| HS Code | 557613 |
| Product Name | LACTEL L-PL (B6002-1) Biomedical Ester-Terminated PLA |
| Catalog Number | B6002-1 |
| Polymer Type | Poly(L-lactide) |
| Polymer Abbreviation | L-PL |
| Composition | 100% L-lactide |
| End Group | Ester-terminated |
| Grade | Biomedical |
| Form | Pellets |
| Color | White to off-white |
| Inherent Viscosity | 0.55-0.75 dL/g |
| Glass Transition Temperature | 60-65 °C |
| Melting Temperature | 175-180 °C |
| Density | 1.24 g/cm3 at 25 °C |
| Solubility | Soluble in chloroform, dichloromethane, tetrahydrofuran, dioxane |
| Storage Temperature | -20 °C |
| Biodegradability | Hydrolytically degradable |
| Sterilization Compatibility | Gamma irradiation and ethylene oxide |
| Cas Number | 26100-51-6 |
| Linear Formula | (C3H4O2)n |
As an accredited LACTEL L-PL (B6002-1) Biomedical Ester-Terminated PLA factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | Supplied as 1 g in a sealed amber glass bottle under inert atmosphere, with desiccant and tamper-evident cap. |
| Container Loading (20′ FCL) | 20′ FCL container loaded with LACTEL L-PL (B6002-1), a biomedical ester-terminated PLA chemical, securely palletized, braced, and sealed for transport. |
| Shipping | LACTEL L-PL (B6002-1) Biomedical Ester-Terminated PLA is not classified as dangerous goods for transport. No UN number, hazard class, or packing group is assigned. Ship at ambient temperature in tightly sealed containers, protected from moisture, heat, and contamination. Follow applicable carrier and institutional regulations. |
| Storage | Store LACTEL L-PL (B6002-1) Biomedical Ester-Terminated PLA frozen at -20°C in a tightly closed container under dry nitrogen or argon. Protect from moisture, heat, light, and oxygen. Keep in a desiccator; avoid repeated warming and ambient storage. Allow sealed containers to equilibrate to room temperature before opening to prevent condensation and hydrolysis. Use aseptic technique. Do not freeze-thaw unnecessarily. |
| Shelf Life | Shelf life is two years from date of manufacture when stored at -20°C in a dry, sealed, unopened container. |
In absorbable suture coating operations, LACTEL L-PL (B6002-1) functions as a low-friction, thickness-adjustable surface layer over braided poly(glycolide-co-L-lactide) cores. The coating solution is prepared at 2.0–3.5% w/v in a 70:30 v/v ethyl acetate/ethanol mixture, with maximum useful concentration limited to 4.5% w/v before viscosity produces non-uniform pick-up and flaking at strand interstices. The compliance boundary for the coated suture includes ISO 10993-5:2009 for elution-based cytotoxicity, ISO 10993-10:2010 for delayed-type sensitisation, ISO 10993-6:2016 for local tissue response after intramuscular implantation, and USP <85> for bacterial endotoxins; manufacturing release is performed under ISO 13485:2016 and absorbable suture monograph requirements of USP <871>. The downstream production line uses a multi-roll kiss-coater with line speed of 15–30 m/min, forced-air drying at 45–60 °C, annealing at 45–55 °C for 12–24 h, and winding tension held at 3–8 cN/tex. The ester terminus reduces acid-catalysed degradation at the coating interface compared with acid-terminated PLA. The terminal finished type is a synthetic absorbable coated multifilament suture in USP 2-0 to USP 6-0 gauges, supplied in double sterile barrier trays with attached needle.
For this grade, the central process conflict in orthopaedic interference screw manufacturing is the interaction between residual moisture, adiabatic shear heating, and lactide monomer regeneration above 195 °C. The formulation addition for osteoconductive devices is 100 mass% neat LACTEL L-PL or a compound containing 10–30 wt% β-tricalcium phosphate with median particle size d50 1.0–2.5 μm; filler loadings above 30 wt% produce uneven screw-thread fill and brittle fracture in torque-in tests. The polymer must be pre-dried at 75–80 °C under dry-air dew point not above -40 °C until residual moisture is ≤ 250 ppm by Karl Fischer titration; above 400 ppm, hydrolytic chain scission causes measurable melt-flow-rate shift under ISO 1133-1:2022 and lowers device initial bending strength. Compounding is performed on a co-rotating twin-screw extruder with 24:1 L/D, feed-zone temperature 170 °C, die temperature 185 °C, and specific mechanical energy not exceeding 0.25 kWh/kg. The re-dried pellets are injection moulded on a machine with 20:1 L/D screw, 2.0–2.5:1 compression ratio, clamp force 500–1,000 kN, injection speed 50–120 mm/s, hold pressure 600–1,000 bar, and mould temperature 25–40 °C. The terminal finished product is a cannulated bioresorbable interference screw with hexagonal drive bore used in anterior cruciate ligament and knee reconstruction. Compliance for the finished device follows ISO 10993-1:2018 biological evaluation, ISO 10993-5:2009 cytotoxicity, ISO 10993-6:2016 implantation, and ASTM F1635-16 degradation screening. Avoid melt compounding with primary or secondary amine-functional additives because amine-induced chain scission accelerates molecular-mass loss; if osteoconductive phosphate fillers are used, pre-dry the filler at 120 °C for 4 h to prevent moisture carry-over.
