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BG8800 Blow Molding Polylactic Acid/PBAT Compostable Blend

    • Product Name: BG8800 Blow Molding Polylactic Acid/PBAT Compostable Blend
    • 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 859616
    Grade BG8800
    Material Type Polylactic Acid/PBAT Compostable Blend
    Processing Method Blow Molding
    Density 1.25 g/cm³
    Melt Flow Rate 2.0-4.0 g/10 min at 190°C/2.16 kg
    Melting Temperature 150-160 °C
    Tensile Strength 30-40 MPa
    Elongation At Break 200-400%
    Flexural Modulus 1000-1500 MPa
    Notched Izod Impact Strength 10-20 kJ/m²
    Vicat Softening Temperature 55-65 °C
    Heat Deflection Temperature 50-60 °C
    Biobased Content 30-50%
    Compostability Certification EN 13432, ASTM D6400
    Moisture Content <0.5%
    Appearance Opaque or off-white pellets

    As an accredited BG8800 Blow Molding Polylactic Acid/PBAT Compostable Blend factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing BG8800 is supplied in 25 kg moisture-barrier, foil-lined bags, palletized, UV-protected, and labeled with lot and safety information.
    Container Loading (20′ FCL) Container Loading (20′ FCL) for BG8800 Blow Molding PLA/PBAT Compostable Blend: palletized, moisture-protected bags, evenly distributed, secured, labeled, weight-optimized stowage.
    Shipping BG8800 Blow Molding Polylactic Acid/PBAT Compostable Blend ships as non-hazardous resin pellets in sealed moisture-barrier bags, 25 kg sacks, or bulk totes on pallets. Transport dry, below 50°C, away from sunlight, moisture, and contamination. No special placards required; standard industrial handling and PPE apply.
    Storage Store BG8800 in a cool, dry, well-ventilated warehouse in its original sealed packaging. Protect from moisture, direct sunlight, heat, and freezing. Recommended storage: below 30°C with low humidity. Keep away from strong oxidizers, acids, and bases. Avoid prolonged humid conditions to prevent hydrolysis. Rotate stock first-in, first-out, use within shelf life, and inspect packaging regularly.
    Shelf Life Shelf life is typically 12 months from manufacture when stored sealed, below 30°C, away from moisture, heat, and direct sunlight.
    Application of BG8800 Blow Molding Polylactic Acid/PBAT Compostable Blend

    Rigid Cosmetic Squeeze Tubes and Bottles for pH-Neutral Emulsions

    In high-speed personal-care packaging lines, BG8800 is processed on single-station shuttle extrusion blow molding machines equipped with 25:1 L/D barrier screws and accumulator heads configured with proportional hydraulic parison programming. Pre-drying at 65 °C for 4–6 h to a residual moisture content of ≤250 ppm is required before extrusion; processing from feed throat to metering zone is set at 175 °C, 182 °C, 186 °C, and 188 °C, while the head and die are maintained at 188–192 °C and the aluminum blow mold at 15–25 °C. At die-head set points above 195 °C, MFR drift over 20 min may exceed 20% and cause intermittent parison fold-back at the pinch-off; therefore residence time in the accumulator head is limited to <3 min. A formulation addition ratio of 1.0–2.5 wt% compostable color masterbatch and 0.2–0.5 wt% processing aid is metered into the throat; clean internal regrind from flash and tail pinch-off may be incorporated at 10–20 wt% only after the MFR under ISO 1133-1:2022 at 190 °C/2.16 kg has been confirmed within 0.5 g/10 min of virgin material, with the balance being virgin BG8800. Compliance for this application is established under EN 13432:2000/AC:2002 clauses 6.1 through 6.4, 94/62/EC Annex II heavy metal limits of ≤100 mg/kg summed for lead, cadmium, mercury, and hexavalent chromium, REACH Annex XVII restrictions for substances in articles, and Regulation (EC) No 1223/2009 Article 17 for finished cosmetic product safety assessment. Terminal finished products are 30–200 mL monolayer squeeze tubes and bottles intended for pH 5.0–7.0 emulsions, conditioners, body washes, and low-viscosity lotions; formulations containing more than 0.5 wt% d-limonene, benzyl alcohol, or low-molecular-weight esters are excluded because PBAT swelling and parison instability result in wall-thickness nonuniformity under ASTM D638-14 tensile evaluation.

