butene-1None (free-radical)Hexene-1
    MFR (190°C, 2.16 kg), g/10 min1.8 – 2.20.8 – 1.21.8 – 2.50.8 – 1.2
    Density (23°C), g/cm³0.918 – 0.9220.916 – 0.9200.924 – 0.9260.916 – 0.920
    Primary film applicationGeneral-purpose blown filmHeavy-duty film, geomembraneHigh-clarity packagingHigh-impact specialty film
    Dart drop impact (50 µm)ModerateHigherLowerHighest
    Optical haze10 – 20%Higher5 – 8%Low
    Melt strengthLowModerateHighLowest
    Compliance of DFDA7042 with food-contact requirements is addressed through conformance to GB 4806.6-2016 (National Food Safety Standard for Plastic Resins for Food Contact Use), which specifies overall migration limits of 10 mg/dm² and specific migration limits for constituent monomers and additives. The resin also conforms to European Union framework regulation (EU) No 10/2011 for food-contact plastics when tested under simulant conditions appropriate to polyethylene. Heavy metal content, determined per GB/T 31604.2-2016, is routinely below regulatory thresholds. The resin is not classified as hazardous under Chinese dangerous goods transportation regulations and does not require special handling beyond standard dry storage practices. Storage stability at ambient temperatures below 40°C and relative humidity below 70% is typically maintained for 12 months from production date without measurable deterioration in melt index or color. Pre-drying is not required for this grade under normal storage conditions; however, moisture uptake in high-humidity environments above 80% relative humidity necessitates pre-drying at 70°C to 80°C for 2 to 4 hours in a desiccant dryer to prevent surface defects in extrudate.

    Limitations Involving Barrier Structures and Optical Clarity Requirements

    Deployment of DFDA7042 in multi-layer barrier structures is constrained by the resin's optical properties and interlayer adhesion characteristics. The grade exhibits insufficient transparency for applications requiring see-through product visibility; monolayer haze values in the 10% to 20% range per GB/T 2410-2008 exceed the 5% threshold typically demanded in transparent stand-up pouches or produce wrap. In coextruded structures where DFDA7042 serves as a sealant or strength layer, adhesion to EVOH or polyamide tie layers requires the use of maleic anhydride grafted polyolefin adhesives; direct adhesion to polar barrier resins is not achieved due to the non-polar surface chemistry of polyethylene. Where high-gloss point-of-sale packaging is specified, the resin is unsuitable as a primary outer layer without blending with LDPE at loadings exceeding 50 wt%. Additionally, the grade is not designed for injection molding applications; its narrow molecular weight distribution and medium melt index produce inadequate flow for injection molding at industrial cycle times. For cast film extrusion of high-clarity packaging, hexene-1 or octene-1 comonomer LLDPE grades provide superior dart impact and tear balance; published quantitative comparison data for this specific resin configuration in cast film is limited. The processing window narrows when the grade is compounded with flame-retardant fillers at loadings above 20 wt%, where increased melt viscosity and filler-induced chain scission compete to alter the melt index by more than ±15% from the virgin resin baseline.
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