| HS Code | 444588 |
| Product Name | SOLPOL -1000B PBAT/Polylactic Acid Film Elastomeric Copolymer |
| Chemical Composition | PBAT/PLA copolymer |
| Appearance | Off-white to light yellow pellets |
| Form | Pellets |
| Density | 1.22-1.27 g/cm3 (typical) |
| Melt Flow Rate | 2-6 g/10 min at 190°C/2.16 kg (typical) |
| Melting Point | 110-130°C (typical) |
| Vicat Softening Point | 60-80°C (typical) |
| Tensile Strength | 15-25 MPa (typical) |
| Elongation At Break | 300-600% (typical) |
| Flexural Modulus | 100-350 MPa (typical) |
| Notched Izod Impact Strength | 5-15 kJ/m2 (typical) |
| Biodegradability | Biodegradable/compostable |
| Compostability | Compostable under industrial composting conditions |
| Processing Method | Blown film extrusion |
| Processing Temperature | 150-180°C (typical) |
| Moisture Content | ≤0.5% (typical) |
| Food Contact | Suitable for food contact applications subject to compliance |
As an accredited SOLPOL -1000B PBAT/Polylactic Acid Film Elastomeric Copolymer factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | SOLPOL -1000B PBAT/Polylactic Acid Film Elastomeric Copolymer packed in 25 kg polyethylene-lined paper bags, forty per pallet (1,000 kg). |
| Container Loading (20′ FCL) | 20′ FCL loading: SOLPOL-1000B PBAT/Polylactic Acid Film Elastomeric Copolymer, palletized, shrink-wrapped, evenly distributed, and secured for safe ocean transportation. |
| Shipping | SOLPOL -1000B PBAT/Polylactic Acid Film Elastomeric Copolymer is generally shipped as a non-hazardous, non-DG polymer in moisture-proof bags, drums, or cartons on pallets. Keep cool, dry, ventilated, away from sunlight and ignition sources. Protect from moisture and physical damage. Follow SDS, package markings, and applicable transport regulations. |
| Storage | Store in a cool, dry, well-ventilated area away from direct sunlight, heat, sparks, and open flames. Keep containers tightly closed and protect from moisture, humidity, and UV light. Maintain ambient temperature, preferably 5–30°C, in original packaging. Avoid contact with strong oxidizers, acids, and bases. Use first-in, first-out stock rotation and inspect containers regularly. Store separately from incompatible substances. |
| Shelf Life | Shelf life: typically 12–24 months when stored sealed in original packaging, cool, dry, protected from sunlight, moisture, and heat. |
In blown film conversion for compostable waste sacks and retail carrier bags, SOLPOL-1000B is metered at 20–30 wt% with a PBAT-rich base resin through a gravimetric dosing unit and processed on a single-screw extruder with 25:1–30:1 L/D, screw diameter 45–55 mm, and spiral mandrel die gap 1.2–1.8 mm. Pre-drying at 70–80 °C for 4 h in a desiccant dryer reduces residual moisture below 250 ppm; when ambient relative humidity exceeds 60%, closed conveying and hopper dryers are required to prevent hydrolysis-induced bubble rupture at gauge below 15 µm. Melt temperature at the die is maintained between 150–165 °C, melt pressure is held at 200–320 bar by screen pack selection, and screw speed is kept at 40–80 rpm to limit shear heating. Blow-up ratio is restricted to 2.5:1–3.5:1 because higher transverse orientation creates thickness variation above ±8% and reduces machine-direction Elmendorf tear. Film gauge is set at 12–35 µm according to sack duty. Tensile strength and elongation at break are measured by ASTM D882, dart impact by ASTM D1709 method A, and tear resistance by ASTM D1922. Heat seals are produced at 120–130 °C, dwell 0.5 s, and pressure 0.3 MPa, with seal strength determined by ASTM F88. Conformity with EN 13432 requires aerobic biodegradation of at least 90% within 180 days by ISO 14855-1, disintegration above 90% after 12 weeks by ISO 16929, and ecotoxicity testing by OECD 208; ASTM D6400 applies equivalent thresholds for U.S. industrial compost acceptance. In hot and dry bubble-cooling conditions, pinhole formation at 12 µm is a recorded field failure mode unless the air ring provides chilled air at 5–10 °C with a dew point below 15 °C. End products include compostable refuse sacks, produce rolls, and retail carrier bags with printability governed by surface treatment to 38–42 mN/m dyne level.
