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PURASORB PLC 7015 B Medical Device Lactide-Caprolactone Copolymer

    • Product Name: PURASORB PLC 7015 B Medical Device Lactide-Caprolactone Copolymer
    • 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 405364
    Product Name PURASORB PLC 7015 B
    Chemical Name Poly(L-lactide-co-caprolactone)
    Cas Number 65408-67-5
    Monomer Composition 70 mol% L-lactide and 30 mol% caprolactone
    Monomer Ratio 70:30 (L-lactide:caprolactone)
    Grade Medical device grade
    Appearance White to off-white granules
    Form Granules
    Inherent Viscosity 1.5 dL/g nominal in chloroform at 25°C
    Glass Transition Temperature Approximately 15-25°C
    Crystallinity Amorphous
    Density Approximately 1.1-1.2 g/cm3 at 25°C
    Solubility Soluble in chloroform and dichloromethane; insoluble in water
    Biodegradability Biodegradable via hydrolysis
    Storage Conditions Store in a cool, dry place, protected from moisture and light
    Packaging Sealed aluminum foil bags under nitrogen
    Residual Monomer Less than 0.5%
    Water Content Less than 0.5%
    Ash Content Less than 0.1%
    Heavy Metals Less than 10 ppm
    Application Medical devices, drug delivery, and tissue engineering

    As an accredited PURASORB PLC 7015 B Medical Device Lactide-Caprolactone Copolymer factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing PURASORB PLC 7015 B supplied in a sealed 1 kg moisture-barrier foil bag, labeled for medical device use.
    Container Loading (20′ FCL) 20′ FCL loaded with palletized PURASORB PLC 7015 B Medical Device Lactide-Caprolactone Copolymer, securely strapped, moisture-protected, shipped under controlled conditions.
    Shipping PURASORB PLC 7015 B is not classified as dangerous goods for transport. No UN number, hazard class, or packing group is assigned. Ship in sealed, nitrogen-purged foil bags at ambient temperature, protected from moisture, heat, and light. Keep containers closed; store refrigerated (2–8°C) upon receipt.
    Storage Store PURASORB PLC 7015 B in its original, tightly sealed packaging in a cool, dry, well-ventilated area, preferably refrigerated at 2–8°C. Protect from moisture, heat, light, and oxidizing agents. Allow containers to equilibrate to room temperature before opening to prevent condensation. Maintain clean, dry conditions to preserve copolymer quality and avoid contamination.
    Shelf Life PURASORB PLC 7015 B typically has a two-year shelf life when stored unopened, dry, and protected from moisture under supplier-recommended conditions.
    Application of PURASORB PLC 7015 B Medical Device Lactide-Caprolactone Copolymer

    Monofilament conversion of PURASORB PLC 7015 B on a single-screw extruder with L/D 24:1 uses a feed-zone temperature of 150°C, a compression-zone temperature of 165°C, a metering-zone temperature of 180°C, and a die temperature of 175°C. The pellets are pre-dried under vacuum at 120°C for 8 h to reduce moisture below 100 ppm, determined by coulometric Karl Fischer titration per ISO 15512:2019. The melt is filtered through a 40 µm screen pack to remove gel particles and black specks. Extruded monofilament is quenched in water at 20°C, then drawn at a ratio of 4:1 to 6:1 in a 55°C water bath. Draw ratios below 3:1 produce oriented fibers with tensile strength below 300 MPa, while draw ratios above 6:1 initiate surface fibrillation because the caprolactone-rich amorphous domains separate under high orientation. Annealing at 70°C for 12 h under nitrogen reduces free shrinkage to 2–3% when measured after 24 h in water at 37°C. Tensile and knot-pull testing follows ASTM D2256-21 for monofilament yarns; suture diameter and knot-pull acceptance limits are defined by the compendial monograph for synthetic absorbable sutures. Gamma sterilization at 25 kGy lowers inherent viscosity, and molecular weight retention below 85% of the pre-sterilization value is treated as a batch rejection criterion.

    What Residual ε-Caprolactone Level Is Acceptable in Emulsion-Derived Depot Microspheres?

