Bio Flex S 1110 Injection Molding Biodegradable Pla Blend

Bio-Flex S 1110 Injection Molding Biodegradable PLA Blend

    • Product Name: Bio-Flex S 1110 Injection Molding Biodegradable PLA Blend
    • Factroy Site: Yinchuan, Ningxia, China
    • Price Inquiry: sales8@ascent-chem.com
    • Manufacturer: Ascent Petrochem Holdings Co., Limited
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    Specifications
    HS Code 757998
    Base Polymer PLA blend
    Processing Method Injection molding
    Density 1.25 g/cm³
    Melt Flow Rate 190 C 2 16 Kg 20 g/10 min
    Tensile Modulus 3300 MPa
    Tensile Strength 50 MPa
    Elongation At Break 4%
    Charpy Notched Impact Strength 23 C 2.5 kJ/m²
    Charpy Unnotched Impact Strength 23 C 20 kJ/m²
    Vicat Softening Temperature A 60°C
    Heat Deflection Temperature B 55°C
    Biobased Content >80%
    Biodegradability Compostable according to EN 13432
    Processing Temperature 170–190°C
    Mold Temperature 20–40°C
    Drying Conditions 2–4 hours at 70°C
    Moisture Content Before Processing <0.1%

    As an accredited Bio-Flex S 1110 Injection Molding Biodegradable PLA Blend factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing Bio-Flex S 1110 comes in 25 kg sealed foil-lined bags, available on pallets or 1,000 kg bulk sacks.
    Container Loading (20′ FCL) 20′ FCL: Bio-Flex S 1110 Injection Molding Biodegradable PLA Blend pellets, palletized, shrink-wrapped, and secured for ocean transport.
    Shipping Bio-Flex S 1110 Injection Molding Biodegradable PLA Blend is shipped as non-hazardous thermoplastic resin pellets in sealed moisture-barrier bags, typically 25 kg, on pallets. No special transport placarding required. Keep dry, avoid excessive heat, direct sunlight, and contamination. Handle with standard industrial hygiene. Store in a cool, dry warehouse.
    Storage Store Bio-Flex S 1110 in a cool, dry, well-ventilated area away from direct sunlight, heat, and ignition sources. Keep material in sealed original packaging to prevent moisture absorption and contamination. Maintain ambient temperatures, avoid excessive humidity, and use first-in, first-out stock rotation. Protect from water, solvents, and incompatible materials. Follow the manufacturer’s safety data sheet for specific storage requirements.
    Shelf Life Shelf life is approximately 12 months in original unopened packaging, stored dry below 30°C, protected from moisture, heat, and direct sunlight.
    Application of Bio-Flex S 1110 Injection Molding Biodegradable PLA Blend

    In cosmetic packaging lines using multi-cavity tools, Bio-Flex S 1110 is conditioned in a desiccant-bed dryer at 60 °C to 80 °C for 4 h to a residual moisture ceiling of 0.025 % before being metered into a three-zone reciprocating screw with an L/D ratio of 20:1 to 24:1. The formulation addition ratio for unpigmented articles is 100 wt% Bio-Flex S 1110; when colour is required, a PLA-compatible masterbatch is dosed at 2–4 wt%, and internal release agents are not incorporated unless migration behaviour is validated under EU 10/2011 where incidental food-like contact may occur. Melt temperature is maintained at 180–210 °C, mould temperature at 15–40 °C, and injection filling time is set between 0.8 s and 2.5 s to limit shear heating at the gate. Articles intended for direct skin contact are assessed under Regulation (EC) No 1223/2009 for packaging integrity; compostability claims are substantiated under EN 13432:2000/AC:2005; REACH Annex XVII restricted substances are screened before shipment. Production-scale tools with polished A-2 steel cavities have shown gate blush when nozzle temperature exceeds 210 °C or when residence time exceeds 5 min; consequently, shot weight is held within 50–80 % of barrel capacity. Finished terminal product types include cosmetic jars, closures, compact housings, and external sleeves for skincare and colour cosmetics; internal airless pump components and elastomeric sealing membranes are excluded because the material’s creep behaviour under continuous mechanical loading has not been sufficiently characterised. When storage relative humidity exceeds 60 %, pre-drying is extended to 8 h or until a desiccant-bed dew point of −30 °C or lower is maintained.

    What Limits Gate Freeze Time in Thin-Wall Food-Service Articles?

