| Код ТН ВЭД | 231291 |
Как аккредитованный завод Ingeo ™ Biopolymer 4043D Biaxially Oriented Film Extrusion PLA, мы соблюдаем строгие протоколы качества - каждая партия подвергается строгим испытаниям для обеспечения последовательных стандартов эффективности и безопасности.
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Biaxially oriented film extrusion from Ingeo™ Biopolymer 4043D for dry bakery and snack packaging begins with desiccant drying of the virgin pellets at 80 °C for 4–6 h to a moisture content below 250 ppm and a dew point of −40 °C or lower. The dry pellet is fed into a single-screw extruder with a 30:1 L/D barrier screw and a coat-hanger die; barrel zone temperatures are profiled from 160 °C at the feed throat to 200–210 °C at the die adaptor, with melt temperature measured at the die between 180 °C and 205 °C. The cast sheet is pinned to a polished chrome chill roll held at 20–35 °C to suppress spherulitic crystallisation and preserve transparency. For a 25 µm finished film, cast sheet thickness is typically 200–250 µm, with automated die bolt control maintaining transverse thickness variation below ±2%. Sequential orientation is performed on a machine-direction roll unit at a draw ratio of 2.5:1–3.5:1 followed by a transverse stenter at 3.0:1–5.0:1, with preheat and stretching zones set between 65 °C and 85 °C. The oriented web is heat-set at 120–130 °C for 10–20 s to reduce free shrink at 70 °C to ≤2% in both axes. After orientation, a 25 µm heat-set film typically exhibits tensile strength between 100–150 MPa and elongation at break between 60–100% when tested according to ISO 527-3. Formulation adjustment is limited to a slip/antiblock masterbatch dosed at 1–3 wt%; higher loading raises haze above 3% when measured by ASTM D1003. The film is corona-treated in-line to a wetting tension of 42–46 dyn/cm using ISO 8296 for water-based flexographic or gravure ink adhesion. Compliance for dry bakery and snack contact is governed by EU Regulation (EC) No 10/2011 for plastic materials and articles intended to come into contact with food, with overall migration tested under EN 1186-1, and by the applicable FDA Food Contact Notification for the specific grade and end-use condition. Terminal products include flow-wrap pillow pouches for biscuits and crackers, transparent carton windows, and pre-formed bread bags where moisture ingress is not the dominant shelf-life variable.
Pressure-sensitive label facestocks based on Ingeo 4043D are produced at 50–75 µm thickness and require controlled transverse-direction stiffness for stable die cutting and automatic dispensing. The cast sheet is oriented at a machine-direction ratio of 2.5:1–3.0:1 and a transverse ratio of 3.5:1–4.5:1, then heat-set at 110–125 °C to keep unrestrained shrinkage below 1.5% after 5 min at 70 °C. The clear facestock is coated on one side with a water-based print primer at 0.5–1.0 g/m² dry coat weight; the reverse side receives a pressure-sensitive acrylic adhesive at 15–25 g/m² and a silicone release liner of 50–90 g/m². Printability is established by corona treatment to 42–46 dyn/cm according to ISO 8296. Register stability in multi-unit flexographic printing is influenced by the hygroscopic expansion of PLA under high relative humidity, so converters running above 60% RH maintain tension isolators and edge-guide sensors between print stations; without such controls, transverse movement across print repeat lengths produces misregister between varnish, white, and halftone units. Die cutting is performed with rotary magnetic cylinders at 100–200 m/min, where the orientational stiffness of 4043D film prevents matrix material from tearing across narrow label gaps. Compliance is governed by REACH Regulation (EC) No 1907/2006 and RoHS Directive 2011/65/EU for general label end uses; when the label is applied to food-contact packaging, the complete label construction must comply with FDA 21 CFR 175.105 for pressure-sensitive adhesives and the relevant food-contact status of the facestock. Terminal products include clear film labels for beverage bottles, cosmetic containers, logistics labels, and surface-printed personal care labels where biaxial orientation reduces moisture-induced curling in high-humidity storage.
