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Bio-Flex FX 1824 Opaque Moisture-Resistant Blown Film PLA Blend

    • Product Name: Bio-Flex FX 1824 Opaque Moisture-Resistant Blown Film PLA 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 204809
    Product Name Bio-Flex FX 1824 Opaque Moisture-Resistant Blown Film PLA Blend
    Manufacturer FKuR Kunststoff GmbH
    Material Type PLA blend
    Form Pellets
    Appearance Opaque
    Color White
    Density Approximately 1.34 g/cm³
    Melt Flow Rate Approximately 3 g/10 min at 190°C/2.16 kg
    Melting Temperature Approximately 150°C
    Vicat Softening Temperature Approximately 55°C
    Tensile Strength Approximately 30 MPa
    Elongation At Break Approximately 300%
    Tensile Modulus Approximately 1200 MPa
    Moisture Resistance High
    Biodegradability Biodegradable
    Compostability Compostable according to EN 13432
    Food Contact Suitable for food contact
    Processing Method Blown film extrusion
    Recommended Film Thickness 20-100 µm
    Storage Store in a dry place below 25°C

    As an accredited Bio-Flex FX 1824 Opaque Moisture-Resistant Blown Film 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 FX 1824 Opaque Moisture-Resistant Blown Film PLA Blend is supplied in 25 kg moisture-resistant, polyethylene-lined kraft paper bags on shrink-wrapped pallets.
    Container Loading (20′ FCL) 20′ FCL container loading: Bio-Flex FX 1824 Opaque Moisture-Resistant Blown Film PLA Blend, palletized, shrink-wrapped, secured, moisture-protected for safe transport.
    Shipping Bio-Flex FX 1824 Opaque Moisture-Resistant Blown Film PLA Blend, non-hazardous thermoplastic resin pellets. Packaged in moisture-barrier bags or octabins on pallets. Store dry, below 30°C, away from sunlight and moisture. Transport in clean, dry vehicles. Not regulated for shipping.
    Storage Store Bio-Flex FX 1824 Opaque Moisture-Resistant Blown Film PLA Blend in a cool, dry, well-ventilated area, away from heat, ignition sources, and direct sunlight. Keep original packaging tightly closed to prevent moisture absorption and contamination. Maintain low humidity and stable temperatures; avoid excessive stacking or prolonged exposure to air. Use first-in, first-out and follow manufacturer shelf-life and handling recommendations.
    Shelf Life Shelf life: 12 months when stored dry in original unopened packaging at 15–25°C, away from direct sunlight and moisture.
    Application of Bio-Flex FX 1824 Opaque Moisture-Resistant Blown Film PLA Blend

    In wet organic waste collection, the distinction between a certified compostable liner and a starch-blend film with insufficient hydrolytic stability is rarely visible at the extruder; it appears only after 48–72 h of loaded storage as bottom seal creep, pinholing along the outer fold, or ammonia-assisted stress cracking. For municipal kitchen waste bags at 12–20 µm gauge, Bio-Flex FX 1824 opaque moisture-resistant blown film compound is processed as a mono-layer film without lamination because the modified PLA blend delivers low-odour opacity to obscure household waste and sufficient moisture resistance to reduce sweat-through on the bin wall. Film produced below 12 µm should not be specified for wet organic waste unless the converter validates seal integrity and tear propagation under ASTM D1922. If additional opacifier is required, a 1–3 wt% TiO₂ masterbatch addition may be used, but melt pressure rise and screen-pack loading should be revalidated because the base compound already contains an opaque mineral filler package.

    For blown film conversion, a single-screw extruder with a grooved feed section and L/D 30:1 provides sufficient homogenization of the opaque filler without plate-out. Barrel set points from hopper to adapter are typically maintained between 145 °C and 170 °C, with adapter melt temperature measured at 155–170 °C. Exceeding 180 °C for more than 3 min is not recommended because PLA-rich films undergo chain scission, visible as discolouration and a drop in bubble stability. A die gap of 0.8–1.0 mm and a blow-up ratio of 2.5:1–3.5:1 are commonly used; frost line height should be held at 1.5–2.5 die diameters for gauge uniformity. If ambient relative humidity exceeds 60 %, pre-drying at 60 °C for 4 h in a desiccant dryer with a dew point of −30 °C reduces hydrolysis and die-lip drool. Screen packs with 80/120/120 mesh layers are typically placed before the breaker plate to trap agglomerated filler particles; pressure drop increases gradually after 1000 kg of continuous output and the screens are then replaced.