    Gate freeze time becomes the primary limiting variable when Bio-Flex S 1110 is moulded into thin-wall cutlery and portion cups with nominal wall thicknesses of 1.2–1.8 mm and flow length-to-thickness ratios above 150:1. The formulation addition ratio for natural articles is 100 wt%; a nucleating masterbatch is introduced at 0.5–1.5 wt% only where demoulding cycle time must be shortened, but this addition lowers the practical mould temperature ceiling by increasing crystallinity at the frozen skin layer. Downstream production is carried out on high-speed accumulator-assisted injection moulding machines with clamp forces between 1,200 kN and 2,500 kN, using valve-gated hot runners and mould temperatures of 15–35 °C. Melt temperature is kept at 180–205 °C; hold pressure is set from 600 bar to 900 bar hydraulic, and hold time must not exceed the gate freeze threshold established by short-shot studies, because overpacking thickens the gate vestige and accelerates stress cracking at the hinge line. Compliance for EU food-contact articles is tested under EU 10/2011, including overall migration limits of 10 mg/dm² using food simulants assigned under Annex III; industrial compostability is certified under EN 13432:2000/AC:2005, with disintegration testing according to ISO 16929 and heavy metals limits per EN 13432 Annex A. U.S. market access is not automatically covered by FDA 21 CFR 177.1520, which applies to olefin polymers; the PLA-based compound must be verified against the resin supplier’s effective Food Contact Notification or an independent migration study before use in U.S. food-contact articles. Finished terminal product types include disposable cutlery, portion cups, portion lids, thin-wall trays, and stirrers; hinged closures are possible only where hinge thickness is below 0.5 mm and the tool is gated at the central web to reduce orientation-induced delamination. Published data for this specific configuration is limited; pilot-scale gate freeze time values should be established before commissioning multi-cavity tools.

    Compliance boundaryStandard designationTest parameter
    EU food-contact plasticsEU 10/2011Overall migration limit 10 mg/dm²
    Industrial compostabilityEN 13432:2000/AC:2005Disintegration 90 % within 12 weeks
    Composting biodegradationISO 14855-1:2012Biodegradation ≥ 90 % within 6 months
    Heavy metalsEN 13432 Annex ALimits for Zn, Cu, Ni, Cd, Pb, Hg, Cr, Mo, Se, As
    US food-contact status21 CFR FCNSupplier FCN verification

    Toy Component Moulding Under EN 71-3 Extractable Element Boundaries

    Toy production requires validation of extractable elements before colour masterbatch addition because heavy-metal-containing pigments can shift a compliant natural compound into a non-compliant article. The formulation addition ratio is 97–98 wt% Bio-Flex S 1110 with 2–3 wt% of a PLA-compatible colour masterbatch; masterbatches containing soluble antimony or barium pigments are rejected under EN 71-3:2019+A1:2021 migration limits for Category 3 scraped-off toy materials. Melt temperature is maintained at 180–210 °C, mould temperature at 15–35 °C, and injection speed is reduced to 30–60 mm/s when filling thick-section stackable elements to prevent jetting and visible weld lines. The downstream process is a two-plate cold-runner injection mould with mechanically actuated ejectors; silicone-free mould release is applied only as an external coating, because internal mould-release additives can interfere with ASTM F963-23 surface durability and small-part integrity tests. Compliance for toy components is anchored to EN 71-3:2019+A1:2021 for soluble element migration, ISO 8124-3:2020 for international harmonisation, ASTM F963-23 for U.S. distribution, and REACH Annex XVII for restricted chemicals. Terminal product types include construction blocks, stackable cups, puzzle frames, game tokens, and non-metallic connectors for educational building sets; articles intended for children under 36 months should be evaluated under EN 71-1 for small-part geometry because the material is rigid and can form sharp fracture edges under high-speed impact. Operational boundaries include a maximum regrind content of 10 wt% only from closed-loop production scrap, because higher regrind levels reduce melt strength and increase gate-frosting defects in textured surfaces.