    Solvent evaporation microencapsulation of PURASORB PLC 7015 B with a peptide or small molecule API uses dichloromethane as the dispersed phase and aqueous polyvinyl alcohol as the continuous phase. The copolymer is dissolved at 15% w/v in dichloromethane and emulsified with a rotor-stator at 10,000 rpm for 2 min. Solvent removal under stirring at 500 rpm and 25°C for 4 h produces microspheres with a volume mean diameter of 20–70 µm when measured by laser diffraction per ISO 13320:2020. Residual dichloromethane is limited to 600 ppm under ICH Q3C Option 1, determined by headspace gas chromatography per USP 467. Residual ε-caprolactone monomer is more problematic in depot forms because caprolactone migrates to the particle surface and can increase initial burst release; a ceiling of 0.5 wt% monomer by GC-FID is therefore applied in process validation. In vitro release in phosphate-buffered saline at 37°C and pH 7.4 is monitored by HPLC per USP 621 over 28 d. Release follows a biphasic profile with an initial diffusion phase governed by surface-associated drug and a second hydrolysis-controlled phase. Microsphere morphology is checked by scanning electron microscopy after lyophilization; surface pores larger than 10 µm correlate with burst release above 20% of payload. Published data for this specific PURASORB grade in microsphere form is limited; process development relies on in-house data and comparison with analogous lactide-caprolactone copolymers.

    Cast film fabrication for absorbable adhesion barrier stock uses a 10 wt% solution of the copolymer in chloroform, spread onto a PTFE-coated glass plate with a knife gap set to 500 µm. Solvent is removed at 25°C for 12 h, then under vacuum at 40°C for 24 h to reduce residual chloroform below 60 ppm per USP 467. The dry film is 50–200 µm thick. Because the caprolactone component lowers glass transition below ambient temperature, the film remains compliant and can be folded without fracture at 25°C. Tensile properties are measured by ISO 527-3:2018 with a test speed of 10 mm/min; elongation at break above 200% is typical for solvent-cast films. Suture pullout resistance is assessed with a 3-0 braided suture passed through the film 2 mm from the edge; failure load above 1.5 N is required in internal handling specifications. In vitro degradation is evaluated in phosphate-buffered saline at 37°C according to ASTM F1635-16, with mass loss recorded at 4, 13, 26, and 52 weeks. The degradation profile is suitable for a temporary barrier that maintains mechanical integrity for at least 8 weeks after implantation, then loses mass over 12–24 months. Cytotoxicity and implantation evaluations are conducted per ISO 10993-5:2009 and ISO 10993-6:2016.

    When β-TCP Loading Reaches 30 wt% in Compression-Molded Interference Screws

    Melt compounding of the copolymer with β-tricalcium phosphate is performed in a 25 mm twin-screw extruder with L/D 40:1, using a screw profile that includes two kneading blocks and a low-shear discharge zone. Dried polymer is fed at 5 kg/h with the barrel profile set from 150°C to 180°C. Addition of β-TCP at 15 wt% raises melt viscosity by approximately 25% relative to unfilled polymer at 180°C and 100 s⁻¹ in a capillary rheometer per ISO 11443:2021; at 30 wt% the viscosity increase is 60–80%, and fill pressures during subsequent compression molding rise accordingly. Above 30 wt% β-TCP, screw torque approaches the extruder’s upper limit and filler agglomeration creates surface defects on molded parts. The compounded strand is pelletized after air cooling and then compression molded at 170°C and 100 bar for 3 min. Molded screws are tested for flexural strength by ASTM D790-17 and implantation properties by ASTM F2502-17. The β-TCP phase buffers acidic hydrolytic degradation products, helping to maintain local pH above 6.5 in in vitro degradation medium at 37°C. The screws must be packaged in nitrogen-flushed foil pouches because moisture absorption above 0.3 wt% before molding generates voids at the polymer–filler interface.