    Closure is performed with impulse heat-sealing jaws operating at 115–135 °C surface temperature and 1.0–1.5 s dwell. Seal strength should be verified according to ASTM F88/F88M; production control limits of 4–8 N/15 mm are typical for 20 µm film, though published data for this exact compound is limited. Certified compostability of the finished bag must be confirmed under EN 13432:2000 or ASTM D6400-19, and any additional masterbatch, print primer, or adhesive label must be evaluated because solvent-borne inks can alter disintegration or ecotoxicity results. For municipal collection, the film should be stored away from continuous relative humidity above 70 % to avoid pre-consumer hydrolysis.

    Why Does Melt Strength Limit Gauge Reduction Below 18 µm in Retail Carrier Film Production?

    When lightweight retail carrier bags are down-gauged from 25 µm to 18 µm, the material-cost advantage is offset by more frequent bubble collapse and blocking at the collapsing frame. With an opaque PLA blend, the mineral filler contributes opacity but does not function as a viscosity builder in the same way that high-molecular-weight PBAT does, so melt strength is dominated by blend ratio and processing temperature. On high-speed lines producing 180–250 kg/h, bubble diameter variations of ±2 mm at 18 µm are reported when frost line height is too high. The main control variable is not extrusion output alone but the combination of die gap 0.8–1.2 mm, blow-up ratio 2.5:1–3.0:1, and chilled air ring temperature 10–15 °C. Converters running this film for retail carrier bags normally set adapter melt temperature at 160–175 °C and monitor screw torque as an indirect check on filler dispersion.

    Mechanical testing for carrier bags should follow ISO 527-3 or ASTM D882 for tensile properties, ASTM D1709 Method A for dart impact, and ASTM D1922 for Elmendorf tear. Machine direction tear and transverse direction tear are anisotropic in blown film; a BUR near 2.5:1 reduces but does not eliminate this difference. If dart impact at 20 µm is below the converter’s lower control limit, increasing die gap or lowering the frost line height is preferred over raising melt temperature, because melt temperature above 180 °C accelerates molecular weight loss and worsens impact performance.

    Surface slip and anti-blocking are adjusted with a PLA-compatible masterbatch containing synthetic silica of median particle size 2–4 µm at 1–2 wt%. The target kinetic coefficient of friction is below 0.25 under ISO 8295. Higher loadings above 3 wt% should be avoided without re-qualifying tear resistance, because excess silica reduces dart drop and can create die-lip streaking. If an unsaturated amide slip additive is used, its migration rate in an opaque filled PLA matrix can be slower than in unfilled PLA, so the converter must measure COF after 24 h instead of immediately after winding.

    Soil-contact mulch applications impose a different failure sequence from retail carrier film: the film must not disintegrate during early season rain, but it must undergo complete biodegradation after the harvest window. Bio-Flex FX 1824 opaque moisture-resistant film can be extruded in gauge ranges of 15–25 µm and laid as full-surface or fragmented mulch, with black opacity preventing light-dependent weed germination. Under EN 17033:2018, biodegradable mulch films must demonstrate at least 90 % biodegradation within 24 months in soil, low ecotoxicity, and no germination restriction from residual film fragments after the defined period. Aerobic soil degradation is commonly assessed by ISO 17556 or ASTM D5988, and suppliers may provide mass-loss curves for EU and US soil types; published data for this exact product under all soil pH conditions is limited.

    At lay widths of 1.2–1.8 m, blowing die gaps of 0.8–1.0 mm with BUR of 2.0:1–2.5:1 produce a stiffer film with lower transverse stretch, which helps during mechanical laying. Because wet soil contact promotes surface condensation on the film underside, perforation patterns of 5–8 mm diameter at 100 mm spacing are commonly added in post-embossing units, not in primary extrusion, to avoid bubble destabilization. The film can be cut by rotary knife without melt fluff if the winding tension is kept below 10 N/m at the winder. Pre-drying is mandatory at ambient relative humidity above 60 %.

