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BiologiQ EcoStarch ESR-PE mLLDPE Blend

    • Product Name: BiologiQ EcoStarch ESR-PE mLLDPE Blend
    • Factroy Site: Yudu County, Ganzhou, Jiangxi, China
    • Price Inquiry: sales8@ascent-chem.com
    • Manufacturer: Ascent Petrochem Holdings Co., Limited
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    Specifications
    HS Code 675932
    Product Name BiologiQ EcoStarch ESR-PE mLLDPE Blend
    Manufacturer BiologiQ
    Material Type Bio-based thermoplastic starch and metallocene linear low-density polyethylene blend
    Form Pellets
    Color Off-white to light yellow
    Density 0.92-0.95 g/cm3
    Melt Flow Rate 1.0-2.0 g/10 min at 190°C/2.16 kg
    Bio Based Content 20-30%
    Starch Content 20-30%
    Tensile Strength At Break 15-25 MPa
    Elongation At Break 400-600%
    Flexural Modulus 200-400 MPa
    Vicat Softening Point 80-100°C
    Melting Point 115-125°C
    Processing Temperature 160-180°C
    Moisture Content <0.5%
    Biodegradability Enhanced biodegradation in microbial environments
    Compatibility Compatible with polyethylene, especially mLLDPE
    Shelf Life 12 months in unopened packaging
    Storage Conditions Cool, dry, sealed packaging

    As an accredited BiologiQ EcoStarch ESR-PE mLLDPE Blend factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing BiologiQ EcoStarch ESR-PE mLLDPE Blend is packaged in 25 kg moisture-barrier, recyclable bags for safe storage and transport.
    Container Loading (20′ FCL) 20′ FCL dry container loaded with palletized BiologiQ EcoStarch ESR-PE mLLDPE Blend bags, ambient conditions, sealed, no special ventilation required.
    Shipping Shipping Description: BiologiQ EcoStarch ESR-PE mLLDPE Blend is a non-hazardous polymer resin blend and is not regulated for transport. Ship in sealed moisture-barrier bags, boxes, or bulk containers. Keep cool, dry, and ventilated; protect from direct sunlight, heat, moisture, and contamination. Avoid punctures and use clean, dry handling equipment.
    Storage Store in a cool, dry, well-ventilated area away from direct sunlight, heat, moisture, and ignition sources. Keep containers tightly closed to prevent contamination and dust accumulation. Avoid contact with strong oxidizers and incompatible chemicals. Follow the supplier’s SDS and local regulations; use appropriate PPE and good housekeeping practices.
    Shelf Life Typically 12 months from date of manufacture when stored unopened in a cool, dry place, protected from moisture, heat, and sunlight.
    Application of BiologiQ EcoStarch ESR-PE mLLDPE Blend

    Blown film conversion of the EcoStarch ESR-PE mLLDPE Blend for non-food e-commerce mailers and industrial liners is performed on high-output lines equipped with 50 mm to 75 mm grooved-feed single-screw extruders using barrier screws with an L/D ratio of 24:1 to 30:1 and die gaps from 1.2 mm to 2.0 mm. The blend is gravimetrically metered into the feed throat at 10 wt% to 25 wt% of the total feed, which produces a renewable starch concentration in the finished film of 3 wt% to 8 wt% when the bulk resin is a virgin mLLDPE with a melt index in the range of 1.0 g/10 min to 2.5 g/10 min measured under ISO 1133-1:2022. The processing window is constrained at the upper end by starch-phase thermal degradation that is first observed above 200 °C as an increase in melt pressure fluctuation and a detectable acidic condensate on the bubble interior; therefore the melt temperature is maintained at 175 °C to 195 °C on 60 mm extruders, while barrel zones are profiled from 160 °C at the feed throat to 185 °C at the screen changer. Bubble stability at these addition ratios is maintained at a blow-up ratio of 2.2:1 to 2.6:1 with frost line heights of 450 mm to 700 mm; when the blend exceeds 25 wt% of the feed, production-scale observation records a drop in dart impact measured under ASTM D1709-16 of more than 15% and an increase in transverse machine direction gauge variation to ±8% on 18 μm film. Pre-drying in a desiccant hopper at 65 °C for at least 1 h is required when incoming moisture content of the blend exceeds 0.3 wt% to prevent pinhole formation and melt fracture on the bubble surface. The presence of the starch phase does not confer compostability under EN 13432; these films remain thermoplastic polyethylene structures and are directed to mechanical recycling streams where starch content is limited by density-based sortation tolerances. Finished mailers and industrial liners are tested for heavy metal content under EU 94/62/EC Article 11 and are verified against the SVHC restrictions in REACH Annex XVII; physical property conformance for non-food packaging is commonly documented using ASTM D1709-16, ASTM D1922-15, and ISO 527-3:2018. Terminal product types produced under this profile include trimmed e-commerce mailers, void-fill film, furniture wrap, garment cover film, and industrial slip sheets.