Shrink sleeve conversion from Ingeo 4043D imposes the narrowest thermal window in this application portfolio because orientation memory is retained only when the cast sheet is stretched near the glass transition and quenched before secondary crystallisation dissipates chain orientation. On production lines equipped with tenter-frame orientation units, the cast sheet is preheated to 55–70 °C using short-wave infrared banks and stretched transversely at a ratio of 4.0:1–5.5:1 while the machine-direction draw is held below 1.5:1 to create an unbalanced shrink film. The stretching temperature must be controlled within ±5 °C across the web; below 55 °C, cold drawing produces stress whitening and transverse gauge bands, while above 80 °C, chain relaxation reduces free shrink at 80 °C below 40% and the sleeve cannot pull tightly over container shoulders. The oriented web is quenched on the stenter rails to below 45 °C before edge trimming, and the annealing section is either bypassed or maintained at 60–70 °C without relaxation to preserve orientation. Free shrink is measured in hot water at 80 °C for 10 s according to ASTM D2732; production targets for 4043D sleeves are 45–60% transverse shrink and 5–15% machine-direction shrink. Formulation changes are kept minimal because plasticisers that lower the stretching temperature also migrate to the film surface and contaminate seaming solvent joints. If slip or anti-fog concentrates are required, dosing is restricted to 1–2 wt% and dispersion is verified by low-magnification polarised light microscopy after cast sheet sampling. Seaming is performed with tetrahydrofuran-based solvent cement or, where volatile organic compound restrictions apply, with scanning laser welders at 10–30 W continuous-wave power; seam strength must exceed 15 N/25 mm before sleeving. Storage stability is a known constraint: rolls of high-shrink 4043D film should be held below 30 °C and 50% RH, because storage above 40 °C initiates slow crystallisation and reduces subsequent free shrink by as much as 20–30% relative to the as-produced value. Compliance for sleeve applications includes EU Regulation (EC) No 10/2011 for food-contact sleeves and FDA 21 CFR 175.300 for polymeric coatings where the shrunk sleeve functions as a coating in dry ambient conditions; print inks and seam solvents are evaluated under REACH Regulation (EC) No 1907/2006. Terminal products include full-body shrink sleeves for cold-fill beverage bottles, tamper-evident neck bands, and multi-pack collation shrink film.
Confectionery twist wrap produced from Ingeo 4043D is converted as a 20–25 µm biaxially oriented film with balanced tensile properties but deliberately low elastic recovery. The sheet is oriented at a machine-direction ratio of 2.0:1–2.5:1 and a transverse ratio of 4.0:1–5.0:1, with stretching-zone temperatures kept between 65 °C and 75 °C; the stenter is quenched below 40 °C after orientation and is not heat-set, so the oriented amorphous structure retains high deadfold. Ingeo 4043D is formulated with a controlled D-lactide level to suppress rapid spherulitic crystallisation during cast-sheet quenching, which allows the film to remain optically clear while still developing twist retention after orientation. Deadfold is assessed by winding a 150 mm × 15 mm specimen around a 5 mm diameter mandrel, holding for 10 s at 23 °C, releasing, and measuring the retained wrap angle; converter specifications are expressed as the minimum angle held without unwinding. The film is converted without migratory slip additives because twist wrap requires sufficient surface friction to stay closed on high-speed twist-wrapping machines running at 600–900 pieces/min. If antiblocking is necessary, synthetic silica is dosed at 0.2–0.5 wt% and the film is produced with a thickness variation below ±2% to prevent twist-tightening variation across the web. Compliance for confectionery contact follows EU Regulation (EC) No 10/2011 and the applicable FDA Food Contact Notification for PLA homopolymer in dry, low-fat sugar-based confectionery at ambient temperature. Terminal products include individual candy twists, lollipop wraps, chocolate coin wraps, and promotional confectionery wraps requiring optically clear reverse-printed graphics.
