| Код ТН ВЭД | 191481 |
Как аккредитованная фабрика Bio-Flex FX 1821 Opaque Low Gauge Blown Film PLA Blend, мы соблюдаем строгие протоколы качества - каждая партия подвергается строгим испытаниям для обеспечения последовательных стандартов эффективности и безопасности.
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In organic waste collection liners produced from Bio-Flex FX 1821 Opaque Low Gauge Blown Film PLA Blend, the decisive conversion variable is not film clarity but retention of melt strength at gauge reductions below 20 µm, because caddy liners must withstand wet food residues, coffee grounds, and bone fragments without puncture failure at the bag-to-caddy stress point. Industry compliance for this downstream segment is governed by EN 13432:2000/AC:2005 and ASTM D6400-23, with ultimate aerobic biodegradation tested under ISO 14855-1:2012 at 58±2 °C and compost disintegration verified in 12 weeks according to Clause 4.3.1 of EN 13432; heavy metal limits are also bound by 94/62/EC Annex II, with a combined limit of 100 mg/kg for lead, cadmium, mercury, and hexavalent chromium. The formulation addition ratio for a monolayer caddy liner is 100 wt% FX 1821 pellet when produced on a stable bubble, whereas converters requiring higher dart impact blend 85–90 wt% FX 1821 with 10–15 wt% of a PBAT-rich copolyester masterbatch; post-industrial FX 1821 regrind may be added up to 15 wt% only after moisture and melt flow rate re-qualification to ISO 1133-1:2022. Downstream production occurs on a three-layer blown film line using a 50 mm single-screw extruder with L/D 30 and a barrier screw, a spiral mandrel die with 0.8 mm die gap, a blow-up ratio of 2.5–3.0, and a frost line height of 600–800 mm; melt temperatures are held between 160–180 °C at the extruder and 170–185 °C at the die, while pre-drying in a desiccant dryer at 70 °C for 4 h to 0.10 wt% moisture is mandatory when ambient relative humidity exceeds 60%; gauge variation in the thin section below 15 µm is controlled by maintaining melt-pressure fluctuation under ±1.5 MPa. Terminal finished product types include 10–20 L kitchen caddy liners with side gussets, 30 L municipal organic waste bags, and institutional compostable bin liners for food-service back-of-house collection. The operational boundary is that FX 1821 caddy liners should not be stored in humid kitchens for more than 12 months without sealed moisture-barrier packaging, because absorbed moisture above 0.25 wt% initiates hydrolytic degradation and lowers heat-seal strength.
High-speed carrier-bag conversion of FX 1821 slit films prioritizes transverse-direction tear retention rather than dart impact, because side-gusset creases and heat-seal edges concentrate stress in the TD orientation during loading. Compliance for this segment rests on the same compostability certification framework—EN 13432:2000/AC:2005 and ASTM D6400-23—but the converter additionally verifies heavy metal content under 94/62/EC Annex II at ≤100 mg/kg total and, where the bag enters retail as a shopping aid, dimensional tolerance under ISO 4593:2019. The formulation addition ratio of FX 1821 can be 95–100 wt% with 0–5 wt% white masterbatch for batch-to-batch opacity control; if the converter requires lower seal initiation on high-speed rotary bag machines, a coextruded sealant layer comprising 80 wt% FX 1821 and 20 wt% PBAT is added at 10–15% of total film thickness, bringing seal bar temperature from 125 °C to 105–115 °C. Downstream production uses a monolayer or two-layer blown film line with die gap 1.0 mm, BUR 3.0–4.0, and melt temperature 160–180 °C; the film is post-gusseted, slit to 300–600 mm widths, printed with water-based flexographic inks, and converted on bottom-seal or side-seal machines at 150–200 bags/min, with heat-seal dwell 0.3–0.6 s and jaw pressure 0.4–0.6 MPa. Finished product types include opaque vest carrier bags in 25–40 µm gauge, boutique shopping bags with central fold and hem, and short-contact produce bags for loose vegetables. The operational boundary is that this FX 1821 film is not a drop-for-drop LDPE substitute for loads above 12 kg; the notched tear mechanism shifts from yielding to crack propagation when film gauge exceeds 50 µm or when the BUR falls below 2.5, making low-BUR tubing prone to handle pull-out.
