Products

PURASORB PLG 1017 Medical Device Lactide-Glycolide Copolymer

    • Product Name: PURASORB PLG 1017 Medical Device Lactide-Glycolide Copolymer
    • Factroy Site: Yudu County, Ganzhou, Jiangxi, China
    • Price Inquiry: admin@ascent-chem.com
    • Manufacturer: Ascent Petrochem Holdings Co., Limited
    • CONTACT NOW
    Specifications
    HS Code 928092
    Productname PURASORB PLG 1017 Medical Device Lactide-Glycolide Copolymer
    Chemicalname Poly(L-lactide-co-glycolide) 10:90
    Synonym PLG 1017
    Casnumber 26780-50-7
    Monomerratio 10:90 L-lactide:glycolide
    Polymertype Random copolymer
    Inherentviscosity 1.7 dL/g (0.5% in HFIP at 25°C)
    Appearance White to off-white powder/granules
    Form Powder/granules
    Color White to off-white
    Odor Odorless
    Solubility Soluble in hexafluoroisopropanol; insoluble in water
    Glasstransitiontemperature Approx. 35–40°C
    Meltingpoint Approx. 200–205°C (semicrystalline)
    Degradationmechanism Hydrolytic degradation
    Degradationproducts Lactic acid and glycolic acid
    Biocompatibility Biocompatible and bioresorbable
    Sterilizationmethods Gamma irradiation or ethylene oxide
    Storageconditions Store at 2–8°C, protected from moisture and light
    Shelflife 2 years when stored properly
    Residualmonomer ≤0.5%
    Watercontent ≤0.5%
    Heavymetals ≤10 ppm
    Ashcontent ≤0.1%
    Regulatorygrade Medical device grade; produced under ISO 13485
    Applications Medical devices, sutures, drug delivery, implants
    Manufacturer Corbion

    As an accredited PURASORB PLG 1017 Medical Device Lactide-Glycolide Copolymer factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing PURASORB PLG 1017 packaged in a 1 kg nitrogen-flushed foil pouch with desiccant, inside a sealed fiber drum.
    Container Loading (20′ FCL) 20′ FCL loaded with PURASORB PLG 1017 medical-grade lactide-glycolide copolymer in sealed drums, palletized, dry, secured, labeled for compliant shipment.
    Shipping PURASORB PLG 1017 is shipped in sealed, moisture-barrier foil packaging, typically under nitrogen, at ambient temperature. It is not regulated as dangerous goods for transport. Protect shipments from heat, light, and moisture; upon receipt, store refrigerated or frozen per supplier instructions.
    Storage Store PURASORB PLG 1017 in a tightly closed container in a cool, dry, well-ventilated place, protected from moisture, light, and heat. Keep away from oxidizing agents. Refrigerated storage (2–8°C) is recommended, or follow supplier specifications. Allow containers to equilibrate to room temperature before opening to prevent condensation and hydrolysis. Use desiccant; avoid prolonged air exposure.
    Shelf Life Shelf life is typically 2 years when stored unopened at 2–8°C, protected from moisture and light.
    Application of PURASORB PLG 1017 Medical Device Lactide-Glycolide Copolymer

    PURASORB PLG 1017 is an acid-terminated poly(L-lactide-co-glycolide) 10:90 copolymer with a midpoint inherent viscosity of approximately 0.17 dL/g measured in chloroform at 25°C. The 10:90 L-lactide:glycolide molar ratio places the material in the fast-degrading segment of the PLGA family, with bulk erosion dominated by ester bond hydrolysis and autocatalytic acceleration from acidic degradation products. The acid-terminated architecture reduces molecular weight distribution tailing and improves solubility in dichloromethane, chloroform, tetrahydrofuran, N-methyl-2-pyrrolidone, dimethyl sulfoxide, acetonitrile, 1,4-dioxane, and ethyl acetate, while water and primary alcohols are nonsolvents. The low inherent viscosity reduces solution viscosity at high polymer loading but limits melt strength, making the grade unsuitable for load-bearing extruded implants unless blended with higher-lactide or higher-molecular-weight PLGA grades. The following application tracks cover six medical device downstream segments in which PLG 1017 is used as a principal matrix, a dissolution-rate modifier, or a carrier polymer.