    Injection molding of absorbable vascular clips on a 35 mm reciprocating screw machine with L/D 20:1 uses a clamped mold with a core temperature of 50°C to prevent sticking and gate blush. Pellets are dried under vacuum at 120°C for 6 h. The barrel profile is 150°C to 180°C, injection pressure is 800 bar, and hold pressure is 600 bar for 4 s. A cold runner with a tunnel gate 1.0 mm in diameter is used; the gate freezes at 3–5 s, after which the part is ejected. Because the copolymer has a glass transition below 25°C, the molded clips require no annealing and retain a ductile failure mode when tested at 37°C. Tensile strength and elongation are measured according to ASTM D638-14 on Type V specimens. Residual stress is evaluated by polarized light microscopy; unacceptable stress birefringence near the gate is controlled by increasing mold temperature from 25°C to 50°C. Sterilization by ethylene oxide at 37°C and 400 mg/L EO with a relative humidity of 60% is used where gamma-induced chain scission would reduce clip open retention force. The clip’s bioburden and sterility assurance level follow ISO 11135:2014 and ISO 11137-2:2013.

    Solvent-Cast Conduit Wall Anisotropy and Suture Pullout Resistance

    A 5% w/v solution of the copolymer in dichloromethane is applied by dip-coating onto a rotating braided poly(L-lactide-co-ε-caprolactone) tube with an outer diameter of 4 mm. Each dip is followed by drying at 25°C for 30 min; after 6 dips, the wall thickness reaches 180–250 µm. The final conduit is dried under vacuum at 40°C for 24 h and residual dichloromethane is tested by headspace GC per USP 467 with a limit of 600 ppm. The laminated wall exhibits anisotropic tensile behavior because the underlying braid contributes longitudinal stiffness while the cast copolymer provides hoop compliance. Suture pullout resistance is measured by passing a 7-0 monofilament suture through the wall 1 mm from the cut edge and pulling at 10 mm/min; a failure load of 0.8–1.5 N is typical. Kink resistance is evaluated by bending the conduit around mandrels with radii from 5 mm to 10 mm; luminal occlusion is measured by a calibrated tapered probe. In vitro degradation is run in phosphate-buffered saline at 37°C for 52 weeks per ASTM F1635-16, and the lattice retains burst strength above 50% of initial through 24 weeks. Published data for this specific solvent-cast conduit construction is limited; the values cited are design targets used in benchtop evaluations, not completed clinical performance data.

    Gamma radiation at 25 kGy changes inherent viscosity, not crystallinity

    Sterilization validation for a lactide-caprolactone device is performed under ISO 11137-2:2013 using the VDmax25 dose-substantiation method when bioburden is below 100 CFU/device. At a sterilizing dose of 25 kGy, the copolymer undergoes chain scission that is observable as a reduction in inherent viscosity of 10–25% when measured in chloroform at 25°C and 0.1 g/dL by ISO 1628-3:2018. The effect is dose-rate dependent; a slower dose rate above 2 kGy/h reduces free-radical recombination time and can produce a smaller viscosity loss than a fast cycle above 10 kGy/h. Crystallinity does not increase substantially in the lactide-rich amorphous domains after irradiation, as shown by differential scanning calorimetry at 10 K/min under nitrogen. The post-irradiation glass transition remains below body temperature, so the sterilized device retains flexibility. Oxidation during storage is limited by packaging in a nitrogen-filled foil pouch with oxygen below 0.5%; headspace oxygen is monitored by gas chromatography. The manufacturer’s specifications for post-sterilization molecular weight retention should be established on each lot because published data for this exact formulation under all irradiation dose rates is limited. A compliance matrix for finished device submission is summarized below.

    Test parameterMethod / standardCritical limit / condition
    Intrinsic viscosityISO 1628-3:2018Report in dL/g; lot-specific acceptance
    Residual monomers and oligomersISO 10993-13:2010 / GC-FIDResidual ε-caprolactone ≤ 0.5 wt%
    Residual solventsUSP 467 / ICH Q3CDichloromethane ≤ 600 ppm
    Moisture contentISO 15512:2019100 ppm before melt processing
    CytotoxicityISO 10993-5:2009Grade 0 or Grade 1
    Irritation and delayed-type hypersensitivityISO 10993-10:2010No erythema or edema above control
    ImplantationISO 10993-6:2016Minimal inflammatory response through 26 weeks
    Systemic toxicityISO 10993-11:2017No mortality or significant weight loss
    In vitro degradationASTM F1635-16Mass loss and molecular weight at 4, 13, 26, 52 weeks
    Sterilization doseISO 11137-2:2013VDmax25 or method 1 dose audit
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    Certification & Compliance
    More Introduction