For soil-biodegradable mulch film, the central conflict in FX 1821 is the need to maintain a 12–18 µm gauge over a 3–6 month crop season while still achieving fragmentation and mineralization after soil incorporation under EN 17033:2018. This standard requires aerobic biodegradation in soil at 25±3 °C according to ISO 17556:2019, with 90% mineralization in a maximum 24 months, and no negative impact on plant germination in the ecotoxicity test of OECD 208. The formulation addition ratio for machine-laid mulch film is generally 100 wt% FX 1821 where the film is used only for early-season weed suppression, but the more common field configuration blends 85–90 wt% FX 1821 with 10–15 wt% PBAT and 2–5 wt% carbon black masterbatch to suppress UV embrittlement and raise machine-direction elongation at the moment of laying; no photostabilizer package is added because it would delay the required soil fragmentation after the crop. Downstream production is a single-layer blown film line equipped with a 1.4–1.8 m lay-flat width capability, die gap 0.8–1.2 mm, BUR 2.5–3.5, and automatic gauge control with total thickness variance not exceeding ±2 µm; the film is perforated and wound on 3-inch cores, then installed by tractor-mounted laying equipment at 2–4 km/h, with soil incorporation after harvest by rotary tiller to 15–20 cm depth to establish microbial contact. Terminal finished products include black and white soil-biodegradable mulch for tomato, pepper, and maize silage rows, as well as low-tunnel ground cover where short-season weed suppression is required. Published multi-season field data for FX 1821 specifically under EN 17033:2018 remains limited; converters must validate degradation rate in local soil moisture and temperature conditions rather than extrapolating from compost-disintegration data. The operational boundary is that FX 1821 mulch is not intended for multi-year orchard cover or permanent weed barriers, and failure to shred the film before soil incorporation can leave large fragments that remain visible beyond 24 months and fail the EN 17033 ecotoxicity screen.
Where short-contact dry food overwrap replaces LDPE on vertical form-fill-seal lines, the critical process variable for FX 1821 is heat-seal initiation temperature, not total migration, because dry bakery goods are low-moisture solids with limited contact area. Industry compliance standards for this segment are Regulation (EU) No 10/2011 on plastic materials and articles intended to come into contact with food, with an overall migration limit of 10 mg/dm² measured by EN 1186-1:2002; in the United States, FDA status must be confirmed through a Food Contact Statement for the specific blend because PLA copolymers are not uniformly covered by a single generic clearance, and published data for this specific FX 1821 food-contact configuration is limited. The addition ratio is typically 70–80 wt% FX 1821 core, 15–20 wt% low-melting PLA/PBAT seal layer, and 5–10 wt% outer skin containing 0.5–1.5 wt% synthetic silica antiblock; this structure allows the sealing layer to initiate at 95–110 °C while the core retains stiffness for machinability. Downstream production is a three-layer coextrusion blown film line with die gap 0.8 mm, BUR 2.0–2.8, frost line height 400–600 mm, and corona treatment to 38–42 mN/m; the film is converted on a VFFS machine with jaw temperature 95–110 °C, dwell 0.2–0.5 s, and forming tube diameters from 80–180 mm; pre-drying of FX 1821 to 0.10 wt% moisture is required before coextrusion to prevent interlayer bubble instability. Finished product types include bread bags for sliced loaves, bakery bags for rolls and pastries, and dry snack pouches for crispbreads; the film is not recommended for high-moisture produce or wet foods because the PLA-based seal can lose integrity at sustained relative humidity above 85%.