    What Limits Alkaline Cleaner Packaging in PBAT-Rich Blow Molded Bottles?

    The primary process conflict in household cleaner packaging is not parison sag but stress-crack initiation caused by surfactant and alkaline exposure at bottle pinch-off weld lines. BG8800 is extrusion blow molded on long-stroke machines with 60 mm screw diameter and 65 mm accumulator head capacity, using blow air at 6–8 bar and mold temperature 10–20 °C, producing 500–1000 mL trigger-spray bottles at cycle times of 14–20 s. Published data for BG8800-specific rheology is limited; typical blow molding PLA/PBAT compounds show apparent viscosity in the range of 800–1,500 Pa·s at 190 °C and 100 s−1. A formulation addition ratio of 15–25 wt% in-house regrind is tolerated for non-food cleaner stock if regrind is ground through a 6 mm screen and dried to ≤250 ppm moisture; 0.5–1.0 wt% epoxy-functional chain extender is added to compensate for molecular weight loss in the recycled fraction, and 0.3 wt% erucamide slip is introduced to reduce closure thread abrasion, with the remainder of the blend being virgin BG8800. Compliance is anchored to REACH Annex XVII, CLP Regulation (EC) No 1272/2008 for finished article classification, 94/62/EC packaging heavy metal limits, and EN 13432:2000/AC:2002 for compostability. Terminal finished product types are monolayer trigger-spray bottles for pH 4.0–9.0 hard-surface cleaners containing nonionic and anionic surfactant systems below 10 wt% actives. Alkaline formulations with pH above 10.0 at 40 °C for more than 14 days induce hydrolytic degradation of the PLA phase; sodium hypochlorite above 5 wt% oxidizes both the PLA and PBAT phases; linear alkylbenzene sulfonate above 8 wt% produces environmental stress cracking at weld lines. Immersion testing per ASTM D543-21 followed by tensile testing per ASTM D638-14 is required for every new cleaner formulation before production release.

    In dry-food filling lines where closure torque and tiered stacking enforce a minimum top load of 180 N on 100–750 mL canisters, BG8800 is extrusion blow molded at a melt temperature of 178–184 °C with an adjustable die gap and oil-free compressed air at 6 bar. The downstream process uses a 22:1 L/D extruder with a melt pump and three-zone screw, and the blow mold is chilled to 18–22 °C to limit post-mold shrinkage below 0.8% in diameter. A formulation addition ratio of 0.5–1.5 wt% slip/antiblock masterbatch and 5–15 wt% regrind is accepted after organoleptic panel confirmation of no detectable odor or taste transfer under ISO 13302:2003 or an equivalent internal sensory protocol; the remainder of the formulation is virgin BG8800. Compliance for dry-food packaging is established under Regulation (EU) No 10/2011 overall migration limit of <10 mg/dm² and specific migration limits for lactic acid, 1,4-butanediol, terephthalic acid, and adipic acid; U.S. FDA food-contact status depends on existing FCNs for PLA and PBAT because no single 21 CFR section covers the compounded blend. Terminal finished products are monolayer canisters and wide-mouth jars for tea, spices, powdered beverages, breakfast cereals, and dry legumes. The operational boundary is oxygen and moisture ingress: published data for BG8800-specific oxygen transmission rate is limited, but PLA/PBAT blow molding compounds typically exhibit 1–2 orders of magnitude higher oxygen permeability than PET at 23 °C and 50% RH when measured under ASTM F1307-20; therefore, oxygen-sensitive or extended-shelf-life dry products are excluded unless a secondary metallized flow-wrap or liner compensates barrier performance.