| Assessment | Standard | Requirement |
|---|---|---|
| Aerobic biodegradation | ISO 14855-1 / ASTM D5338 | ≥90% conversion within 180 days |
| Disintegration in compost | ISO 16929 | ≥90% after 12 weeks |
| Ecotoxicity | OECD 208 | No adverse effect on higher plant emergence and growth |
| Film tensile | ASTM D882 | Records tensile strength and elongation at break at 25 µm |
| Film impact | ASTM D1709 method A | Dart drop at 25 µm |
| Film tear | ASTM D1922 | Elmendorf tear at 25 µm |
Extrusion coating of kraft paperboard with a SOLPOL-1000B-modified PLA/PBAT layer is constrained by the thermal sensitivity of the polyester phase and the need to prevent PLA block crystallization during draw-down. The coated structure is produced on a 45–60 mm single-screw extruder fitted with a barrier screw and a coathanger die; melt temperature at the die is restricted to 155–175 °C, and the die is positioned 150–250 mm above the nip to limit neck-in to 15–20 mm. The compound is first dried to below 200 ppm moisture at 70 °C for 6 h. Chill roll temperature is controlled at 15–25 °C, nip pressure at 3–5 N/mm², and paperboard moisture at below 5% to prevent steam-generated voids. Melt flow rate determined by ISO 1133-1:2022 at 190 °C/2.16 kg is adjusted to 8–15 g/10 min using the elastomer content to improve fibre wetting; however, the higher MFR window simultaneously raises coating weight variation beyond 15–25 g/m². Adhesion strength is measured by TAPPI T 540 with a target not less than 1.0 N/15 mm; bond failure at the paperboard fibre layer, not at the interface, is required. Food-contact status under EU 10/2011 requires overall migration below 10 mg/dm² and specific migration control for lactic acid, adipic acid, 1,4-butanediol, and terephthalic acid. U.S. FDA status must be confirmed against the specific food-contact notification for the formulated coating layer. Compostability of coated board is assessed by ASTM D6868 and EN 13432, referencing ASTM D5338 or ISO 14855-1 for aerobic biodegradation. End products include hot beverage cups, compostable food trays, sandwich packs, and folding carton liners.
When melt-compounded in a co-rotating twin-screw extruder with 40:1 L/D and barrel profile 160–190 °C, SOLPOL-1000B at 10–20 wt% acts as an impact modifier for PLA-rich injection-moulding compounds. The compounded pellets are dried to below 250 ppm moisture before moulding. Injection moulding uses a barrel profile of 160–180–180–175 °C rear-to-nozzle, back pressure 5–10 bar, screw rotation 60–120 rpm, and mould temperature 80–100 °C to promote PLA crystal nucleation and reduce cycle time. A 12-cavity spoon tool with shot weight of 8.5 g requires clamp force of 800–1,200 kN; gates are cut to 0.8–1.2 mm thickness and 1.5–2.5 mm width to avoid shear-induced cleavage of the elastomer phase. Residence time is held below 10 min to prevent PLA molecular weight loss beyond 5% and lactide reformation at the nozzle. Notched Charpy impact by ISO 179-1/1eA increases from 2–3 kJ/m² to 5–8 kJ/m² at 15 wt% addition, while tensile modulus by ISO 527-2 decreases from 3,200 MPa to 2,200–2,500 MPa. Annealing at 80 °C for 30 min after ejection stabilises crystallinity and reduces post-mould warpage. Moisture uptake above 0.3% in storage above 60% RH is an operational boundary because hydrolytic embrittlement in the polyester phase accelerates. Disintegration under ISO 20200 at 58 °C must exceed 90% after 90 days for many biowaste collection schemes; EN 13432 conformity for compostable cutlery requires the full biodegradation and ecotoxicity sequence, while food-contact articles must be verified under EU 10/2011 and the applicable U.S. FDA food-contact notification for the formulated grade. End products include knives, forks, spoons, coffee stirrers, and hotel amenity articles.