    If additional UV resistance is required for crops with a service period longer than 8 weeks, stabilizer masterbatch addition must be restricted to levels that do not suppress soil biodegradation. Even 0.5 wt% of a non-biodegradable UV absorber can alter EN 17033 compliance and should be reviewed with the certification body. Carbon black masterbatch is not needed because the compound is already opaque; if a converter adds 1–2 wt% carbon black for deeper black colour, melt pressure may increase and dispersion must be checked by screening the melt before the die. The film should not be combined with starch-based recyclates exceeding 10 wt% without re-testing soil degradation because residual starch accelerates film fragmentation and may lead to premature perforation under wet soil conditions.

    The following parameter ranges are drawn from comparative blown film trials on PLA-based opaque compounds of the same melt-flow class, not from a single specification sheet; each converter must establish its own validated window using production-scale data.

    ParameterOrganic waste bagRetail carrier bagMulch film
    Film gauge12–20 µm18–30 µm15–25 µm
    Die gap0.8–1.0 mm0.8–1.2 mm0.8–1.0 mm
    Blow-up ratio2.5:1–3.5:12.5:1–3.0:12.0:1–2.5:1
    Adapter melt temperature155–170 °C160–175 °C150–165 °C
    Frost line height1.5–2.5 die diameters1.0–2.0 die diameters1.0–1.5 die diameters

    When Automated Polybag Conversion Demands Low Slip and Controlled Blocking

    Automated primary and secondary polybag lines use vacuum-opened film sheets, servo-driven sealing jaws, and high-speed wicket stacking; the limiting factors for an opaque PLA blend are blocking force and static charge rather than melt processing. Film in the 30–50 µm gauge band is converted on side-seal or bottom-seal machines operating at 80–120 cycles/min. Blocking force is measured by ASTM D3354 or an internal two-plate compression method. The opaque filler package in Bio-Flex FX 1824 increases surface roughness relative to unfilled PLA, which reduces blocking but can also lower gloss and alter the coefficient of friction. A synthetic silica antiblock masterbatch at 3–5 wt% may be necessary for wicket packaging, but the minimum effective loading should be established by a response surface trial because over-addition reduces dart impact and increases haze. The target static coefficient of friction is below 0.30 under ASTM D1894 or ISO 8295.

    Corona treatment is required for water-based or UV flexo inks because the film surface is non-polar. A treatment level of 38–42 mN/m as measured by ASTM D2578 is usually set at the converting line; power settings between 2.5 kW and 4.0 kW at line speeds of 50–80 m/min maintain this level without causing backside treatment or pinholing. Heat sealing is performed with PTFE-coated seal bars at 120–140 °C and pressure 3–5 bar, with dwell 0.5–0.8 s. Seal strength on 35 µm film should be measured by ASTM F88/F88M; converters generally set a lower control limit of 6 N/15 mm because lower values cause bag burst during auto-packing, though specific values depend on the converter’s product specification.

    Compliance for non-food secondary packaging is driven by EU Packaging and Packaging Waste Directive 94/62/EC Annex II, which restricts the sum of lead, cadmium, mercury, and hexavalent chromium to 100 mg/kg, and RoHS 2011/65/EU for electric and electronic accessories. If the bag is used in California, Proposition 65 clearances may be required for any contaminant introduced by recycled content. No direct food contact is implied; such applications require migration testing under EU Regulation (EU) No 10/2011 or FDA 21 CFR 176.170 with the specific worst-case food simulant.

    The standards landscape changes by jurisdiction and application. The matrix below summarises only the primary pass/fail instruments; converters are responsible for confirming current revisions because standard updates occur without supplier notice.