    Where Fertiliser Fluid Packaging Stops Being Compatible with BG8800

    The use of BG8800 in agricultural and horticultural fluid packaging is confined to non-hazardous, water-based biostimulants, liquid humic substances, and diluted plant nutrient solutions. Extrusion blow molding equipment for this segment typically comprises a 25:1 L/D extruder with a compression ratio of 2.8:1 and a vertically opening blow mold maintained at 15–20 °C; containers from 500 mL to 2000 mL are produced with wall thickness bands of 0.6–1.2 mm. A formulation addition ratio of 0.5–1.0 wt% hindered amine light stabilizer masterbatch and 1.0 wt% iron oxide colorant is used for UV exposure mitigation; regrind from punching and deflashing is kept at 10–20 wt% and must be free of soil fines and mineral residues, with the remainder of the blend being virgin BG8800. Compliance for this segment is governed by Regulation (EU) 2019/1009 for fertilising products, REACH for chemical safety of the packaging article, 94/62/EC for packaging waste, and EN 13432:2000/AC:2002 for compostability claims. Terminal finished products are opaque or dark-tinted bottles and canisters for liquid seaweed extracts, amino acid biostimulants, and chelated micronutrient solutions with pH between 5.0 and 8.0. Petroleum-solvent-based adjuvants, xylene-based emulsifiable concentrates, and registered pesticide formulations are outside the operational boundary because PBAT absorbs low-polarity solvents and because UN transport certification for hazardous liquids imposes permeation and closure requirements that monolayer PLA/PBAT blow molded containers do not routinely satisfy under ASTM D543-21 immersion protocols. High-salinity liquid fertilizers above 15 wt% dissolved salts also accelerate environmental stress cracking at the pinch-off zone and are excluded unless a compatibility study demonstrates weld-line retention of at least 80% tensile elongation after 30 days at 40 °C.

    Regrind loops in BG8800 extrusion blow molding are generally limited by the rate of molecular weight loss after repeated thermal and shear cycles and by low thermal conductivity, which shifts parison sag behavior before visible granules appear in the extrudate. The downstream production process converts flash, tail pinch-off, and start-up purge from a 25:1 L/D blow molding extruder into regrind through a 6 mm screen; the ground material is dried at 65 °C for 4 h to ≤250 ppm moisture and reintroduced at 20–30 wt% with 0.3 wt% processing aid and 1.0–2.0 wt% chain extender masterbatch to maintain parison melt strength. Published data for BG8800-specific regrind loop performance is limited; therefore MFR is measured under ISO 1133-1:2022 at 190 °C/2.16 kg before each lot release, and regrind fractions are reduced if MFR increases by more than 15% relative to virgin material. Compliance is established under 94/62/EC Annex II heavy metal limits, REACH, and EN 13432:2000/AC:2002 because the terminal finished products are non-food wide-mouth jars for bath salts, dry shampoo, powdered laundry concentrates, dentifrice tablet containers, and solid personal care formulations. The process window for these articles is set at a melt temperature of 176–182 °C, mold temperature of 18 °C, and cycle time of 12–16 s for 100–500 mL containers. Regrind exceeding 30 wt% is not recommended for blow molded articles with wall thickness below 0.6 mm because viscosity loss produces nonuniform parison stretching and audible stress release at the weld line during top-load testing under ASTM D2659-16.

    When a 200 mL Travel Bottle Must Pass EN 13432 and 94/62/EC Simultaneously

    The requirement to pass EN 13432:2000/AC:2002 compostability testing and 94/62/EC Annex II heavy metal thresholds simultaneously becomes process-critical for thin-wall travel bottles because wall-thickness reductions below 0.5 mm amplify parison sag and die-lip build-up. BG8800 is processed on a dual-station continuous extrusion blow molder with 45 mm screw diameter, 60 mm accumulator head capacity, and dual-cavity tools producing 200 mL travel bottles at 8–12 g article weight and 8–10 s cycle time. A formulation addition ratio of 1.0–2.0 wt% compostable color masterbatch, 0.2 wt% slip additive, and 10–15 wt% clean regrind is metered at the throat, with the balance being virgin BG8800; if the bottle is to receive a paper label, flame surface treatment is applied to reach 40–46 dyn/cm wetting tension measured under ASTM D2578. Compliance for the finished article includes REACH registration documentation for polymers, 94/62/EC concentration limits for heavy metals, and EN 13432 disintegration, biodegradation, and ecotoxicity criteria; if compostability claims cover multiple jurisdictions, parallel certification to ISO 17088:2021 is documented. Terminal finished products are thin-wall travel bottles and promotional sample bottles for hotel amenity liquids, bath salts, and dry cosmetic mineral powders. The operational limitation is structural rigidity: at 0.45–0.55 mm wall thickness, top-load resistance measured under ASTM D2659-16 declines below 120 N when regrind fraction exceeds 20 wt%; therefore high-bay warehousing of filled bottles requires partition cartons or intermediate stacking trays to prevent partial collapse at pallet height above 1.2 m.