    Table 1. Compliance standards matrix for PLG 1017 downstream application tracks
    Application trackBiological evaluationChemical/safetyManufacturing/quality
    Long-acting injectable microspheresISO 10993-6; USP <85>ICH Q3C(R8); ISO 10993-18ISO 13485:2016; USP <788>
    Drug-eluting stent coatingsISO 10993-4; ISO 10993-5; ISO 10993-6; ISO 10993-11ISO 10993-18ISO 25539-2:2020; USP <788>
    In-situ forming injectable depotsISO 10993-6; ISO 10993-11ICH Q3C(R8); USP <790>USP <787>; ISO 13485:2016
    Transdermal microneedle arraysISO 10993-5; ISO 10993-10ISO 10993-18ISO 13485:2016; ISO 14644-1
    Adhesion barrier filmsISO 10993-5; ISO 10993-6; ISO 10993-10ISO 10993-7; ISO 10993-18ASTM F2902-16; ISO 13485:2016
    Dental GTR membranesISO 10993-1:2018; ISO 10993-5; ISO 10993-6ISO 10993-18ISO 22803:2004; ISO 13485:2016

    Long-acting injectable microsphere systems represent the highest-volume downstream application for low inherent viscosity acid-terminated 10:90 PLGA grades. In a water-in-oil-in-water double-emulsion process, PLG 1017 is dissolved in dichloromethane at 5–18% w/v, while the active pharmaceutical ingredient is either co-dissolved in the organic phase or introduced as an aqueous internal phase at a drug-to-polymer mass ratio from 1:4 to 1:20 depending on peptide or small-molecule solubility. The primary emulsion is generated under rotor-stator high-shear mixing at 3,000–10,000 rpm with a Silverson L4RT or IKA T25 digital ULTRA-TURRAX fitted with a fine-rotor workhead; the secondary emulsion is transferred into 0.5–2% w/v aqueous polyvinyl alcohol at 10–25°C. Solvent extraction and evaporation are performed in jacketed reactors with a controlled ramp from 15°C to 40°C over 4–8 h. Terminal microspheres are collected by sieving, washed with water for injection, and lyophilized at primary drying shelf temperatures of −35°C to −20°C and secondary drying at +15°C to +25°C. Process failure modes observed on production lines include batch-to-batch variability in primary emulsion viscosity when the aqueous drug phase exceeds 20% of the organic phase volume, leading to bimodal particle size distributions, and in-line laser diffraction analysis with a Malvern Mastersizer 3000 is used to control mean particle size and span. Compliance boundaries include Ph. Eur. 2.6.12 and 2.6.13 for microbial examination, USP <788> for particulate matter, USP <85> for bacterial endotoxins, ICH Q3C(R8) for residual dichloromethane and polyvinyl alcohol, ISO 10993-6 for local intramuscular implantation effects, and ISO 13485:2016 process controls. Finished product types include sterile microsphere vials for reconstitution, dual-chamber prefilled syringes with diluent compartments, and single-dose reconstitution kits for peptide-loaded depot injections where release typically spans 1–3 months depending on drug-polymer distribution and particle size.

    What Limits Drug-Eluting Stent Coating Uniformity on Cobalt-Chromium Struts?