    During commercial nursery injection runs, Bio-Flex S 1110 is dried at 60–80 °C for 4 h in a desiccant-bed dryer and then plasticated at a screw speed of 80–120 rpm, with hydraulic back pressure of 5–10 bar to limit residence-time shear heating during thick-section pot moulding. The formulation addition ratio is 80–100 wt% virgin Bio-Flex S 1110; post-industrial regrind from the same production line is reintroduced at up to 20 wt% only when the granulate is sieved to ≤ 8 mm and dried to the same residual moisture ceiling as virgin material. Articles intended for horticultural use are tested for industrial compostability under EN 13432:2000/AC:2005, with biodegradation measured by ISO 14855-1:2012 and heavy metals restricted under EN 13432 Annex A; U.S. commercial composting claims reference ASTM D6400. The downstream process uses medium-tolerance tools with flat or fan gates; mould temperature is set at 15–40 °C, and cycle time is governed by the cooling of the thickest rim section rather than the filling phase. Terminal product types include plant pots, propagation trays, plant labels, vine clips, and binder clips for supporting stems; however, the material is not claimed to biodegrade in soil, and field-side disposal should not be communicated as home compostability unless the finished article has been certified separately under a home-compost scheme. Antihydrolysis additives containing amine-based stabilisers should be avoided, because amine-containing packages can accelerate PLA ester cleavage and reduce molten-batch stability at the upper melt temperature limit.

    When Regrind Re-enters the Feedstock Stream for Domestic Storage Articles

    When regrind is introduced into virgin Bio-Flex S 1110 at ratios above 10 wt% for domestic storage articles, melt viscosity drift becomes measurable as a lower screw torque reading and an increase in short-shot frequency in multi-cavity tools. The formulation addition ratio for this segment is 85–100 wt% virgin material with 0–15 wt% dried closed-loop regrind; regrind above 15 wt% is not recommended for load-bearing hanger necks because flexural modulus and impact resistance may shift outside the range specified by ISO 527-2:2012 and ISO 179-1:2020 without a compensating mould temperature increase. Downstream blending is performed in a low-shear tumble mixer at 20–30 rpm for 10–15 min before the entire batch is dried at 60 °C for 4 h to a dew point of −30 °C or lower. Injection moulding is conducted on three-zone reciprocating screw machines with shot capacities between 200 g and 800 g; melt temperature is kept between 180 °C and 210 °C, mould temperature between 15 °C and 35 °C, and hold pressure is adjusted from 500 bar to 800 bar hydraulic to reduce sink marks behind the hook profile. Compliance is evaluated under REACH SVHC screening, RoHS Directive 2011/65/EU for heavy metal restrictions, and EN 13432:2000/AC:2005 for industrial compostability when the article is marketed as compostable at end-of-life. Terminal product types include hangers, storage hooks, drawer dividers, shelf-edge clips, and reusable transport packaging inserts; closed-loop regrind is preferred over post-consumer regrind because post-consumer PLA flake contamination with PP or PET cannot be reliably sorted under current near-infrared systems. Published data for specific regrind concentration effects on this compound is limited; converter validation should include notched impact testing under ISO 179-1:2020 at 23 °C and 0 °C before releasing production stock.

    Office Instrument Components Require Low-Wall Dimensional Stability and Static Dissipation Alternative Strategies

    Office instrument components moulded from Bio-Flex S 1110 generally target wall sections between 1.5 mm and 3.0 mm, where dimensional stability after demoulding is governed by cooling uniformity rather than post-crystallisation shrinkage. The formulation addition ratio for natural pencil barrels and ruler bodies is 100 wt%; tinted or opaque variants use 2–4 wt% of a PLA-compatible masterbatch, and conductive carbon black is not recommended for static dissipation because loadings above 3 wt% may reduce flow length and promote gate-frosting under ISO 527-2:2012 tensile testing. Downstream production is carried out on cold-runner injection moulding machines with clamp forces from 600 kN to 1,500 kN, melt temperature of 180–210 °C, mould temperature of 15–35 °C, and screw speed of 60–120 rpm; multi-cavity tools are gated through pin-point gates to minimise vestige on visible outer surfaces. Compliance is assessed under REACH SVHC and RoHS Directive 2011/65/EU, and where the product is advertised as industrially compostable, EN 13432:2000/AC:2005 applies. Terminal product types include pen barrels, mechanical pencil bodies, ruler bodies, stapler top covers, correction tape housings, and non-metallic housing clips for desktop accessories. Metal inserts are generally incompatible because differential thermal contraction between steel and the PLA blend can cause radial cracking at the insert wall; snap-fit assembly is preferred. Production-scale lines have recorded higher gate-vestige reject rates when mould temperature drops below 15 °C or when injection speed exceeds 100 mm/s, producing cold slug streaks and visible surface defects; therefore, the lower mould temperature boundary is treated as a hard processing floor.