    PURASORB PLC 7015 B is a resorbable medical-device copolymer of 70:30 mol% L-lactide and ε-caprolactone, supplied as cylindrical granules under the Corbion PURASORB designation. The grade carries a nominal inherent viscosity midpoint of 1.5 dL/g, with release documentation commonly specifying 1.3–1.7 dL/g measured as a 0.1% w/v chloroform solution at 25 °C. The B grade is intended for melt extrusion, injection molding, compression molding, solvent casting, and electrospinning of implantable devices. The caprolactone comonomer disrupts chain packing, lowering the glass transition into the 15–25 °C range and reducing crystallinity relative to poly(L-lactide). This yields a flexible matrix with a longer in-vitro mass-loss profile than 50:50 PLGA and a less brittle mechanical response than semicrystalline PLLA.

    What release specifications and analytical methods define the 7015 B grade?

    Release documentation for the 7015 B grade controls monomer ratio by 1H-NMR; the lactide content is typically held within 68–72 mol% to preserve the intended balance of stiffness and elongation. Residual monomer is determined by gas chromatography, with residual lactide limited to ≤0.5 wt% and residual ε-caprolactone limited to ≤1.0 wt%. Water content by Karl Fischer is limited to ≤0.5 wt% because hydrolytic chain scission in the melt is first-order in residual moisture. Tin catalyst residue is limited to ≤200 ppm by ICP-OES, and heavy metals are commonly reported below 10 ppm under USP <233> or an equivalent method. Loss on drying is limited to ≤0.5 wt%, and residual solvents are controlled to ICH Q3C limits. The polymer is manufactured under a quality system aligned with EN ISO 13485:2016, and supplier documentation is designed to support biological evaluation under ISO 10993-1:2018.

    Property Test method Specification
    L-lactide:ε-caprolactone ratio 1H-NMR 70:30 nominal; 68–72 mol% lactide
    Inherent viscosity 0.1% CHCl3, 25 °C, Ubbelohde 1.3–1.7 dL/g; midpoint 1.5 dL/g
    Residual lactide GC ≤0.5 wt%
    Residual ε-caprolactone GC ≤1.0 wt%
    Water content Karl Fischer ≤0.5 wt%
    Tin ICP-OES ≤200 ppm
    Loss on drying Gravimetric ≤0.5 wt%
    Residual solvents USP <467> / ICH Q3C Class 2/3 limits

    Before melt processing, dried pellets are blanketed under nitrogen and fed into a co-rotating twin-screw extruder. A 25 mm extruder with an L/D 40:1 configuration and a medium-shear screw design is operated at 120–180 °C from feed throat to die, with melt temperature limited to 190 °C and melt residence time below 5 min. Because the glass transition lies near ambient temperature, the feed zone is kept below 40 °C to prevent pellet sintering; downstream zones are set to 150–170 °C to maintain a stable viscosity plateau. Production-scale extrusion of the B grade requires dried moisture below 0.1 wt%. Vacuum drying at 25–35 °C for 24 h is used because higher temperatures cause granule blocking. Batch-to-batch viscosity drift is minimized when drying and melt-residence conditions are held constant; excursions above 190 °C or residence beyond 10 min cause chain randomization, lactide reformation, and molecular-weight loss. Primary and secondary amines should not be compounded into the melt because aminolysis accelerates ester cleavage.