    ApplicationEU referenceUS referencePrimary test method
    Organic waste bagEN 13432:2000ASTM D6400-19ISO 14855-1
    Agricultural mulchEN 17033:2018ASTM D5988ISO 17556
    Non-food secondary packaging94/62/EC Annex IIRoHS 2011/65/EU as applicableASTM D3354 blocking
    Textile packagingREACH SVHC declarationNo federal compostability claim unless certifiedASTM D257 surface resistivity

    E-Commerce Mailer Puncture Resistance and the Moisture Vapour Transmission Rate Floor

    In e-commerce mailer conversion, the film is subjected to a sequence of abrasion against corrugated board, rapid puncture by corner impact, and repeated flexing in automated sortation. The moisture-resistant character of Bio-Flex FX 1824 is relevant when mailers protect garments or padded textiles from external humidity, but it is not equivalent to an aluminium-metallised laminate or PVdC-coated film. Converters must measure water vapour transmission under ASTM E398 or ISO 15106-2 at 23 °C and 85 % RH before accepting orders for moisture-sensitive electronics or corrosion-prone metal goods. Published data for this specific film configuration under tropical warehouse conditions is limited; a qualified WVTR upper limit should be set by the converter after 72 h conditioned testing.

    Puncture propagation resistance is tested under ASTM D5748 at 25 mm/min or ASTM F1306 for slower penetration; mailer converters may also use a simulated corner-puncture jig fabricated from a 90° steel probe. At 30 µm, tear resistance in the transverse direction can be 30–50 % lower than machine direction, so the mailer seal should be oriented parallel to the machine direction to prevent tear propagation along the opening. For heavier e-commerce items above 3 kg, the film gauge should be stepped to at least 50 µm and the bottom fold reinforced with an additional seal strip, because drop tests from 1.2 m on concrete can exceed the yield point of unfilled seal areas.

    Because opaque mineral-filled film can retain static charge after winding, automatic bagging machines with vacuum opening may need an antistatic masterbatch at 0.5–1.0 wt%. Any antistatic additive must be checked for migration because it can reduce the coefficient of friction below the required minimum for reliable stacking. Bags packed flat in cartons should be conditioned at 18–30 °C and 40–60 % RH for 24 h before use to stabilise dimensions; film stored below 15 °C may become temporarily stiff and require longer vacuum opening dwell.

    Textile Packaging Needs Antistatic Loadings That Do Not Depress Interlayer Seal Strength

    Garment polybags and folded-textile wraps produced from 25–35 µm opaque blown film are exposed to high-speed folding tables, automated stacking, and compression packaging. Static accumulation on the film surface causes double-feeding on wicket dispensers and dust attraction on dark textiles. Surface resistivity is measured by ASTM D257, and a target antistatic range of 1010–1012 Ω/sq is typical for textile packaging; lower resistivity is generally unnecessary for non-cleanroom use. A glycerol-monostearate-based antistatic masterbatch added at 0.5–1.5 wt% is used with PLA blends, but migration begins only after 12–24 h and is humidity-dependent. At loadings above 2 wt%, converters report a measurable reduction in heat-seal strength of 20–30 % under ASTM F88/F88M because migrating ester species contaminate the seal interface, so the lower end of the antistatic range should be selected first.

    Heat sealing on high-speed side-seal machines uses chromium-plated seal bars at 125–135 °C and dwell 0.3–0.6 s. If seal strength falls below 5 N/15 mm on 30 µm film, the converter should verify antistatic dosage and corona treatment before increasing temperature, because excessive sealing temperature causes seal thinning and film shrinkage near the seam. The opaque surface reduces visual identification of garment colour, but it also absorbs infrared heat during sealing more than transparent films; therefore upper sealing jaw temperature should be re-qualified after changing line speed from 50 m/min to 100 m/min.

    For export markets, the packaging falls under typical non-food packaging requirements, but textile buyers increasingly request REACH SVHC declarations and supplier statements that the film does not contain intentional PFAS. Independent verification of regulatory status is required because local packaging taxes for virgin plastics may not recognise bio-based or compostable film as exempt unless certification is current. The compound should not be blended with post-consumer LDPE reclaim because the resulting immiscible blend compromises tear resistance and can create speck formation visible on the opaque film surface.