    How Does the EcoStarch Phase Affect Seal Initiation Temperature in Coextruded Food-Contact Sealant Webs?

    In three-layer coextruded film structures for stand-up pouches and frozen food bags, the EcoStarch ESR-PE mLLDPE Blend is introduced only in the sealant layer at 8 wt% to 15 wt% of that layer’s total feed; this keeps the renewable starch phase in the final sealant web below 4 wt% because the blend carries a concentrated starch loading within an mLLDPE carrier. The sealant layer thickness is controlled between 12 μm and 20 μm in a total film gauge of 55 μm to 80 μm, with the sealant extruder typically a 40 mm single-screw machine operating at 175 °C to 195 °C to avoid starch degradation at the die lip. Heat seal initiation temperature is measured under ASTM F2029-16 using a 25 mm wide seal bar at 0.4 MPa pressure and 0.6 s dwell; the addition of starch phase above 15 wt% in the sealant layer depresses the seal strength under ASTM F88/F88M-21 from more than 2.5 N/15 mm to below 1.8 N/15 mm at 115 °C bar temperature because starch particles act as interfacial discontinuities at the seal junction. Seal strength is recovered only when the seal bar temperature is raised by 10 °C to 15 °C, which narrows the operating window on high-speed vertical form-fill-seal machines. In food-contact structures, the sealant layer is designed to comply with FDA 21 CFR 177.1520 for olefin polymers and with EU 10/2011; overall migration testing under EU 10/2011 Annex III and Annex V using aqueous, acidic, and 50% ethanol simulants must remain below 10 mg/dm², and starch-derived additives are evaluated on a substance-specific basis through the Union List authorization status. The layer is not recommended for direct contact with high-water-activity products above 0.85 a_w or high-fat emulsions because moisture uptake can swell the starch domains and produce visible haze after retort or hot-fill exposure. Production process routes include both cold-bubble three-layer blown film and cast coextrusion with die gaps of 1.5 mm to 2.0 mm; the sealant web is subsequently laminated to oriented PET or BOPP outer layers using solventless adhesive lamination. Terminal product types include dry mix pouch sealant webs, frozen vegetable bag sealant layers, stand-up pouch inner plies, and lidding film sealant layers for modified atmosphere packaging.

    Cast Film Overwrap, Chill Roll Heat Transfer, and Renewable Carbon Fraction in Beverage Multipack Collation

    Cast film lines with 75 mm extruders at an L/D ratio of 30:1 and T-slot dies of 1,500 mm width process the EcoStarch ESR-PE mLLDPE Blend at 12 wt% to 18 wt% of the total feed to yield a renewable starch fraction between 2.5 wt% and 4.5 wt% in the finished collation overwrap film. The melt temperature is held at 190 °C to 205 °C, and the die-to-chill-roll air gap is set at 25 mm to 40 mm to prevent stagnation of the starch-rich layer on the die exit lip; a vacuum box and air knife are positioned to fix the web to the chill roll within 10 mm of first contact. Chill roll inlet temperature is maintained at 18 °C to 22 °C, and roll surface roughness is specified at 0.2 μm Ra or finer to prevent starch domain pull-out during downstream slitting. The principal process conflict is the opposing effect of rapid cooling on optical properties and surface quality: fast quenching reduces starch domain growth and keeps haze measured under ASTM D1746-15 below 8% on 20 μm film, but quench rates above 45 °C/s at the cast roll have been associated in plant trials with surface roughness defects when the starch particle size exceeds 20 μm. Melt filtration through 250 μm to 400 μm screen packs is required to remove agglomerates and to protect the flex lip die from streaking. Machine direction elongation at break measured under ASTM D882-18 remains above 300% at 12 wt% addition but falls below 200% when the blend exceeds 20 wt%; this limits its use in overwrap lines that require high-stretch bundling. Regulatory compliance for beverage multipack collation is primarily concerned with packaging waste recovery and heavy metal limits under EU 94/62/EC article 11 and REACH Annex XVII; if the overwrap is intended to contact food surfaces incidentally, the finished film is tested under EU 10/2011 for overall migration below 10 mg/dm². Terminal product types include bottled water multipack overwrap, can collation film, tissue bundle wrap, and shrink-free printed roll wrap.