Mailer film puncture in e-commerce logistics is a two-layer failure mode: the outer FX 1821 skin resists scuffing and perforation from automated sorting equipment, while the inner seal zone must damp impact energy without delamination at the fold line. Compliance in this segment is governed by 94/62/EC Annex II heavy metal limits of ≤100 mg/kg, REACH candidate list disclosure for substances above 0.1 wt%, and, when marketed as compostable, EN 13432:2000/AC:2005 or ASTM D6400-23 with disintegration under ISO 20200 or ISO 16929; mechanical tear and puncture are benchmarked according to ASTM D1922-09 and ASTM F1306-19. The formulation addition ratio for a 35–50 µm mailer consists of an outer layer with 80–90 wt% FX 1821 and 10–20 wt% PBAT-rich copolyester inner layer, plus 2–5 wt% filler masterbatch in the core if higher opacity is required; post-industrial regrind is limited to 10–20 wt% and only in the core layer to maintain outer-surface scuff resistance. Downstream production uses a two-layer or three-layer blown film coextrusion line with die gap 1.0 mm, BUR 3.0–3.5, melt temperature 160–180 °C, and in-line corona treatment to 38–42 mN/m for water-based flexographic printing or digital inkjet; after slitting and folding, compostable pressure-sensitive adhesive closure strips are applied, and seam strength is tested at 23 °C and 50% RH after 24 h conditioning. Terminal products include opaque e-commerce shipping mailers, document envelopes with tear strips, and courier pouches for non-food logistics. The operational boundary is that mailers with FX 1821 outer skins should not be exposed to continuous outdoor weathering beyond 30 days; UV exposure above 500 h QUV can promote surface cracking at the fold before the seal layer fails.
The thinnest commercial application — multipack tissue overwrap at 14–18 µm — demands that blocking resistance be formulated into the surface, not applied as a secondary powder, because powder contamination compromises automatic paper-bundle scanning and printability. Compliance for this non-food segment is limited to REACH SVHC disclosure at 0.1 wt%, absence of heavy metals above 100 mg/kg under 94/62/EC, and, if the overwrap is sold as compostable, EN 13432:2000/AC:2005; food-contact clearance is not required but converters still request a low-odor declaration because the film is used near paper bedding and personal care items. The formulation addition ratio is 100 wt% FX 1821 for standard machine runs, with 0.5–1.5 wt% synthetic silica antiblock concentrate added when film-to-film blocking is observed at rewind storage temperatures above 30 °C; slip agents are kept below 1 wt% to avoid seal-strength loss on hot-knife overwrap machines. Downstream production uses a single-layer or two-layer blown film line with die gap 0.6–0.8 mm, BUR 3.0–3.5, frost line height 300–500 mm, and high-speed winding at 150–250 m/min; the film is converted on automatic tissue bundlers using hot-knife or hot-wire sealing at 130–150 °C with dwell 0.2–0.4 s, and shrink must be minimal because the overwrap is a tight bundle rather than a heat-shrink sleeve. Terminal finished products include four-roll and six-roll household tissue bundles, kitchen towel sleeves, and compressed personal-care packs. The operational boundary is that gauge below 12 µm is not advisable on conventional air-cooled blown film lines because bubble breathing and die-lip build-up create localized thickness bands that reduce bundle integrity.
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Bio-Flex FX 1821 is an opaque low-gauge blown film PLA blend supplied as granulate for conventional single-screw blown film extrusion. The compound is formulated to produce film in the 15 µm to 50 µm range; opacity is achieved through a dispersed scattering phase rather than by pigmentation alone. The material combines a PLA-rich continuous phase with a biodegradable copolyester impact-modifying phase. This structure differs from unmodified PLA by reducing brittle failure in thin films and differs from PBAT-rich compostable films by retaining higher modulus. Application areas include organic waste collection bags, lightweight shopping bags, and secondary packaging where industrial compostability claims are evaluated under DIN EN 13432:2000-12 and ASTM D6400.
Pre-drying is mandatory at ambient relative humidity above 60% or after more than 4 h of open-container storage. A desiccant dryer set at 60 °C for 4 h with a dew point at or below -30 °C reduces residual moisture below 250 ppm. Above this moisture level, hydrolytic chain scission reduces melt viscosity and causes sudden bubble tears. On a 45 mm single-screw extruder with 30:1 L/D, barrel profiles from 150 °C in the feed zone to 175 °C in the metering zone are used. The die temperature is maintained at 170 °C to 180 °C. The effective melt-temperature window for low-gauge bubble stability is narrow; excursions below 155 °C increase surface sharkskin, while excursions above 185 °C increase die-lip build-up and film gels. The die zone should be controlled within ±5 °C of the set point.