Metallized biaxially oriented Ingeo 4043D is produced from a 20–30 µm substrate that is corona-treated in-line to 42–46 dyn/cm and then wound with a controlled residual moisture level below 0.3% by weight to prevent outgassing in the vacuum chamber. The base film is loaded into a roll-to-roll metallizer evacuated to a pressure below 5 × 10⁻⁴ mbar; aluminium wire feed is set to deposit a coating of 30–60 nm, corresponding to optical density 2.0–3.0. Deposition uniformity is monitored by sheet resistance, with production targets between 1.5 ohm/sq and 3.0 ohm/sq. Metal adhesion is measured with a tape pull test per ASTM D3359, with removal below 5% of the coated area considered acceptable. Without metallisation, a 25 µm PLA film typically exhibits an oxygen transmission rate of approximately 500–600 cm³/m²·day at 23 °C/0% RH measured by ASTM F1927; after aluminium deposition, OTR falls to 5–20 cm³/m²·day under the same conditions, while water vapour transmission rate falls below 1 g/m²·day at 38 °C/90% RH measured by ASTM F1249. Formulation for metallizable grades removes migratory amide slip concentrates because surface bloom degrades metal adhesion; if antiblocking is required, nano-silica at 0.2–0.5 wt% is preferred. The metallized web is optionally top-coated with a protective lacquer at 1–2 g/m² before lamination or printing. Compliance for food-contact metallized structures follows EU Regulation (EC) No 10/2011 and the applicable FDA Food Contact Notification for the PLA layer, with the printed and laminated final structure assessed under 21 CFR 175.105 when laminating adhesives are used. Terminal products include oxygen-sensitive snack packaging, inner liners for dry foods, cosmetic sachets, and decorative gift wrap requiring a bright metallic finish on a renewable carbon substrate.
For pressure-sensitive adhesive tape backing, Ingeo 4043D film is converted at 25–40 µm thickness with an orientation ratio of 2.5:1–3.0:1 in the machine direction and 3.5:1–4.5:1 in the transverse direction, followed by heat-setting at 120–130 °C to keep shrinkage below 1% at 80 °C for 5 min. The film must be free of migratory slip additives because subsequent silicone release coating and acrylic adhesive lamination require stable surface energy; corona treatment is therefore raised to 46–50 dyn/cm immediately before coating. The film is coated on one surface with a solvent-free platinum-catalysed silicone release system at 0.5–1.0 g/m² and cured to a low release force; the reverse side receives a tacky acrylic adhesive at 20–35 g/m². Longitudinal thickness variation must remain below ±3% because caliper shifts cause adhesive coat weight control systems to oscillate and produce stripes in the finished roll. Tensile modulus after orientation is approximately 3.0–3.8 GPa measured by ISO 527-3, which supports high-speed slitting on razor-blade slitters at 300–500 m/min without necking. Dust extraction systems are required because the relatively stiff PLA fracture edge generates particulate contamination that can transfer to adhesive surfaces. Compliance includes ISO 9001:2015 for process traceability, REACH Regulation (EC) No 1907/2006 for substance registration, and RoHS Directive 2011/65/EU where electrical insulation tape end uses are specified. Terminal products include carton sealing tape, stationery tape, masking tape, and low-noise unwind adhesive tape for office dispensers.
Lidding film structures based on Ingeo 4043D are prepared as a 25–50 µm oriented base web that is printed and laminated or coated with a peelable sealant before die-punching to tray dimensions. The base film is heat-set at 120–130 °C so that after lamination it retains dimensional stability at 70 °C with shrink below 1.5%. The peelable seal system is selected from either an aqueous vinyl acetate-ethylene copolymer coating at 2–4 g/m² dry coat weight or a solventless polyurethane lamination adhesive with a peel-seal lacquer; seal initiation is typically 85–110 °C, and production sealing equipment operates at 130–160 °C for 0.5–1.5 s dwell time. Seal strength is measured according to ASTM F88, with target values of 4–8 N/15 mm for peelable lidding on PP or PLA trays; cohesive failure within the sealant layer rather than adhesive failure to the tray flange is required for consumer opening. Compliance for refrigerated food contact is verified under EU Regulation (EC) No 10/2011 using food simulant B for acidic wet foods or simulant A for aqueous produce, with overall migration below 10 mg/dm² per EN 1186-1; for the United States, the structure is subject to the applicable FDA Food Contact Notification for the PLA layer and FDA 21 CFR 175.105 for the laminating adhesive. The primary operational boundary is high-humidity refrigeration: PLA lidding film loses tensile stiffness when exposed to condensed moisture, so trays with high headspace moisture require anti-fog treatment at 1–2 wt% and a minimum base film thickness of 30 µm to prevent tenting over the seal. Terminal products include lidding for cold-fill fruit and salad trays, dry snack cups, and meal-kit compartments where peelable opening without scissors is a design requirement.