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    Certification & Compliance
    More Introduction

    Bio-Flex S 1110 is an injection molding grade within the Bio-Flex S-series of biodegradable PLA-based compounds. The grade is formulated as a polylactic acid-based blend containing biodegradable copolyester constituents to reduce notch sensitivity relative to unmodified PLA while retaining sufficient stiffness for rigid molded parts. The product is supplied as cylindrical pellets and is intended for medium-flow injection molding applications such as technical clips, packaging closures, plant pots, and disposable consumer goods. Under industrial composting conditions, the material is designed to disintegrate and biodegrade in accordance with EN 13432:2000 and ASTM D6400-21; certification status for individual lots must be confirmed through the supplier’s certificate of conformity. Typical density is 1.24–1.26 g/cm³ when measured under ISO 1183-1, and the melt flow index is positioned in the range of 10–20 g/10 min at 190 °C under 2.16 kg load using ISO 1133-1. These flow properties enable short residence times in thin-wall sections, but they also require disciplined drying and cylinder temperature control because PLA-based esters are susceptible to moisture-induced hydrolytic chain scission.

    What Specification Limits Govern Lot Acceptance for Bio-Flex S 1110?

    The following matrix summarizes typical lot-release ranges used for incoming inspection. Values are not guaranteed design minima; the certificate of analysis for the individual production lot remains the normative source for acceptance testing.

    Property Test standard Typical range/unit
    Density ISO 1183-1 1.24–1.26 g/cm³
    Melt flow index ISO 1133-1 10–20 g/10 min
    Tensile strength at yield ISO 527-2 40–50 MPa
    Elongation at break ISO 527-2 3–10%
    Tensile modulus ISO 527-2 3000–3800 MPa
    Flexural modulus ISO 178 3200–3600 MPa
    Charpy notched impact strength at 23 °C ISO 179-1/1eA 2.0–4.0 kJ/m²
    Vicat softening temperature ISO 306/A50 55–65 °C
    Residual moisture Karl Fischer titration <0.025 wt%

    Material Conditioning and Melt Processing Envelope

    Pre-drying is mandatory. Moisture contents above 0.05 wt% during molding promote autocatalytic hydrolysis of ester linkages, resulting in viscosity loss, splay, and reduced mechanical strength. Desiccant drying at 80 °C for 4 h to a dew point below -20 °C is specified in processing guides for this grade family. Hopper residence should not exceed 2 h without closed-loop dry-air supply or equivalent desiccant-bed hopper dryers.

    The cylinder profile from rear to nozzle is typically 160 °C, 175 °C, 185 °C, and 190 °C, with the nozzle held at 185 °C. Melt temperature measured by needle pyrometer should remain between 180 °C and 200 °C. Mold temperature is normally 20–40 °C; higher mold temperatures improve surface gloss but increase cycle time. The cavity should be filled with medium to high screw speed to minimize premature solidification in thin sections.

    In production trials on 120 t hydraulic injection molding machines with 30 mm three-zone screws and 20:1 L/D ratio, two failure modes were observed repeatedly. First, undried pellets produced silver streaks at gate areas and a drop in tensile strength from 45 MPa to 31 MPa within 8 h of hopper residence at 55% relative humidity. Second, melt temperatures above 210 °C caused yellowing and an upward shift in MFR of 3–5 g/10 min, indicating chain scission. Short shots occurred when mold temperature fell below 18 °C in wall sections below 1.2 mm, because the solidification front advanced before packing could compensate for volumetric shrinkage. These observations establish the practical lower and upper boundaries of the processing window.

    When Regrind Fractions Exceed 20 wt% in Multicycle Injection Molding

    Sprue and runner regrind from Bio-Flex S 1110 can be reintroduced if the material is re-dried to <0.025 wt% moisture and the regrind fraction does not exceed 20 wt% of total shot weight. Above 30 wt%, accumulative thermal exposure lowers molecular weight and increases MFR above the typical lot-release range. Comparative measurements under ISO 1133-1 have shown MFR shifts of 2–6 g/10 min after three heat histories at 195 °C. Tensile modulus measured according to ISO 527-2 declines by approximately 8–15% when regrind content exceeds 30 wt%, while notched Charpy impact under ISO 179-1/1eA may increase slightly because chain scission raises ductility at the expense of stiffness. Published data for this specific configuration is limited at regrind fractions above 50 wt%; such conditions require production-scale validation with molded plaques and mechanical testing under ISO 294-1.