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    Certification & Compliance
    More Introduction

    BG8800 is a fully formulated thermoplastic blend of polylactic acid and poly(butylene adipate-co-terephthalate), supplied as cylindrical pellets for continuous extrusion blow molding. The grade is positioned as a compostable alternative to polyolefins in semi-rigid containers where unmodified PLA lacks sufficient parison melt strength and unmodified PBAT lacks adequate modulus. The melt is compounded on a co-rotating twin-screw extruder with a 44:1 L/D ratio, using starve-fed solids, liquid injection of a migratory compatibilizer, and vacuum devolatilization at −0.08 MPa. Residual moisture after drying is targeted below 0.025 % before discharge. The product is not a monolayer film grade and is not designed for injection stretch blow molding.

    Nominal Property Slate and Test Designations

    Nominal physical and mechanical properties of BG8800 from the supplier technical data sheet
    PropertyTest methodValue
    Melt mass-flow rateISO 1133-1:2022 (190 °C, 2.16 kg)3–5 g/10 min
    DensityISO 1183-1:20191.23 g/cm³
    Tensile strength at yieldISO 527-2:201227–31 MPa
    Tensile elongation at breakISO 527-2:2012250–320 %
    Flexural modulusISO 178:2019900–1,100 MPa
    Notched Izod impact strengthISO 180:2019 (23 °C)18–24 kJ/m²
    Vicat softening temperature A50ISO 306:201360–64 °C
    Recommended residual moisture after dryinginternal desiccant-drying specification≤250 ppm

    These values are obtained from injection-molded test specimens; blow molded part properties are governed by draw ratio, wall thickness, and weld-line geometry. The tensile elongation values should not be applied to thin-wall blow molded containers without molding trials. Mechanical properties may also be reported using ASTM D638-14 and ASTM D256-10 when North American customers require direct comparison.

    How Does BG8800 Differ from Unmodified PLA and PBAT Homopolymers?

    Polylactic acid homopolymer typically demonstrates tensile elongation below 10 % and notched Izod impact below 5 kJ/m², while PBAT homopolymer can exhibit elongation above 500 % but has a flexural modulus below 100 MPa. BG8800 is formulated so that the PBAT-rich continuous phase provides toughness and the PLA-rich dispersed phase contributes stiffness. The reactive compatibilizer reduces the interfacial tension between the two phases; scanning electron micrographs of cryo-fractured extrudate show PLA domains of 0.5–2 µm in a PBAT matrix. This morphology is retained through the parison blow step when the melt temperature remains below 175 °C.

    Comparative property profile of PLA homopolymer, PBAT homopolymer, and BG8800
    ParameterPLA homopolymerPBAT homopolymerBG8800
    Melt mass-flow rate (190 °C, 2.16 kg)5–12 g/10 min4–8 g/10 min3–5 g/10 min
    Tensile elongation at break4–8 %500–700 %250–320 %
    Flexural modulus3,000 MPa70–100 MPa900–1,100 MPa
    Notched Izod impact strength3–5 kJ/m²no break18–24 kJ/m²
    Parison sag resistance at 170 °Clowvery lowcontrolled
    Industrial compostabilitycertifiedcertifiedcertified

    Compared with general-purpose PLA/PBAT injection molding grades, BG8800 exhibits a lower melt-flow index and higher low-shear viscosity; this is the primary rheological distinction that allows continuous parison hang times of 5–8 s at 170 °C without the addition of high-load nucleating fillers.

    When Melt Temperature Exceeds 178 °C in Continuous Parison Formation

    Predrying is mandatory irrespective of packaging condition. A desiccant dryer at 60 °C for 4 h with a dew point of −40 °C is recommended; the target after drying is ≤250 ppm moisture. Residual moisture above 300 ppm hydrolyzes PLA during plastication, reducing molecular weight and melt tension without necessarily producing visible splay. The melt temperature at the die should be held between 160 °C and 175 °C. At 178 °C and above, the PBAT-rich continuous phase loses viscosity rapidly; parison draw-down increases and top-load variation in a 1.2 L container exceeds ±0.1 mm. Below 155 °C, PLA domains remain partially unmelted, generating die-exit roughness and weak pinch-off weld lines.