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Ingeo™ Biopolymer 4043D is a polylactide resin engineered specifically for biaxially oriented film extrusion and supplied as clear pellet feedstock. The grade is derived from dextrose obtained from annually renewable plant sources and polymerised through lactide ring-opening, producing a thermoplastic polyester with a specific gravity of 1.24 g/cm³ when tested to ASTM D792. The melt flow rate is 4.0 g/10 min under ASTM D1238 / ISO 1133-1:2022 at 210 °C with a 2.16 kg piston load. This melt-flow position is lower than many general-purpose PLA film extrusion grades, which is significant for melt strength during sequential or simultaneous biaxial stretching. Intended application fields include tenter-frame and double-bubble lines producing labels, twist-wrap films, lamination webs, and shrink-sleeve base films. The resin is not primarily sold as an unoriented cast film material; biaxial orientation is required to develop the property profile associated with the grade.
Typical physical property data for biaxially oriented 4043D film are summarised in Table 1. These values are dependent on draw ratio, heat-set dwell, and line configuration; the table should be read as supplier-published starting data rather than a universal specification.
| Property | Test method | Typical oriented film value |
|---|---|---|
| Specific gravity | ASTM D792 / ISO 1183 | 1.24 g/cm³ |
| Melt flow rate | ASTM D1238 / ISO 1133-1:2022 | 4.0 g/10 min at 210 °C, 2.16 kg |
| Glass transition temperature | ASTM D3417 | 55–60 °C |
| Crystalline melt peak | ASTM D3418 | 145–160 °C |
| Tensile strength at break, MD/TD | ASTM D882 | 100–120 MPa / 100–120 MPa |
| Tensile modulus, MD/TD | ASTM D882 | 3.0–3.6 GPa / 3.2–3.8 GPa |
| Elongation at break, MD/TD | ASTM D882 | 100–160% / 80–120% |
| Haze | ASTM D1003 | 2–5% |
| Gloss at 60° | ASTM D2457 | 85–95 |
Biaxial orientation of PLA is not a single-step web stretching operation. During melt extrusion, 4043D exhibits a melt flow rate of 4.0 g/10 min, but the more useful parameter in the longitudinal stretching gap is the transient extensional viscosity. A narrow molecular weight distribution limits the low-molecular-weight tail that would otherwise reduce die-lip melt tension and promote draw resonance in the cast sheet. The amorphous cast sheet is quenched to below 60 °C to freeze orientation and prevent premature spherulitic crystallisation. Subsequent reheat in the 70–80 °C range positions the polymer roughly 15–25 °C above the glass transition temperature of 55–60 °C, providing segmental mobility while retaining enough stiffness for controlled tensile orientation.
On commercial sequential tenter lines, edge tear at the clip points is influenced by temperature uniformity across the web. Production reports and equipment technical bulletins indicate that cast roll temperatures below 30 °C elevate quench stress and can generate transverse striations, while cast roll temperatures above 45 °C may cause blocking on draw rolls. The practical cast roll set point is therefore 25–40 °C with closed-loop control across the roll face held to ±1 °C. Because the glass transition of PLA is broad, uneven heating before machine-direction stretching produces visible bowing when the web enters the transverse stretch. Infrared heater zones are commonly tapered from approximately 80 °C at the sheet edges to 70 °C at the centre to compensate for edge cooling. Published radiative absorption data for 4043D film of varying thickness are limited; line-specific tuning is required.
Ingeo 4043D must be dried before melt processing. Hydrolytic degradation at melt temperatures above 190 °C proceeds rapidly when residual moisture exceeds 250 ppm. A desiccant dryer with a dew point of ≤ -40 °C and an inlet temperature of 80 °C for 4 h is the standard start-up condition. Hopper sizing should be based on residence time rather than temperature alone; a hopper of 100–150 kg/h throughput must provide full plug-flow exposure at the specified moisture level. Vacuum drying at 80 °C for 6–8 h may reduce moisture to a comparable level where desiccant capacity is marginal, but throughput may be reduced.