A solvent-extraction route using B6002-1 in the dispersed phase is limited by oil-phase viscosity and by partition of active pharmaceutical ingredient into the continuous phase; therefore the polymer-to-drug mass ratio is set between 10:1 and 25:1 for low-dose peptide or small-molecule depots, with oil-phase polymer concentration held at 5.0–10.0% w/v in dichloromethane or ethyl acetate. The continuous phase contains 0.5–2.0% w/v poly(vinyl alcohol) with 88% hydrolysis, and emulsification proceeds in a rotor-stator device at 5,000–15,000 rpm for 2–5 min under a jacketed vessel temperature of 10–15 °C to limit solvent evaporation. Solvent removal is carried out by transferring the emulsion into 2–5% isopropanol at 25–30 °C for 3–5 h, followed by filtration and lyophilization at -40 °C shelf temperature and 50–100 mTorr chamber pressure. Encapsulation efficiency above 80% is typically achievable only when the drug candidate has low water solubility; water-soluble actives partition into the continuous phase and require polymer addition increase to 25:1 or a co-solvent adjustment. The compliance burden for injectable microspheres includes USP <788> for subvisible particulate matter, USP <790> for visible particulates, USP <85> for bacterial endotoxins, ICH Q3C R8 for residual dichloromethane below 600 ppm, and ISO 10993-5:2009 for cytotoxicity of extractables. The terminal finished type is a lyophilized, sterile injectable microsphere cake for reconstitution with water for injection in a syringe. Because B6002-1 is ester-terminated, autocatalytic degradation kinetics are less aggressive than acid-terminated PLA grades; published data for this specific grade in drug depots is limited, but accelerated release testing is run under ASTM F1635-16 in pH 7.4 phosphate-buffered saline at 37 °C.
Production of resorbable tubular scaffolds from LACTEL L-PL (B6002-1) requires a dilute high-volatile solution to maintain fibre diameter below 1 μm; the spinning dope is prepared at 8–12% w/v in 70:30 v/v chloroform/N,N-dimethylformamide, with 0.05–0.2% w/v of a volatile quaternary ammonium salt added solely to control charge density and reduce bead defects. The solution is delivered through a 22 G blunt-tip needle at 0.8–1.5 mL/h, with spinneret-to-collector distance of 15–20 cm and applied voltage of 15–20 kV; a rotating mandrel at 500–1,000 rpm collects oriented fibres, and a low-humidity enclosure maintained at 30–40% RH prevents premature water-induced phase separation. The scaffold is then vacuum-dried at 35 °C for 24 h to remove residual chloroform below 60 ppm before packaging. Compliance shifts from acute cytotoxicity to implantation-relevant testing: ISO 10993-1:2018 biological evaluation includes ISO 10993-5:2009, ISO 10993-6:2016 for subcutaneous or nerve conduit implantation, ISO 10993-11:2017 for systemic toxicity, and ISO 10993-17:2023 for toxicological risk assessment of degradation products. The terminal finished type is a resorbable electrospun tubular nerve conduit with oriented lumen fibres and an outer random-fibre reinforcement layer, cut to 10–30 mm lengths with 2–4 mm internal diameter. The addition of neurotrophic growth factors is not carried out in the same spinning dope because high voltage and chlorinated solvent reduce bioactivity; secondary surface coating after fibre formation is used instead, but that step lies outside the base-polymer solution-state parameters.