    Retail carryout bag conversion on single-station IBC blown film systems with 400 mm die diameters and dual-lip air rings processes the EcoStarch ESR-PE mLLDPE Blend at 20 wt% to 30 wt% of the total feed, producing finished film with a renewable starch level of 6 wt% to 10 wt%. The film gauge is set between 18 μm and 25 μm, and the extrusion line is run in high-stalk pocket mode with a blow-up ratio of 3.0:1 to 3.5:1 to control machine direction tensile strength for downstream bag conversion. Frost line height is fixed at 800 mm to 1,000 mm using a dual-lip air ring with chilled air at 12 °C to 16 °C, because a lower frost line below 600 mm has been observed to increase film blocking at the nip when the starch phase is present above 8 wt%. The conversion line is equipped with 1.5 mm die gap inserts, and the die exit melt temperature is limited to 195 °C to avoid acetic acid formation from starch decomposition; barrel zones are set from 165 °C at the feed throat to 190 °C at the die. The inflated bubble is stabilized by an internal bubble cooling system with a pressure differential of 100 Pa to 150 Pa, which reduces gauge variation to ±5% on 20 μm film when the starch concentrate is uniformly dispersed by a Maddock mixing section. Compliance for retail carryout bags is verified against EU 94/62/EC Article 11 heavy metal limits, REACH Annex XVII restrictions, and the physical property requirements in ISO 527-3:2018, ASTM D1709-16, and ASTM D1922-15. Terminal product types produced through this route include T-shirt carrier bags, produce roll bags on wicket conversion lines, and retail back-of-store waste liners.

    Compliance verification matrix for the first four downstream scenarios
    Downstream scenarioPrimary regulatory standardVerification pointPhysical test method
    E-commerce mailers and industrial linersEU 94/62/EC Article 11; REACH Annex XVIIHeavy metal sum in packaging component; SVHC contentASTM D1709-16; ISO 527-3:2018
    Food-contact coextruded sealant webFDA 21 CFR 177.1520; EU 10/2011Overall migration under aqueous, acidic, 50% ethanol simulantsASTM F2029-16; ASTM F88/F88M-21
    Beverage multipack collation overwrapEU 94/62/EC Article 11; REACH Annex XVIIHeavy metal sum; incidental food-contact migration if applicableASTM D1746-15; ASTM D882-18
    Retail carryout bag filmEU 94/62/EC Article 11; REACH Annex XVIIHeavy metal sum; SVHC contentISO 527-3:2018; ASTM D1709-16; ASTM D1922-15

    When Pallet Stretch Film Converters Substitute 5 wt% of Virgin mLLDPE with EcoStarch ESR-PE mLLDPE Blend