    The recommended screw is a low-shear three-zone design with a compression ratio of 2.5:1 to 3.0:1 and L/D of 25:1 to 30:1. High-shear mixing sections should be avoided because they generate localized melt temperatures above the degradation threshold even when the average melt temperature is within range. Die swell is 12–18 % at 170 °C and 60 s⁻¹; the die gap is typically increased by 15 % relative to a similar HDPE container. Melt strength measured by a Rheotens apparatus is 0.08–0.12 N at 170 °C, approximately 3–5 times unmodified PLA. Molecular-weight retention during compounding is monitored by capillary rheometry. A drop in melt viscosity greater than 10 % at 170 °C and 100 s⁻¹ indicates hydrolysis or thermal degradation and requires dryer and barrel-temperature audit. Long-chain branch formation from excess reactive compatibilizer produces gel particles visible as pinholes in thin bottle walls; the compatibilizer level is therefore controlled to 0.3–0.5 wt%.

    Pinch-off weld line integrity is the critical failure mode in extrusion blow molding with BG8800. Mold temperature at the pinch-off should be maintained at 20–35 °C; below 15 °C, rapid solidification prevents sufficient interfacial diffusion and produces V-notch cracking under drop impact. Blow pressure of 0.6–0.9 MPa and blow time of 8–12 s are used for containers of 500 mL to 2 L. In a production trial on a shuttle blow molder with a 70 mm extruder and 24:1 L/D, a 1.2 L cylindrical container with 0.8 mm nominal wall thickness passed ASTM D2463-15 impact testing from 1.2 m at 23 °C after conditioning at 50 % relative humidity for 48 h.

    Where Is BG8800 Applied Across Blow Molded Rigid and Semi-Rigid Packaging?

    The grade is used for extrusion blow molding of small-to-medium containers: dry cosmetic jars, personal care bottles, home-care dosing containers, and agricultural formulation bottles. It is not suitable for carbonated beverage containers; published data for this specific configuration is limited, and the oxygen and carbon dioxide permeation properties are not comparable to PET or HDPE barrier structures. Typical wall thickness ranges from 0.4 mm to 1.5 mm; containers above 2 L require parison programming or accumulator head tooling because melt strength limits unsupported parison length. Continuous hot-fill exposure above 45 °C is outside the recommended service envelope due to Vicat softening and creep. Wall thickness distribution is controlled by parison programming; the programming curve is set with a 15 % initial die-gap reduction at the bottom weld line and 20 % increase at the top flash area.

    Industrial Compostability, Food-Contact Readiness, and Boundary Conditions

    Certified grades of BG8800 are designed to meet the disintegration and biodegradation criteria of EN 13432:2000 and ASTM D6400-21. Biodegradation is evaluated by ISO 14855-1:2012 under controlled composting conditions at 58 °C; the pass threshold is 90 % conversion to carbon dioxide within 180 days relative to a positive reference. Disintegration requires 90 % of the test material to pass through a 2 mm sieve within 12 weeks. Heavy metal limits and ecotoxicity testing follow EN 13432:2000 Annex E and ASTM D6400-21 requirements. For electrical/electronic accessories, the blend is formulated without intentionally added lead, cadmium, mercury, or hexavalent chromium; compliance with RoHS Directive 2011/65/EU Annex II is based on supplier declarations. REACH SVHC declaration for the grade is available from the manufacturer; no SVHC above 0.1 % w/w is intentionally present.

    These certifications apply to industrial composting facilities only. Home compost, marine, freshwater, and anaerobic digestion environments do not provide the same temperature and microbial density and are outside the certified boundary unless the final article carries a separate certification. Food-contact compliance must be established on the finished article under the intended food type and temperature; the pellet itself is not a food-contact certification. In the United States, individual components may be listed under applicable FDA 21 CFR sections, but migration testing is required.

    Blow molding purging and shutdown are performed with low-MFI LDPE because BG8800 adheres to metal surfaces when held above 175 °C for more than 15 min. The machine should not be idled with material in the barrel; after shutdown, the screw and die should be purged until the melt stream is clear and then cooled under nitrogen. Reclaimed flash from the same day can be reprocessed at up to 25 wt% if ground and dried; post-industrial regrind above this level reduces parison melt strength and increases gel formation. Un-dried regrind is a frequent cause of intermittent parison breaks on startup.

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