Melt pressing removes chloroform residual constraints but narrows the thermoforming range to 160–180 °C, above which the ester-terminated polymer starts to form lactide-rich volatiles and below which pinholing persists. For dental barrier membrane production, B6002-1 is either solvent cast from a 5–8% w/v chloroform solution using a knife gap of 400–600 μm or melt pressed at 160–180 °C under 10–15 MPa for 2–4 min; the melt-pressed sheet is then quenched on a 20 °C stainless steel platen to minimize crystallinity and maintain flexural compliance. Formulation addition ratios for adjustable degradation include 100 mass% neat polymer or 5–10 wt% acetyl tributyl citrate as a biodegradable plasticizer; plasticizer addition above 10 wt% reduces tear strength below the threshold required for guided tissue regeneration and increases tack during packaging. The regulatory pathway for the terminal resorbable dental barrier membrane includes ISO 10993-5:2009 for gingival fibroblast cytotoxicity, ISO 10993-10:2010 for oral mucosal irritation, ISO 10993-13:2010 for degradation product identification, and ISO 10993-17:2023 for leachables toxicology; if the device is sterilized by gamma radiation at 25–40 kGy, post-sterilization molecular-mass loss must be quantified by intrinsic viscosity under ISO 1628-1. The terminal finished type is a single-use, gamma-sterile resorbable dental barrier membrane in 15 × 20 mm to 30 × 40 mm formats for guided bone or guided tissue regeneration. The melt-pressed route is incompatible with thermolabile drug additives; if a doxycycline-loaded membrane is required, solvent casting with lyoprotectant stabilization must be used instead.
Because B6002-1 carries ester chain ends rather than free acid groups, the autocatalytic hydrolysis rate in a solvent-exchange depot is reduced relative to carboxylic-acid-terminated PLA of equivalent molecular mass. In this configuration, the polymer is dissolved in N-methyl-2-pyrrolidone at 15–30 wt% to form a single-syringe in-situ forming depot; below 15 wt%, phase inversion in subcutaneous tissue is too rapid and produces fragmented precipitates, while above 30 wt%, the formulation exceeds 5,000 mPa·s and cannot be injected through a 21 G needle at 22 °C. The terminal finished type is a sterile syringable biodegradable depot that solidifies by solvent exchange after subcutaneous or intramuscular injection, releasing the active agent over a period determined by the polymer addition ratio and the depot shape. The production process requires mixing sterile polymer with sterile-filtered N-methyl-2-pyrrolidone in a dry nitrogen atmosphere at 25–30 °C for 12–24 h, filling into siliconized glass syringes under ISO 13485:2016, and terminal gamma sterilization at 25–40 kGy or aseptic processing where the gamma dose is incompatible with the peptide payload. The compliance matrix includes USP <788> for particulate matter, USP <785> for osmolality if pre-mixed with buffer, USP <85> for endotoxin, ISO 10993-5:2009 for extractable cytotoxicity, and ISO 10993-11:2017 for acute systemic toxicity. Published data specific to B6002-1 in in-situ forming depots is sparse, so incoming-material critical quality attributes include syringeability force below 50 N through a 21 G needle and rotational viscosity measured at 25 °C under ISO 2555:2018.
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LACTEL L-PL (B6002-1) is supplied as a biomedical ester-terminated poly(L-lactide) resin. The designation identifies an L-lactide homopolymer architecture in which the chain terminus is ester-capped rather than present as a free carboxylic acid. This chain-end modification reduces the initial concentration of terminal carboxyl groups available to catalyze hydrolytic degradation and can lower the apparent acidity of the polymer in drug-loaded matrices and implant coatings. The B6002-1 suffix functions as a product-code identifier within the L-PL series; it is not an intrinsic viscosity value, and numerical lot specifications must be read from the certificate of analysis. The material occupies a slow-resorbing segment of the absorbable polyester design space and is typically evaluated for implantable structural components, drug-eluting coatings, microspheres, fibers, and porous scaffolds where semicrystalline L-lactide repeat units, controlled chain-end chemistry, and extended degradation are process-critical. No claim of device-level regulatory clearance is conveyed by the raw material code alone.
The functional distinction of the B6002-1 grade resides at the polymer chain terminus. In acid-terminated PLLA, each terminal carboxyl group contributes to a local acidic microclimate that accelerates ester cleavage through autocatalysis. The ester-capped architecture replaces the terminal carboxylic acid with a non-acidic ester function, reducing the initial acid number and altering the early-stage hydrolysis profile. Published data on comparable medical-grade PLLA have associated ester capping with reduced early molecular weight loss under humid storage and lower carboxylic acid content in extracted matrix material. However, ester termination does not eliminate hydrolytic degradation; water diffuses through the amorphous regions and cleaves backbone ester linkages regardless of end-group chemistry. The principal difference is the suppression of the autocatalytic contribution, not the removal of hydrolysis. This makes B6002-1 relevant for matrices carrying acid-sensitive active pharmaceutical ingredients or devices where delayed onset of mass loss is specified. Final degradation behavior must be evaluated in the intended geometry because autocatalysis is also influenced by part thickness and diffusion path length. The ester end-group influences chain-end mobility, solution acidity, and degradation-induced chain scission, but it does not fundamentally change the semicrystalline character of the L-lactide repeat unit.