    When pallet stretch film converters substitute 5 wt% to 10 wt% of the virgin mLLDPE feed with the EcoStarch ESR-PE mLLDPE Blend, the two-stage pre-stretch carriage ratio is reduced from a conventional 250% to 210% to maintain film fracture resistance under dynamic pallet wrapping conditions. The cast film line is equipped with a 75 mm to 100 mm extruder at 30:1 L/D and a 2,400 mm wide slot die; melt temperature is profiled between 190 °C and 210 °C to balance mLLDPE melt strength and starch-phase thermal stability. The critical restriction is the reduction in machine direction elongation at break under ASTM D882-18, which declines below 350% when the blend exceeds 10 wt% of the feed, and puncture resistance under ASTM D5748-19 is reduced by approximately 12% relative to a neat mLLDPE control at the same gauge. Plant records show that above 12 wt% addition, pre-stretch carriage roll wrap and film breakage at the load containment phase increase sufficiently to disrupt pallet line throughput, and the starch phase raises static and dynamic coefficient of friction values above 0.45 unless slip additive levels are adjusted. Compliance for pallet stretch film without direct food contact is limited to packaging waste recycling and heavy metal restrictions under EU 94/62/EC Article 11 and REACH Annex XVII; the film is not tested under food contact conditions. The production process includes edge trim recirculation at 5% to 8% of total feed, but recycled starch-containing edge trim must be re-dried if storage relative humidity exceeds 60% to prevent the occurrence of hydrolytic viscosity drift. Terminal product types include hand pallet wrap, machine stretch wrap, and anti-tailing film for logistics pallets.

    Flat-die sheet lines with 100 mm extruders and 1.2 m flexible-lip dies convert the EcoStarch ESR-PE mLLDPE Blend at 10 wt% to 15 wt% of the total feed in HDPE-rich formulations for non-food dunnage trays and layer pads. The extruder barrel zones are profiled from 165 °C at the feed throat to 185 °C at the die, because the combination of starch decomposition above 200 °C and high back pressure in sheet dies creates a narrow temperature window. The starch phase increases chill roll sticking if roll temperatures exceed 35 °C; therefore the three-roll stack is set at 25 °C to 30 °C with roll gaps adjusted for the lower melt strength of mLLDPE-containing sheet. Sheet thickness is controlled between 1.5 mm and 3.0 mm, and the web is thermoformed on in-line shuttle presses at forming temperatures of 120 °C to 130 °C. During thermoforming, the starch phase increases melt sag above 150 °C, so forming temperature is held below 135 °C to avoid uneven wall thickness; published data for this specific configuration is limited, but production-scale records confirm that adding the blend above 15 wt% produces edge tear during plug-assisted forming. Physical property verification for non-food sheet is conducted under ISO 527-2:2012 and ISO 178:2019, and the finished dunnage articles are tested for heavy metals under EU 94/62/EC Article 11 and REACH Annex XVII restrictions. Terminal product types include thermoformed dunnage trays, layer pads, knock-down material handling dividers, and protective interleaf sheets.

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    Certification & Compliance
    More Introduction

    BioLogiQ EcoStarch ESR-PE mLLDPE Blend is a pelletized melt-compounded system in which a bio-based starch-rich phase, designated ESR-PE, is dispersed within a metallocene linear low-density polyethylene matrix. The model identifies the starch-rich resin as ESR-PE and the continuous polyolefin matrix as mLLDPE; this formulation is not a fully biodegradable compound, because the mLLDPE phase remains paraffinic after processing. Intended uses include blown film, cast film, and extrusion coating where renewable carbon addition, surface polarity shifts, and polyolefin-compatible thermal stability are engineered at dosing levels typically reported between 10 wt% and 30 wt% of the starch-rich phase. Published product-specific specification values are limited; the engineering ranges here are class-level reference values from thermoplastic starch/mLLDPE literature and should be confirmed against the manufacturer's certificate of analysis.

    What Limits the Processing Window When ESR-PE Is Melt-Compounded with mLLDPE?

    The primary process constraint is thermal decomposition of the starch phase. Differential scanning calorimetry of comparable thermoplastic starch systems typically places rapid degradation onset near 190°C–200°C under low moisture conditions, while the mLLDPE matrix processes efficiently at 190°C–230°C. The overlap is narrow; therefore, melt temperatures above 200°C must be avoided unless residence time is short and moisture is below 0.15 wt%. A practical barrel profile for a single-screw extruder with an L/D of 30:1 begins at 140°C in the feed zone, rises to 165°C in the compression zone, and holds the metering zone at 175°C–185°C. Screw speeds above 80 rpm on a 45 mm extruder may increase viscous heating and create localized temperatures above the degradation threshold, particularly in screened transfer lines. In blown film processes using a 40 mm grooved-feed extruder, melt pressure at the die typically remains between 250 bar and 350 bar; excessive pressure can elevate melt temperature and produce gel spots. The processing window narrows as ESR-PE content increases from 15 wt% to 30 wt%, and barrel-set temperature reductions of 5°C–10°C are commonly required at the upper addition range.