Sealant-layer formulation for compostable flexible pouches incorporates SOLPOL-1000B at 15–25 wt% to depress seal initiation temperature without sacrificing interlayer adhesion in coextruded films. The sealant layer is coextruded at 10–20% of total thickness, with die melt temperature 155–170 °C on a three-layer blown or cast line. Seal initiation temperature is measured by ASTM F2029 at a threshold seal strength of 4.4 N/25.4 mm; PBAT-rich sealant layers containing the elastomer typically initiate at 95–110 °C, whereas unmodified PLA-rich sealants require 120–130 °C. Hot tack is measured by ASTM F1921 at dwell 0.5 s and pressure 0.275 MPa; recorded failure modes include stringing and seal lift-off at fill speeds above 60 pouches/min. Seal strength after cooling is measured by ASTM F88 at jaw separation rate 200–300 mm/min. The complete pouch structure must meet EN 13432 or ASTM D6400 compostability thresholds: ≥90% biodegradation by ISO 14855-1 within 180 days, ≥90% disintegration by ISO 16929, and ecotoxicity per OECD 208. Food-contact compliance under EU 10/2011 requires overall migration below 10 mg/dm² and specific migration control for lactic acid, adipic acid, 1,4-butanediol, and terephthalic acid; U.S. status requires confirmation under the applicable FDA food-contact notification. End products include dry-food stand-up pouches, fresh-produce zipper bags, and side-gusset pouches for coffee and tea.
| Requirement area | Reference | Test condition / limit |
|---|---|---|
| Biodegradation | ISO 14855-1 | ≥90% within 180 days |
| Disintegration | ISO 16929 | ≥90% after 12 weeks |
| Ecotoxicity | OECD 208 | Plant emergence and growth |
| Overall migration | EU 10/2011 | <10 mg/dm² |
| Seal strength | ASTM F88 | Measured at 200–300 mm/min |
| Hot tack | ASTM F1921 | Dwell 0.5 s, pressure 0.275 MPa |
Direct extrusion of PLA-based sheet containing 10–25 wt% SOLPOL-1000B is performed on a 35–50 mm single-screw flat-die line with melt temperature 165–180 °C, die gap 0.8–1.2 mm, and calender rolls set at 40–60 °C to keep initial crystallinity below 10%. Sheet thickness is controlled between 300–800 µm. Thermoforming is conducted on a plug-assisted pressure former at sheet surface temperature 90–110 °C measured by infrared pyrometry, with aluminium tooling at 20–30 °C and forming pressure 5–7 bar; the elastomeric phase reduces strain hardening, so unmodified PLA pressure settings of 3–4 bar are insufficient. Draw ratios above 1.5:1 are not recommended because corner wall thickness falls below 150 µm and orientation-induced stress concentrates at the plug contact. Sag resistance is assessed as deflection at 100 °C; sheet with crystallinity above 15% resists sag but limits edge trim regrind compatibility to 20–30%. Food-contact verification follows EU 10/2011 and applicable FDA food-contact notifications; compostability certification of the finished tray follows EN 13432 or ASTM D6400 with ISO 14855-1 and ISO 20200 disintegration tests. End products include produce punnets, clamshells, bakery trays, and cold-serve food trays.
Compostable agricultural mulch film containing SOLPOL-1000B is extruded as a 10–25 µm monolayer on monotube blown film lines with die melt temperature 150–165 °C; the finished roll is laid in widths up to 1.2 m by tractor-mounted equipment. EN 17033 governs this application and requires soil biodegradation of at least 90% within 24 months by ISO 17556 at 20–25 °C, plus ecotoxicity assessments under OECD 208 and OECD 222. Carbon black masterbatch at 2–4 wt% reduces solar transmittance and slows ester hydrolysis during the service window, but raises bulk density and reduces transparency. After 100 h of QUV exposure with UVA-340 lamps at 0.68 W/m², tensile strength retention above 50% is a common field target, although published data for this specific grade at submicron gauge is limited. Burial below 15 cm before crop harvest is an operational limitation because premature disintegration destroys weed suppression. End products include biodegradable mulch for tomato, strawberry, and vineyard applications where retrieval from soil is impractical.
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SOLPOL-1000B is supplied as a PBAT/PLA film elastomeric copolymer compound in pellet form for tubular blown-film and flat-die cast-film conversion. The grade designation identifies the polybutylene adipate terephthalate/polylactic acid base chemistry, not a single additive package. Principal converting applications are compostable refuse sacks, produce bags, agricultural mulch film, and sealant layers in multi-layer biodegradable films. The melt volume-flow rate for this compound class is typically 3–6 cm³/10 min at 190 °C/2.16 kg under ISO 1133-1:2022; the lot-specific certificate of analysis remains the controlling specification. The class-based engineering envelope in this document is anchored to ISO 1183-1:2019, ISO 527-3:2018, ISO 6383-2:1983, ISO 14855-1:2012, EN 13432:2000, and ASTM D6400-23. Where the COA is not available for a specific property, the ranges below are compounding envelopes for PBAT/PLA film elastomeric copolymers and must be verified before release.