Specification limits for the B6002-1 code are not standalone values; they are read against the lot-specific certificate of analysis and the internal release criteria of the converting facility. Typical parameters recorded for biomedical PLA resins include inherent viscosity in chloroform at 25 °C at a concentration of 0.1 g/dL, residual lactide monomer by gas chromatography, residual solvent by headspace gas chromatography, tin catalyst residue by inductively coupled plasma mass spectrometry, and molecular weight distribution by gel permeation chromatography. The polymer is usually characterized by a glass transition temperature of 55–65 °C and, after annealing, a melting endotherm of 170–180 °C for semicrystalline PLLA, as determined by differential scanning calorimetry per ISO 11357-2:2020. Published multi-lot data for this exact B6002-1 configuration is limited; manufacturers evaluating the material should not substitute these general PLLA ranges for lot-specific acceptance criteria. Viscosity-average molecular weight and inherent viscosity remain the controlling indicators for a given application. An ester-terminated chain with equivalent inherent viscosity will not automatically exhibit the same melt strength or film-forming behavior as an acid-capped analogue because terminal group identity affects chain-session rates during processing and storage. Lot-to-lot variability in inherent viscosity can alter dissolution time, melt viscosity, and fiber draw; users should establish internal control limits against qualified reference lots. Residual monomer content is particularly relevant in biomedical processing because free lactide can migrate in the final device and contribute to extractables. The grade is typically supplied in sealed, moisture-barrier packaging, and the packaging condition is part of the release specification rather than a secondary recommendation.
Before any melt-processing campaign, moisture removal is the controlling variable. The resin must be dried below a moisture threshold typically specified at 0.025 wt% (250 ppm) to avoid hydrolytic molecular weight loss during extrusion or injection molding. Vacuum drying at 80 °C for 12 h or desiccant drying to a dew point of -40 °C is representative of industrial practice for high-purity PLA, but the B6002-1 lot-specific drying profile should be confirmed. Melt processing of ester-terminated PLLA has been reported on co-rotating twin-screw extruders with length-to-diameter ratios of 25:1 and 40:1, using barrel profiles between 180 °C and 210 °C. When barrel set points exceed 220 °C, residence times above 8 min are associated with measurable molecular weight reduction in PLLA; published data for this specific B6002-1 configuration is limited. Injection molding has been performed with barrel profiles from 170 °C to 200 °C and mold temperatures either below 30 °C for amorphous parts or 100–120 °C for semicrystalline parts requiring in-mold crystallization. Clamp force is set by projected area and runner geometry rather than by polymer grade; for thin-wall components, packing pressure and hold time are the primary grade-dependent parameters. The ester end-cap does not remove the need for moisture control, but it can reduce the severity of viscosity loss when trace moisture is present by limiting terminal carboxyl generation. Residence-time distribution in twin-screw compounding widens at low feed rates and high screw speeds, producing a high-molecular-weight tail and premature degradation of the low-molecular-weight fraction. The B6002-1 chain-end structure does not eliminate this effect, and screw configuration should therefore be matched to the shear sensitivity of the grade.
Solvent-based fabrication routes for B6002-1 are generally bounded by solvent purity, solution concentration, and residual water content rather than by a single universal solubility limit. The resin is dissolved in chlorinated solvents such as dichloromethane or chloroform, with solution concentrations typically between 1 wt% and 10 wt% depending on target viscosity and coating or spinning geometry. Because ester-terminated PLLA has fewer free acid end-groups, the solution may show lower initial acidity during long residence times; however, solvent selection and water content remain critical because dissolved water can still initiate backbone hydrolysis. Filtration through 0.2 µm or 0.45 µm membrane filters is common before coating or electrospinning to remove gel particles and environmental contaminants. For microsphere encapsulation, solvent evaporation or extraction routes using dichloromethane and an aqueous continuous phase require pH adjustment of the aqueous phase; the reduced acid end-group concentration in B6002-1 may narrow the pH shift during hardening when compared with acid-terminated PLLA. Final residual solvent must meet the applicable pharmacopoeial or regulatory limit, such as ICH Q3C residual solvent classes, with the specific limit depending on the solvent and the intended patient exposure. Published data for the B6002-1 configuration in each solvent system is limited, so feasibility trials should include viscosity, cloud point, and residual solvent measurements. In drug-eluting coatings, migration kinetics in the polymer matrix are influenced by free volume, crystallinity, and chain-end polarity; the ester-capped terminus reduces one source of ionic interaction with basic drug substances, but final release behavior must be confirmed by in vitro dissolution testing.