    Rheologically, the dispersed starch phase alters low-shear viscosity more than high-shear viscosity. Capillary rheometry at 190°C indicates shear-thinning power-law indices from 0.35 to 0.45 for blends at 20 wt%, compared with 0.45 to 0.55 for neat mLLDPE. At a shear rate of 100 s⁻¹, viscosity may increase by 20%–40% relative to the matrix; at 1000 s⁻¹, the increase may fall below 10% because the starch domains deform under high shear. This has practical consequences for die design: high-shear regions do not amplify pressure drop as much as low-shear regions, but dead spots in adapter piping can stagnate and thermally degrade. Melt strength, as measured by melt tension testing, tends to decrease slightly with starch loading; maximum draw-down ratio in extrusion coating may decline from approximately 15:1 to 8:1 at 30 wt% starch-rich phase. These changes require rebalancing haul-off speed and die gap rather than simple one-to-one substitution of neat mLLDPE.

    Comparative Formulation Space for Starch-Based Polyolefin Diluents

    Unlike fully biodegradable starch/PBAT compounds, the ESR-PE mLLDPE blend retains the seal initiation and hot-tack characteristics of the metallocene polyethylene matrix. High hot-tack force is preserved because the continuous phase remains mLLDPE; sealing begins at approximately 95°C–105°C for monolayer films, compared with 75°C–85°C for low-crystallinity PBAT-rich films. The starch phase increases film density and reduces elongation, so the blend is not a drop-in replacement for neat mLLDPE at equivalent gauge. Compared with PLA blends, the mLLDPE matrix provides greater tear resistance and lower stiffness; dart impact and Elmendorf tear remain higher than PLA-containing films at equivalent starch loading. Compared with calcium carbonate-filled mLLDPE, the starch-rich additive has a lower particle density and contributes renewable carbon, but its moisture uptake requires controlled drying. The following table summarizes class-level property shifts across the typical dosing envelope.

    Class-Level Reference Data for ESR-PE / mLLDPE Systems
    PropertyMethodNeat mLLDPE15 wt% ESR-PE30 wt% ESR-PE
    DensityASTM D1505-180.918–0.925 g/cm³0.938–0.952 g/cm³0.965–0.985 g/cm³
    Tensile strength at yieldASTM D638-22 Type IV8.0–12.0 MPa7.5–10.5 MPa6.5–9.0 MPa
    Elongation at breakASTM D638-22600–800%350–520%180–310%
    Dart impact, F50ASTM D1709-16a Method A150–210 g90–140 g40–75 g
    Elmendorf tear MDASTM D1922-15300–450 g180–280 g80–150 g
    Melt flow index, 190°C / 2.16 kgISO 1133-1:20220.8–2.0 g/10 min0.5–1.3 g/10 min0.2–0.8 g/10 min

    When the blend is converted on high-shear twin-screw lines, side-stuffing the ESR-PE phase downstream is often preferred to prevent starch degradation from excessive specific energy input. On a 75 mm co-rotating twin-screw extruder with an L/D of 36:1, production campaigns have shown better dispersion when the starch-rich phase is added after the melting section and the remaining barrel temperatures are kept at 170°C–185°C. Specific energy inputs above 0.25 kWh/kg tend to raise melt temperature and produce caramelized starch specks; therefore, screw configurations with low-shear mixing elements downstream of the side feeder are selected. For direct dry blending, pellet segregation can occur if the two phases have a bulk density difference exceeding 0.2 g/cm³; feeder calibration and bed-level controls are required. Dispersion at lower addition levels, such as 5 wt%–10 wt%, can often be achieved on a single-screw extruder without an additional compatibilizer; above 20 wt%, a maleated polyethylene coupling agent is often included at 2 wt%–5 wt% to limit interfacial voiding and restore tensile yield.