At the extruder, a single-screw configuration with an L/D ratio of 24:1 to 30:1 and a barrier feed section is common. Barrel profile is typically 180 °C in the feed zone, rising to 200–210 °C in the metering zone, with adapter and die set points at 200–220 °C. Melt temperature measured at the die should remain within 190–220 °C. Melt temperature above 240 °C is not recommended because lactide regeneration and yellowing increase; temperatures below 180 °C elevate melt pressure and intensify die lines. Screen packs using 60/100/60 mesh are common, but exact filtration must be adjusted for coextruded layers and coating performance. A rising melt-pressure trend at constant screw speed, or a die-pressure reading above 180 bar, indicates gel accumulation or degraded resin and should not be ignored.
| Processing variable | Start-up reference range |
|---|---|
| Desiccant dryer temperature | 80 °C |
| Desiccant dryer dew point | ≤ -40 °C |
| Drying residence time | 4 h |
| Maximum residual moisture at hopper throat | 250 ppm |
| Melt temperature at die | 190–220 °C |
| Cast roll temperature | 25–40 °C |
| Machine-direction preheat | 70–80 °C |
| Machine-direction stretch ratio | 2.5–3.5 |
| Transverse-direction preheat | 75–85 °C |
| Transverse-direction stretch ratio | 3.0–4.0 |
| Heat-set temperature | 120–140 °C |
| Heat-set dwell | 10–30 s |
The distinction between 4043D and general-purpose PLA film extrusion grades becomes most visible in orientation window breadth and heat stability. A general film grade with a higher melt flow index may extrude at lower head pressure, but it can generate a weaker melt curtain and less stable edge beads on high-speed tenter lines. The higher melt viscosity of 4043D improves draw resonance control during machine-direction stretching. After biaxial orientation, the film develops a tensile modulus of approximately 3.0–3.6 GPa in the machine direction and 3.2–3.8 GPa in the transverse direction when tested under ASTM D882. This stiffness is generated by strain-induced alignment, not by filler addition, and is substantially above that of unoriented amorphous PLA sheet.
The grade is selected where deadfold retention, gloss, and dimensional stability after heat-setting are controlling requirements. Heat-set temperature in the range 120–140 °C reduces free shrink and improves dimensional stability, but dwell beyond 30 s can embrittle edge regions. Differences from injection-moulding grades such as Ingeo 2003D are related to molecular architecture and additive package. Injection-moulding grades are not optimised for extensional strain hardening; their lower melt viscosity and solidification behaviour are intended for rapid mould filling and part ejection. Public datasheets for 4043D provide limited information on molecular weight distribution, z-average molecular weight, or D-isomer content; these data must be obtained from supplier technical service when critical to process modelling.
For barrier structures, 4043D frequently serves as a structural skin in coextruded or coated films. Oxygen transmission rate and water vapour transmission rate are not fixed by pellet properties alone; they vary with orientation state, layer thickness, heat-set history, and coating. Published data for barrier values of this specific configuration are limited. Testing should be performed on the finished structure under ASTM D3985 at 23 °C and 0% RH for oxygen, and under ASTM F1249 at 38 °C and 90% RH for water vapour. No universal transmission value should be assumed from the neat resin datasheet.
Compliance statements for Ingeo 4043D must be confirmed on the finished oriented film rather than on the pellet alone. Supplier regulatory documentation for food-contact use in the United States generally references 21 CFR 177.1500 or an effective Food Contact Notification, while European Union compliance is assessed under EU Regulation 10/2011 as amended. Finished structures must meet the overall migration limit of 10 mg/dm² when tested according to EN 1186, and specific migration limits for residual monomers, oligomers, and processing aids must be confirmed in the relevant food simulant. Printing inks, lamination adhesives, corona treatment, and recycled regrind content all alter the final migration profile. Compliance cannot be transferred directly from the base resin if downstream conversion introduces non-listed substances.
Operational boundaries include continuous-use temperature below 60 °C for non-annealed structures, because the glass transition temperature of 55–60 °C defines the onset of dimensional change under load. Pre-drying is mandatory at relative humidity above 60%, because pellet-surface moisture adsorption can occur within 2 h in uncontrolled storage. Basic fillers and certain amine-containing additives should be avoided in masterbatches because they can catalyse hydrolysis and molecular weight loss during melt processing; neutral or mildly acidic masterbatches are preferred. Processors should not interchange 4043D with unspecified PLA regrind without verifying melt flow rate, moisture content, and thermal history, because hydrolytically degraded regrind shifts the stretch window and increases gel formation in the tenter-frame web.