Pre-drying is mandatory when ambient relative humidity exceeds 60% or when pellet surface moisture exceeds 400 ppm. A desiccant-bed dryer delivering a dew point of −40 °C at 65 °C for 4–6 h reduces moisture below 200 ppm before the feed throat. In a 75 mm co-rotating twin-screw compounder with L/D 44:1 and vacuum devolatilisation at −0.08 MPa, melt temperature should not exceed 210 °C, and residence time above 190 °C should remain below 5 min to limit hydrolytic chain scission and transesterification at the PBAT–PLA interface. On a blown-film line, the screw should use a medium-shear profile with three kneading blocks in the dispersion zone; specific energy input above 0.22 kWh/kg accelerates molecular weight loss and reduces tear resistance. Melt filtration with 100/80/100 mesh screen packs is recommended for film thinner than 25 µm to control gel-related pinholes. Pressure at the screen changer should remain below 12 MPa; pressures above 14 MPa force melt temperature past 210 °C and initiate local PLA degradation at the screw tip.
Unmodified extrusion-grade PLA typically exhibits a tensile modulus of 2.8–3.5 GPa and elongation at break of 2–6% under ISO 527-3:2018, providing stiffness but low puncture and tear tolerance. Unmodified PBAT film grades exhibit tensile modulus below 100 MPa, elongation above 600%, and high surface tack, which reduces bubble stability. SOLPOL-1000B is formulated to place room-temperature tensile modulus between 150 MPa and 400 MPa while retaining elongation above 300%. The elastomeric character arises from the PBAT-rich continuous phase, while the PLA-rich domains increase modulus and reduce blocking. The comparative envelope is shown below; it is not a certificate of analysis.
| Property | Test method | SOLPOL-1000B class envelope | PBAT homopolymer film | PLA homopolymer film |
|---|---|---|---|---|
| Density | ISO 1183-1:2019 | 1.22–1.28 g/cm³ | 1.20–1.24 g/cm³ | 1.24–1.26 g/cm³ |
| Tensile strength MD | ISO 527-3:2018 | 28–42 MPa | 18–30 MPa | 60–80 MPa |
| Elongation at break MD | ISO 527-3:2018 | 300–500% | >600% | 3–8% |
| Elmendorf tear | ISO 6383-2:1983 | 12–20 N | 10–18 N | 2–5 N |
| Seal initiation temperature | ASTM F88/F88M-21 | 85–105 °C | 70–90 °C | 110–130 °C |
Compared with PBAT/starch compounds, SOLPOL-1000B reduces melt viscosity fluctuation in humid conditions because the PLA-rich domain is less hygroscopic than gelatinised starch. However, the PLA fraction narrows the low-temperature heat-seal window. The product also differs from PLA homopolymer in having lower seal initiation temperature and lower Elmendorf tear transition temperature. In a multi-layer construction, SOLPOL-1000B is typically specified as the sealing layer over a PLA core, because the PBAT-rich surface provides cohesive seal failure below 100 °C without the optical haze of an all-PBAT skin.
The reintroduction of edge trim into flat-die cast film becomes a process control issue above 15 wt%. Hydrolytic chain scission during the first pass lowers intrinsic viscosity by 0.04–0.08 dL/g per pass when the regrind is not dried to <200 ppm moisture. The reduction in melt strength appears as an increase in neck-in from 8 mm to 16 mm on a 900 mm coat-hanger die at 180 kg/h output, leading to edge-thickness variability and lower unwind roll hardness. Regrind above 20 wt% also raises gel counts when flakes are ground with dull knives; local shear heating raises melt temperature to 215 °C and accelerates transesterification. Film converters should limit regrind to 20 wt% unless the extrusion line is fitted with closed-loop melt-pressure control and a 100 mesh screen pack. In cast-film operation, a 900 mm flat die with 0.7 mm lip gap and 20 mm air gap allows stress relaxation; chill roll temperature is held at 15–25 °C. Lower roll temperatures reduce blocking but increase PLA-phase crystallinity, raising haze above 5% per ASTM D1003-21.