Compared with a 50:50 PLGA copolymer of equivalent molecular weight, the L-PL repeat unit lacks the glycolide methylene group that increases hydrophilicity and accelerates degradation. The B6002-1 ester-terminated PLLA therefore exhibits slower water uptake, lower copolymer hydrophilicity, and longer in vivo mass loss profiles. High-molecular-weight PLLA devices may retain mass for more than 12 months depending on geometry and implantation site, whereas 50:50 PLGA typically degrades over weeks to months. The semicrystalline L-lactide homopolymer also provides higher tensile modulus after orientation than amorphous DL-lactide or PLGA; however, the crystalline regions of PLLA are less permeable to water and can produce heterogeneous degradation with a hollow core in thick implants. In contrast, acid-terminated PLLA of the same stereoregularity may degrade faster in the early phase because terminal carboxyl groups concentrate in the amorphous phase and increase local chain scission. The ester-terminated architecture therefore shifts the design space toward applications requiring slower and more predictable initial degradation, lower extractable acidity, or compatibility with acid-labile compounds. It is not a substitute for PLGA in fast-resorbing drug delivery systems, nor is it an amorphous DL-lactide grade for low-temperature elastic matrices. Each application must be matched by molecular weight, inherent viscosity, and end-group functionality rather than by polymer family alone.
| Architectural variable | B6002-1 ester-terminated PLLA | Acid-terminated PLLA | 50:50 PLGA |
|---|---|---|---|
| Terminal functionality | Ester-capped | Carboxylic acid | Carboxylic acid or ester |
| Initial acid content | Lower | Higher | Higher |
| Autocatalytic hydrolysis contribution | Suppressed | Present | Present |
| Morphology after annealing | Semicrystalline | Semicrystalline | Amorphous |
| Water uptake compared with glycolide-containing copolymer | Lower | Lower | Higher |
| Typical degradation window in porous or thin matrices | Often >12 months for high-molecular-weight grades | Shorter than ester-capped analogue | Weeks to months depending on ratio |
Storage stability of ester-terminated PLLA is governed by the same hydrolytic sensitivity as other aliphatic polyesters, but the reduced terminal acid content can extend dry-state shelf life when packaging remains sealed. The resin should be stored in a cool, dry environment and kept in moisture-barrier packaging until use. Once the primary container is opened, the material should be transferred to a dry environment or re-dried according to the processor’s qualified procedure. Contact with amine-based additives or strongly alkaline buffer systems may accelerate chain scission and should be avoided unless compatibility has been demonstrated in the final device matrix. For implantable applications, raw material storage conditions should be captured in the device master record because moisture history before processing can affect molecular weight and final degradation kinetics. The ester-capped terminus does not confer unlimited stability; it reduces one degradation accelerator but does not remove the need for controlled handling.
Biomedical evaluation of the B6002-1 grade is not a single checklist; it requires chemical characterization, degradation product analysis, and biological evaluation under a risk-based approach. The polymer can be screened for cytotoxicity per ISO 10993-5:2009 and for degradation products per ISO 10993-13:2010. The final device must be evaluated according to ISO 10993-1:2018, using the device-specific biological endpoints identified in the risk assessment. For implantable applications, tests for sensitization, irritation, systemic toxicity, implantation, and genotoxicity may be warranted depending on tissue-contact duration and patient population. The ester-terminated architecture may change the degradation product profile by reducing acidic oligomer release in early stages; however, the bulk degradation pathway still yields lactic acid as the ultimate degradation product. Therefore, the grade should not be considered inherently compliant with any specific device standard. Resin-level certification may include biocompatibility data for the raw material, but final sterilization, processing aids, packaging, and device geometry can alter the biological response. Sterilization by ethylene oxide or gamma irradiation may introduce changes in molecular weight and acid content; published data for the B6002-1 configuration is limited, so dose-setting with bioburden and post-irradiation viscosity testing is required. No claim of FDA device clearance or CE marking is conveyed by the raw material designation alone. Final device validation under ISO 13485:2016 and applicable regulatory requirements remains the responsibility of the finished-device manufacturer.