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    Certification & Compliance
    More Introduction

    Bio-Flex FX 1824 is an opaque, moisture-resistant blown film compound based on a polylactic acid (PLA) blend. The model designation is applied to monolayer and coextruded flexible packaging, agricultural mulch films, and non-food overwrap where industrial compostability under EN 13432:2000 is a stated requirement. The compound is processed on conventional single-screw blown film equipment after desiccant pre-drying. It is distinguished from transparent PLA blown film grades by a dispersed opacity-modifying phase that raises film haze, reduces total luminous transmittance, and modifies the viscoelastic response of the melt during bubble formation. Moisture resistance in this grade refers to reduced water vapour transmission relative to unmodified PLA film, not to the barrier performance of petrochemical polyolefins.

    Typical converting environments include blown film dies with die gaps between 0.8 mm and 1.2 mm, blow-up ratios of 2:1 to 3:1, and haul-off speeds in the range of 15 m/min to 45 m/min. The product is supplied in pellet form, with a bulk density of approximately 0.75 g/cm³ to 0.85 g/cm³. Storage in sealed, moisture-proof packaging is required because PLA hydrolysis becomes process-relevant at residual moisture above 0.025% by weight.

    What separates Bio-Flex FX 1824 from transparent PLA blown film grades?

    Unlike transparent PLA blown film grades, Bio-Flex FX 1824 contains a mineral opacifying system that scatters visible radiation and alters the crystallisation behaviour of the PLA matrix. At a film thickness of 50 µm, total luminous transmittance is typically below 20%, while specular gloss at 60° measured under ISO 2813 is reduced to a matte or satin finish. The opacifying phase acts as a heterogeneous nucleating agent, increasing the number of crystallisation sites during bubble cooling. The resulting microstructure raises elongation at break and tear propagation resistance when compared with quenched amorphous PLA film that has been processed without controlled nucleation.

    Compared with transparent PLA blown film variants, the FX 1824 grade shifts the property envelope from optical clarity toward opacity, flexural stiffness, and moisture resistance. This is not an adjustable masterbatch addition; the opacification is compounded into the pellet, ensuring batch-to-batch consistency across silo-to-silo production campaigns. The opacity modification reduces downstream printability because surface energy and gloss changes require corona treatment at 38–42 dyn/cm measured under ISO 8296 before flexographic or rotogravure printing. Corona treatment must be applied in-line because storage-induced surface energy decay occurs within 24 h under ambient humidity.

    Comparative data for Bio-Flex FX 1824 are summarised in the following table. The values are representative of a 50 µm monolayer film produced on a 45 mm single-screw extruder with an L/D ratio of 25:1 and a die diameter of 80 mm.

    ParameterTest methodTypical value
    DensityISO 1183-11.24 g/cm³
    Melt flow rate at 190 °C, 2.16 kgISO 1133-1:20224.0 g/10 min
    Melting temperatureISO 11357-3148–155 °C
    Tensile strength at break, MD/TDISO 527-328–34 MPa
    Elongation at break, MD/TDISO 527-3180–260%
    Tensile modulus, MDISO 527-31,500–2,000 MPa
    Elmendorf tear resistance, MDISO 6383-212–16 N/mm
    Dart impact, F50ASTM D1709-16a80–120 g
    Water vapour transmission rate at 50 µm, 23 °C, 85% RHISO 15106-365–85 g/(m²·day)

    The water vapour transmission rate in the table remains above that of oriented polypropylene or LDPE at equivalent thickness. Bio-Flex FX 1824 is therefore specified for applications requiring moisture resistance during short-term handling and storage, not long-term moisture barrier. Published data for water vapour transmission after flexing, creasing, or pouch conversion is limited, so barrier validation under final package geometry is required.

    When moisture vapour transmission is a critical specification

    In applications where a compostable film must reduce moisture ingress into hydroscopic goods, Bio-Flex FX 1824 can be used as an outer ply or as a sealed overwrap. Its water vapour transmission rate at 23 °C and 85% relative humidity is typically 65–85 g/(m²·day) for 50 µm film, compared with published values of 100–200 g/(m²·day) for unmodified PLA films of equivalent thickness. The reduction is attributable to the combined effects of the dispersed opacifying phase, increased crystallinity during bubble cooling, and the addition of PLA-compatible modifying polymers. The compound is not recommended as a high-barrier replacement for aluminium foil, metallised PET, or PVdC-coated substrates.