Compostability testing for this product class follows ISO 14855-1:2012 at 58 °C under controlled aerobic composting conditions. A 25 µm film will typically exceed 90% theoretical carbon dioxide evolution after 90 days when the aromatic fraction in the PBAT segment remains below 55 mol% and the PLA fraction does not exceed 30 wt%. Disintegration and ecotoxicity are evaluated separately under EN 13432:2000 annexes, including the plant growth test. ASTM D6400-23 certification requires heavy-metal content below the limits in 40 CFR 503.13 and fluorine below 100 mg/kg. The product should not be described as marine biodegradable without ASTM D6691-17 or ISO 19679:2020 data; published data for this specific configuration is limited. For direct food-contact packaging, compliance must be confirmed under EU Regulation 10/2011 and applicable 21 CFR polyester sections, with overall migration not exceeding 10 mg/dm².
Table 2 summarises the verification matrix when a compostable or food-contact claim is made.
| Requirement | Test method / regulation | Typical control |
|---|---|---|
| Aerobic biodegradation | ISO 14855-1:2012 | >90% CO₂ evolution after 90 days at 58 °C |
| Disintegration | EN 13432:2000 Annex A | <10% residue on 2 mm sieve after 12 weeks |
| Heavy metals | ASTM D6400-23 / 40 CFR 503.13 | Below regulatory limits |
| Fluorine | ASTM D6400-23 | <100 mg/kg |
| Food contact overall migration | EU Regulation 10/2011 | 10 mg/dm² |
The PLA-rich phase sorbs water at a rate that is not linear with relative humidity. At 23 °C and 80% RH, unpelletised film reaches 0.8 wt% equilibrium moisture within 24 h, while dry pellets reach 0.3 wt% within 6 h. Hydrolysis proceeds by random ester cleavage; the rate constant at 190 °C increases by roughly one order of magnitude when moisture rises from 200 ppm to 800 ppm. Bulk bags should remain sealed and stored below 30 °C; any silo residence above 8 h in humid air requires a hopper dryer, not a hot-air oven alone. Resin exposed to ambient air for more than 4 h during a rainy shift should be returned to a dryer before extrusion, because the resulting viscosity drop causes die-lip haze and lower transverse-direction tear.
A blown film line using a 55 mm single-screw extruder, 250 mm die, 1.6 mm die gap, and a dual-lip air ring can produce 25–50 µm film at a blow-up ratio of 2.2:1 to 3.0:1. The frost line is maintained at 4–7 die diameters above the die face. At blow-up ratios below 2.0:1, transverse-direction tear drops by more than 25%; above 3.2:1, bubble instability increases because PBAT-rich melt has lower strain-hardening. Addition of 2 wt% silica antiblock with 4–6 µm median particle size reduces blocking at roll-stock temperatures above 35 °C but increases haze from 3% to 7% per ASTM D1003-21. Erucamide slip at 800–1,200 ppm migrates from the PBAT-rich phase within 72 h and should be validated by seal strength testing under ASTM F88/F88M-21 because slip migration lowers heat-seal strength by 10–20% on the sealed inner layer.
Differential scanning calorimetry under ISO 11357-3:2018 typically shows a PBAT-rich endotherm at 110–125 °C and a PLA-rich endotherm at 150–165 °C. The glass transition of the PLA-rich phase is near 55–60 °C. Contact-heat sealing of SOLPOL-1000B differs from PBAT because the PLA fraction raises the onset of cohesive failure without imparting PLA-like brittleness. A 30 µm monolayer film sealed at 93 °C and 0.5 MPa for 0.5 s typically gives a seal strength of 6–10 N/15 mm; raising the bar temperature to 110 °C creates squeeze-out and a seal strength loss of 15–25%. The practical upper seal-bar temperature is 105 °C for this class. In lamination, the amorphous PLA phase softens near 60 °C, so winding tension above 150 N/m at roll temperatures above 45 °C causes blocking and elongation set. The product is not recommended for hot-fill applications above 80 °C or for retort pouches unless protected by a high-temperature-core layer.
Film converters switching from PLA homopolymer to SOLPOL-1000B must reduce die temperatures from 210–230 °C to 190–195 °C and increase the air gap in cast film from 10 mm to 20 mm to allow stress relaxation and reduce edge weave. The same temperature reduction applies to flat-die feedblocks when the compound is used as a sealant skin over a PLA core; failure to reduce the die adapter setting creates viscosity mismatch and interfacial flow instability at the combining block.