    When solvent casting or electrospinning replaces melt extrusion

    For solvent-cast films, spray coatings, and electrospun fiber mats, PURASORB PLC 7015 B is dissolved in dichloromethane, chloroform, or acetone at 5–15 wt% solids depending on final thickness. The 1.5 dL/g midpoint gives a process viscosity that is lower than that of PLLA of similar inherent viscosity and higher than that of polycaprolactone homopolymer; no universal solvent-viscosity curve is applicable because solution viscosity depends strongly on solvent quality, water content, and temperature. Electrospinning from 18–22 wt% chloroform/acetone solutions on a 12–18 kV field at 0.3–0.8 mL/h flow rate yields continuous fiber mats; the low crystallinity minimizes gel particles. Residual solvent removal after casting is performed under vacuum at ≤35 °C until headspace gas chromatography shows solvent below 0.1 wt%. Solvent processing avoids the melt-residence constraints of extrusion, but it introduces a separate residual solvent risk that must be evaluated under ISO 10993-18:2020 for leachables.

    Thermal transition data and melt-rheology boundaries

    Differential scanning calorimetry of the 7015 B grade shows a glass transition between 15 °C and 25 °C; a sharp poly(L-lactide) melting endotherm is absent or weak unless extended annealing above 80 °C is applied. The copolymer is therefore processed as an amorphous or low-crystallinity thermoplastic, and dimensional stability during storage is limited by the 40–50 °C softening ceiling. Melt rheology at 160 °C is shear-thinning; dynamic oscillatory measurements by ISO 6721-10 give complex viscosity in the range of 102–103 Pa·s at angular frequency 1 rad/s, but the exact value is molecular-weight and moisture dependent. Published data for this specific grade under controlled moisture and shear history is limited; processing-capability studies should be repeated on lot-specific material. Injection molding cycle times below 60 s are preferred; prolonged hold-up beyond 10 min shifts molecular weight by chain randomization and lactide reformation.

    Because the 70:30 copolymer is nearly amorphous, the mechanical response after molding is less brittle than poly(L-lactide) and less stiff than glycolide-containing copolymers. Tensile specimens conditioned under ISO 527-1:2019 show yield stress in the 20–30 MPa range and elongation at break above 100% for fully dried, unsterilized injection-molded plaques. Flexural modulus measured by ISO 178:2019 is approximately 1.0–1.5 GPa. These values should not be used as design allowables for load-bearing devices because test speed, conditioning humidity, residual solvent, and sterilization method each shift the ductile-to-brittle transition. Moisture absorption above 0.5 wt% before molding reduces molecular weight and produces premature yellowing and surface defects on finished components.

    Degradation kinetics in aqueous media are not equivalent to PLGA

    Water uptake of the 70:30 L-lactide-caprolactone copolymer is lower than that of 50:50 PLGA. Phosphate-buffered saline immersion at 37 °C and pH 7.4 produces a hydrolytic induction period before mass loss. In-vitro studies on similar 70:30 L-lactide-ε-caprolactone compositions report measurable mass loss in compression-molded films after 12–16 weeks, with complete mass loss extending beyond 12 months, depending on specimen thickness and molecular weight. Molecular-weight loss is fastest in the first 8 weeks; polydispersity rises as random chain scission occurs preferentially at lactide units. Mechanical property decay is not linear with mass loss: tensile strength retention drops below 50% before 10% mass loss. This behavior differs from glycolide-rich PLGA, which exhibits faster autocatalytic core degradation and a more abrupt mass-loss event. Published data for this specific 7015 B grade is limited; degradation studies should be repeated on lot-specific material because sterilization and residual monomer affect early hydrolytic rate.

    Compared with PURASORB PL 38 poly(L-lactide), the 7015 B grade has lower tensile modulus, higher elongation, and less dimensional rigidity after molding. Compared with PURASORB PDLG 5004, a 50:50 PLGA, the 7015 B grade absorbs less water, degrades more slowly, and provides a more compliant matrix for flexible implantable devices. Compared with polycaprolactone homopolymer, the lactide-rich segments raise the glass transition and tensile strength while retaining enough flexibility for soft-tissue applications. The processing window is broader than that of high-lactide semicrystalline grades because the low crystallinity reduces premature solidification in molds, but the low glass transition makes ambient-temperature pellet handling more sensitive to blocking. The product therefore occupies an intermediate position in the resorbable polymer portfolio for devices requiring soft-tissue compliance, controlled solubility in chlorinated solvents, and a longer hydrolysis profile than glycolide-rich copolymers.

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