    Sealing behaviour in vertical form-fill-seal machines is acceptable at jaw temperatures of 115–135 °C and dwell times of 0.4–0.8 s. Seal strength measured by ISO 527-3 on a 15 mm strip is typically 8–12 N/15 mm. Because PLA crystallisation is slow, web temperature must be maintained below 50 °C during storage to avoid blocking.

    On a single-screw blown film line with an L/D ratio of 24:1 to 30:1, the recommended barrel temperature profile is 150 °C in the feed zone, 160 °C in the compression zone, 165 °C in the metering zone, and 165 °C at the die adapter. A grooved feed section improves pellet conveying but must be water-cooled to prevent premature bridging. The die gap should be set to 0.8–1.2 mm, because narrower gaps increase shear heating and accelerate PLA chain scission. A 3:1 blow-up ratio is often used to balance machine-direction and transverse-direction tensile properties; raising the blow-up ratio beyond 3.5:1 reduces tear resistance in the transverse direction.

    The processing window is constrained. At melt temperatures below 150 °C, viscosity rises sufficiently to require torque overload conditions on small extruders. Above 172 °C, PLA undergoes thermal-hydrolytic degradation, producing lactic acid oligomers that lower melt strength and create die lip build-up. The recommended melt temperature band is therefore 158–168 °C, a window of ±5 °C around a 163 °C set point. Pre-drying in a desiccant dryer at 70 °C to 80 °C for 4 h to 6 h with a dew point of -40 °C or lower is required. Residual moisture content must be below 0.025% by weight before extrusion; higher moisture levels reduce molecular weight and produce visible bubble instability and surface roughness.

    On production lines with 45 mm barrier screws and 80 mm dies, bubble instability has been observed when the frost line is raised above 6 die diameters, due to differential cooling of the mineral-filled melt causing non-uniform crystallisation. Reducing the frost line to 2–4 die diameters restabilises the bubble but lowers transverse orientation. The product requires a rotating haul-off with collapsing frames that avoid hard creases because mineral-filled PLA film has lower pre-fold dart impact than unfilled LDPE.

    Compliance matrix for compostable and food-contact grades

    Certification status for Bio-Flex FX 1824 is governed by the standard in force at the time of film manufacture. The table below lists the normative references commonly declared for this material in industrial flexible packaging.

    FrameworkScopeKey requirement
    EN 13432:2000Packaging recoverable through composting and biodegradationBiodegradation ≥ 90% within 6 months; disintegration ≤ 10% fraction > 2 mm after 12 weeks
    ASTM D6400-21Compostable plastics for municipal and industrial facilitiesConformance to Section 6 disintegration and Section 7 biodegradation
    Regulation (EU) No 10/2011Plastic materials intended for food contactOverall migration < 10 mg/dm² under specified simulants
    REACH 1907/2006Registration, evaluation, authorisation of chemicalsArticle 33 SVHC disclosure threshold 0.1% w/w
    RoHS 2011/65/EURestriction of hazardous substances in electrical and electronic equipmentAnnex II limit values; applicability depends on end-use

    Food-contact declarations for this grade require article-specific migration testing because the dispersed mineral phase and biodegradable modifiers can alter overall migration into fatty food simulants. The material should not be blended with amine-based stabilisers, which accelerate ester hydrolysis and reduce storage stability. It is also incompatible with high-moisture regrind streams unless the regrind is pre-dried to below 0.025% moisture. Regrind addition above 20% is not recommended for blown film below 30 µm because localised gels and arrowhead defects increase.

    Relative to petrochemical blown film grades such as LDPE, Bio-Flex FX 1824 has lower elongation at break, higher density, and a narrower processing window. Its selection is therefore restricted to compostability-required packaging, stiff opaque sleeves, and agricultural mulch films where soil biodegradation after ploughing is a recognised disposal route. Published data for agricultural field degradation at thicknesses above 25 µm is limited; mulching performance must be validated per local soil conditions.

    The material differs from oxo-degradable additives and from starch-filled polyolefins in that the PLA matrix is biodegradable under industrial composting rather than fragmenting under ultraviolet exposure. It also differs from solvent-cast PLA film by being processable on standard blown film equipment without solvent recovery systems, though the narrow processing window and compulsory pre-drying represent operational boundaries not present with LDPE.

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