Die gap settings between 0.8 mm and 1.2 mm are typical. Below 20 µm, the narrower gap improves transverse gauge uniformity; wider gaps reduce backpressure on older extruders. Blow-up ratios from 2.2:1 to 2.8:1 are used to balance machine-direction and transverse-direction properties. Frost line height is set at 2 to 4 die diameters. Raising the frost line increases machine-direction tear resistance but reduces bubble stability because slow PLA crystallization between 90 °C and 120 °C (ISO 11357-3:2018) prolongs the tacky region. Dual-lip air rings and internal bubble cooling are used on high-output lines below 20 µm; published data for the specific interaction between internal bubble cooling volume and FX 1821 melt strength is limited, so starting conditions require line trials.
Production-scale failure modes include die-lip build-up after prolonged runs above 180 °C and surface sharkskin when melt temperature falls below 150 °C. Die-lip build-up is controlled by purging with a PLA-compatible purge compound and by avoiding hold-up times longer than 10 min at melt temperature. The use of 1 wt% to 3 wt% of a PLA-compatible slip/antiblock masterbatch reduces blocking at film gauges below 20 µm; addition above 5 wt% can lower dart impact resistance and increase particle-related film defects. The product is not processed with barrier screws containing Maddock mixing elements because high-shear dispersive mixing over-shears the PLA phase. Melt filters with 100 mesh to 150 mesh screens are used to remove gel particles from opaque film.
Thermal degradation of PLA-based compounds proceeds through two competing pathways: chain scission from residual moisture and lactide reformation from backbiting at high temperature. For Bio-Flex FX 1821, the maximum recommended melt residence time is 10 min at 170 °C; at 190 °C, the residence time should not exceed 5 min. The copolyester phase lowers melt viscosity and reduces shear heating compared with high-molecular-weight PLA homopolymer, but it also broadens the melting range and delays solidification. Capillary rheometry under ISO 11443:2021 shows shear-thinning behaviour; low-shear viscosity is higher than PBAT-rich compounds, which stabilizes the bubble, while high-shear viscosity is low enough for thin-gauge extrusion. The exact viscosity curve should be obtained from the current technical datasheet because it depends on moisture content and additive package. Crystallization under blown film cooling is suppressed; the resulting film is predominantly amorphous and can develop post-crystallization shrinkage above 50 °C.
Current manufacturer technical data for Bio-Flex FX 1821 granulate report a density of 1.24 g/cm³ (ISO 1183-1:2019) and a melt flow rate of 4.0 g/10 min at 190 °C and 2.16 kg (ISO 1133-1:2022). The melt flow rate is a low-shear indicator and should not be used alone to predict blown film bubble stability. Tensile strength at break in 30 µm blown film is higher in machine direction than transverse direction; elongation at break is typically above 200% in both directions under ISO 527-3:2018. Elmendorf tear strength under ISO 6383-2:1983 is lower than PBAT-rich films but higher than unmodified PLA; typical machine-direction values are in the 5 N to 8 N range for 30 µm film. Published data for specific low-gauge configurations of Bio-Flex FX 1821 is limited, so converter-specific values should be confirmed by lot trials. Gauge uniformity below 20 µm is measured with an on-line capacitance gauge; variation above ±5% causes bag-width control problems in side-seal and wicket configurations.
Downstream converting limits are set by the higher modulus and lower surface energy of PLA-rich film. Corona treatment to a minimum surface energy of 38 mN/m (ISO 8296:2003) is required before flexographic or gravure ink application. Water-based inks and UV-curing overprint varnishes are preferred; solvent-based inks containing ketones or acetates can swell the PLA surface and reduce heat-seal strength. Heat sealing is generally performed against a PLA-compatible seal layer rather than using Bio-Flex FX 1821 itself as a self-sealing surface. Bag-making equipment should be adjusted for higher spring-back and lower elongation compared with PBAT-rich films. Perforation and tear features must be tested with ISO 6383-2:1983 because tear anisotropy is sensitive to frost line height and blow-up ratio. The opacity additive package increases film density and can affect ultrasonic sealing; contact pressure and amplitude should be re-optimized when changing from translucent PBAT-based structures.