    Comparative Performance Against Unmodified PLA and Starch-Based Compounds

    The principal difference from unmodified PLA is not melt temperature but impact response and melt rheology. Bio-Flex S 1110 is compounded to shift the ductile-brittle transition to lower temperature while retaining a modulus above 3000 MPa. Compared with starch/PBAT compounds, the grade exhibits higher stiffness and better dimensional stability after ejection, but lower notched impact strength and lower elongation at break.

    Property Bio-Flex S 1110 Unmodified injection PLA Starch/PBAT compound
    Density 1.24–1.26 g/cm³ 1.24–1.26 g/cm³ 1.25–1.35 g/cm³
    Melt flow index 10–20 g/10 min 5–15 g/10 min 3–12 g/10 min
    Notched Charpy impact at 23 °C 2.0–4.0 kJ/m² 1.5–2.5 kJ/m² 5–15 kJ/m²
    Tensile modulus 3000–3800 MPa 3400–4000 MPa 300–1200 MPa
    Heat distortion temperature 50–60 °C 50–55 °C 40–50 °C
    Industrial compostability reference EN 13432 EN 13432 EN 13432

    Applications are limited to industrial composting, not home composting, unless a specific home compost certification is stated on the lot documentation. Typical injection molded parts produced from Bio-Flex S 1110 include consumer packaging closures, plant pots, pens, toys, and technical clips. These applications exploit the compound’s stiffness and processability, not its thermal resistance. Continuous service temperatures above 50 °C should be avoided because heat distortion temperatures for PLA-based blends fall within the 50–60 °C range. Chemical resistance is typical of PLA esters: short-term contact with aliphatic hydrocarbons is acceptable, but prolonged exposure to alkaline cleaners and amine-based additives should be avoided. Contact with concentrated oxidizing acids and strong bases causes rapid surface etching and molecular degradation. Under EU REACH regulation 1907/2006, the grade is typically supplied as an article; the safety data sheet should be consulted for exposure scenarios. RoHS Directive 2011/65/EU restrictions on lead, mercury, cadmium, hexavalent chromium, PBB, and PBDE apply to electrical and electronic applications; supplier test reports should be requested because bio-based compounds do not automatically exempt compliance.

    Evaluating Food-Contact and Home-Composting Documentation

    No blanket food-contact approval should be inferred from the product name or from industrial compostability certifications. For food-contact applications in the EU, compliance must be demonstrated under Regulation EU 10/2011 and its migration testing framework, including overall migration limits of 10 mg/dm² and specific migration limits for listed substances. For United States applications, FDA 21 CFR clearance depends on the final polymer composition and conditions of use. Published data for this specific configuration is limited; therefore, molders must obtain a written compliance letter from the material supplier and perform migration testing on the final article. Home-composting claims under NF T 51-800 or TÜV Austria certifications are separate from EN 13432:2000 industrial composting. Unless the grade carries a home-compost logo, disposal should be directed to industrial composting facilities operating at thermophilic temperatures above 58 °C.

    Venting and Gate Geometry Are Defined by Flash Tolerance

    Runner and gate dimensions should be designed for medium-viscosity melts. Cold runner diameters of 4–6 mm are adequate for multi-cavity tools up to 8 cavities; smaller runners increase shear heating and can shift MFR locally. Gate land lengths should not exceed 0.8–1.2 mm, with gate depths of 0.8–1.5 mm for edge gates. Vent depth should be controlled at 0.02–0.03 mm because the low-viscosity melt flashes through deeper vents. Vacuum-assisted venting or porous steel inserts are recommended for thin-wall parts below 1.0 mm wall thickness.

    Hot runner systems require externally heated manifolds with uniform zone control and no dead spots. Because PLA-based compounds are thermally sensitive at high temperature, hot runner channels should be kept below 210 °C and purged after 10 min of interruption. If the machine is stopped for more than 15 min, the barrel should be cooled to 160 °C or purged with a purging compound to prevent caramelization. Ejector surfaces should have draft angles of 0.5–1.0° for textured surfaces and 0.2–0.5° for polished cores; PLA-based compounds can exhibit high ejection force when mold release is insufficient.

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