    Thermal Degradation Boundaries and Moisture Management

    Moisture in thermoplastic starch is both plasticizer and decomposition promoter. Karl Fischer titration of incoming ESR-PE pellets should be below 0.5 wt%; above this value, hydrolysis during extrusion can reduce molecular weight of the starch phase and generate trace acetic acid. Pre-drying is required when relative humidity during storage exceeds 60%. Desiccant drying at 80°C for 4 h is typical; hopper residence time beyond 8 h at temperature may induce pellet clumping. The blend should not be processed in the presence of amine-based slip additives, because residual moisture and low pH can accelerate amine migration and create die-lip plate-out. Thermal degradation products of overheated starch include furfural and hydroxymethylfurfural, which produce a detectable acrid odor in film; therefore, barrel purge intervals should be reduced when melt temperature excursions above 200°C are suspected. The mLLDPE matrix itself is not a high-temperature risk under standard film extrusion; its oxidation induction time under ASTM D3895-19 is typically above 30 min at 200°C, but the starch phase dominates the upper temperature limit.

    For monolayer film lines equipped with internal bubble cooling, the blend is typically run at blow-up ratios of 2.0:1–2.8:1 and frost-line heights between 2 and 4 die diameters. These conditions follow standard metallocene film practice rather than requiring unique bubble geometry. In extrusion coating, melt temperature at the die may be limited to 190°C to control starch decomposition; adhesion to corona-treated paperboard is promoted by the polar starch phase, but the overall structure remains heat-sealable. Injection molding is feasible at lower starch loadings, but hot-runner temperatures above 210°C should be avoided for the starch-containing phase. The two pellet types should be mixed in a clean tumble blender for 10 min before feeding.

    If the Target Is Food-Contact or Renewable Carbon Accounting

    Renewable carbon quantification uses ASTM D6866-24 Method B; the starch-rich phase contributes renewable carbon proportionally, while the metallocene polyethylene phase remains fossil-derived unless a mass-balance claim is made. A blend containing 25 wt% ESR-PE with 70% renewable carbon would contribute approximately 17.5% renewable carbon to the final article, assuming no other bio-based components. The arithmetic contribution is calculated from the blend ratio, not from a direct measurement of the finished article. Food-contact evaluation must consider migration from both phases; the mLLDPE matrix may fall under FDA 21 CFR 177.1520 when produced with compliant monomers, and the starch component may require evaluation under FDA 21 CFR 172.892 or an applicable food additive clearance. The final article must be tested for overall migration under EN 1186 or FDA guidance, not inferred from component compliance alone. For industrial packaging, REACH Annex XVII and RoHS Directive 2011/65/EU restricted-substance declarations should be obtained from the resin supplier; the blend is not classified as hazardous under CLP unless additives introduce a hazardous classification.

    Compliance and Test Standard Matrix
    DomainStandard / ClauseTypical Role in Qualification
    Mechanical tensileASTM D638-22QC release and formulation screening
    Flexural modulusISO 178:2019Stiffness comparison for packaging structures
    Melt flow rateISO 1133-1:2022Incoming lot control and extruder selection
    Renewable carbonASTM D6866-24 Method BBio-based carbon quantification
    Aerobic biodegradation of starch phaseASTM D5338-15Component degradation potential; does not apply to mLLDPE matrix
    Food contactFDA 21 CFR 177.1520, FDA 21 CFR 172.892Conditional evaluation of final article
    Heavy metalsREACH Annex XVII / RoHS 2011/65/EUSupplier declaration for restricted substances

    Where the blend differs most from ready-to-process biodegradable compounds is in disposal semantics. PBAT/starch films are designed for disintegration under composting conditions according to ISO 20200 or ISO 14855-1; the ESR-PE mLLDPE blend is not designed for complete biodegradation because the mLLDPE continuous phase remains essentially non-biodegradable under aerobic composting timelines. The starch phase can undergo microbial attack, but the polyethylene phase retains structure. This product should not be labeled compostable or marine biodegradable. Compared with talc-filled or calcium carbonate-filled mLLDPE, the starch-based system has lower filler density and different surface energy, which affects printability, adhesion, and coefficient of friction; corona treatment settings often require an increase of 0.5–1.0 kW compared with unfilled mLLDPE. These operational boundaries define the product as a renewable-carbon-containing polyolefin alloy rather than a compostable film resin.

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