Substitution on an existing PBAT-rich line requires changes in temperature set points, screw speed, and bubble geometry. PBAT-rich compounds typically process at 130 °C to 150 °C; Bio-Flex FX 1821 requires melt temperatures of 160 °C to 180 °C. The temperature increase must be performed in 5 °C to 10 °C increments to avoid thermal degradation of residual PBAT phase in the die. Screw speed is typically reduced by 10% to 20% during start-up because shear heating can push the melt above the upper limit. Blow-up ratio may be reduced from 3.0:1 to 2.2:1 to 2.8:1, and frost line height lowered to 2 to 3 die diameters. For lines equipped with gravimetric dosing, output is limited by melt temperature rather than by screw torque; higher barrel temperatures may reduce viscosity enough to maintain torque, but the melt film in the die is closer to degradation. Thermocouple immersion depth and die temperature uniformity should be verified before start-up.
The following table compares Bio-Flex FX 1821 with unmodified PLA and PBAT-rich compostable film at a qualitative level; converter-specific trials are required to confirm gauge limits and mechanical values.
| Parameter | Bio-Flex FX 1821 | Unmodified PLA film | PBAT-rich compostable film |
|---|---|---|---|
| Lowest stable blown film gauge | 15 µm to 20 µm | 25 µm and above | 10 µm to 15 µm |
| Tensile modulus | Medium-high | High | Low |
| Elongation at break | Medium | Low | High |
| Tear propagation resistance | Medium | Low | High |
| Opacity | Opaque | Translucent | Translucent to opaque |
| Melt temperature window | 160 °C to 180 °C | 170 °C to 200 °C | 130 °C to 150 °C |
The differences in modulus and tear anisotropy affect downstream bag conversion. A lower elongation at break increases the required web tension control accuracy. The higher stiffness reduces film blocking but can increase crease formation during folding. If the converter uses a rotary die cutter, blade sharpening intervals are shortened because the dispersed opaque phase is abrasive. For seal integrity, the seal bar temperature may need to be increased by 5 °C to 10 °C relative to PBAT-rich structures. Print adhesion requires corona treatment because PLA has a lower surface energy than oxidized PBAT; without treatment, ink adhesion measured by tape pull can fall below acceptable limits.
Industrial compostability claims for Bio-Flex FX 1821 must be verified against current DIN EN 13432:2000-12 and ASTM D6400 certificates covering the final film structure.
| Compliance criterion | Standard / method | Assessment basis |
|---|---|---|
| Industrial compostability | DIN EN 13432:2000-12 | Certification body certificate for final film |
| Compostability in North America | ASTM D6400 | Third-party certification |
| Heavy-metal limits | EN 13432, Annex E | Raw-material disclosure |
| Disintegration under composting | ISO 16929:2021 | Laboratory-scale compost test |
| Food-contact migration | Regulation (EC) No 10/2011 | Migration testing of finished article |
Certification is grade-specific and can be invalidated by adding non-certified masterbatch, printing ink, or adhesive. The grade is not intended for home compost, marine degradation, or anaerobic digestion unless separate certificates are available. For food-contact articles, migration testing under Regulation (EC) No 10/2011 and FDA 21 CFR must confirm that specific migration limits for the final additive package are met. Storage in sealed moisture-barrier bags at 15 °C to 30 °C is required; partially used containers exposed to ambient air above 60% RH for more than 30 min should be re-dried. Residual moisture of granulate can be checked by a Karl Fischer oven method; values above 250 ppm are unacceptable for thin-gauge production. Regrind levels above 20% are not recommended for films below 20 µm because gel counts and bubble instability increase. The material is not suitable for contact with strong alkaline cleaning agents or amine-based additives because PLA undergoes hydrolysis and chain scission under alkaline conditions.