    PLG 1017 is dissolved at 1–4% w/v in chloroform/tetrahydrofuran 90:10 v/v or acetone/ethyl acetate blends for drug-eluting stent coating. Antiproliferative active pharmaceutical ingredient is added at a drug-to-polymer mass ratio of 1:2 to 1:3, yielding a target drug content of 0.8–1.5 µg/mm² on 60–120 µm struts. Ultrasonic spray coating at 20–60 kHz with a Sono-Tek MediCoat or equivalent atomizer is performed while the stent rotates at 100–200 rpm and translates at 0.5–2 mm/s under laminar flow at 40–60°C. Critical defects observed at scale include webbing at sidewall radii, orange-peel topography, and polymer bridging across strut gaps; these are controlled by adjusting atomizer power, solution viscosity, and drying airflow. The low acid-terminated 10:90 grade has a relatively low glass transition temperature, typically near 35–45°C, so coatings may exhibit blocking if spooled at ambient temperatures above 30°C without secondary drying. Compliance standards include ISO 25539-2:2020 for cardiovascular stent systems, ISO 10993-4 hemocompatibility, ISO 10993-5 genotoxicity, ISO 10993-6 implantation, ISO 10993-11 systemic toxicity, USP <788> particulate matter, and ISO 10993-18 chemical characterization for residual tin catalyst or processing additives. Terminal finished products include coronary drug-eluting stent systems, peripheral below-the-knee stent systems, and coated stent subassemblies supplied to original equipment manufacturers. Published comparative release data for PLG 1017 in fully approved drug-eluting stent formulations is limited; development batches are routinely characterized by USP Apparatus 7 reciprocating holder dissolution and scanning electron microscopy for coating integrity.

    In-situ forming injectable depots prepared from PLG 1017 and N-methyl-2-pyrrolidone or dimethyl sulfoxide exploit the copolymer’s solubility in water-miscible aprotic solvents and its acid-terminated hydrophilic architecture. PLG 1017 is dissolved at 30–45% w/v in NMP with the active pharmaceutical ingredient co-dissolved or suspended at a final drug load of 3–15% w/w; the solution is filtered through 0.22 µm PVDF membranes and filled into single-use syringes under a dry nitrogen atmosphere with residual moisture kept below 0.1% w/w. Upon injection into aqueous physiological fluid or subcutaneous tissue, solvent exchange with water precipitates the PLGA matrix as a depot. Depot morphology is controlled by polymer concentration, solvent selection, injection volume, and tissue vascularity. Production equipment includes bubble-free vacuum mixing, nitrogen-blanketed filling lines, and terminal sterilization by gamma irradiation at 25–40 kGy where drug stability permits. Compliance includes ISO 10993-6 for local tissue response, ISO 10993-11 for systemic toxicity, USP <787> subvisible particulate matter for therapeutic protein injections, USP <790> visible particulates, and ICH Q3C(R8) residual solvent limits for NMP and DMSO. Terminal finished products include prefilled syringes with luer-lock adapters, cartridge-based depot injector systems, and kit configurations with separate diluent and polymer-solution cartridges. The main operational boundary is that hydrated PLG 1017 degrades rapidly; precompounded solution must be stored at −20°C to 5°C, and hold times above 24 h at 25°C increase bulk viscosity drift and acid shift.

    Transdermal Bioresorbable Microneedle Arrays Formed by Vacuum-Assisted Mold Filling

    PLG 1017 is used as a bioresorbable matrix in microneedle arrays because its low inherent viscosity permits filling of high-aspect-ratio polydimethylsiloxane molds without excessive bubble entrapment. The copolymer is dissolved at 10–25% w/v in acetonitrile, 1,4-dioxane, or dimethyl sulfoxide, with vaccine antigens, lidocaine hydrochloride, or cosmetic actives added at 1–20% w/w of total solids. The solution is cast onto PDMS molds with 500–850 µm pyramidal or conical cavities, subjected to vacuum-assisted filling at 0.2–0.5 bar for 5–15 min, and dried at 25–40°C for 12–24 h before demolding. Needle fracture during demolding is the primary failure mode because the 10:90 copolymer has low molecular weight and limited tensile strength; blending with 5–10 wt% poly(ethylene glycol) 400 or PLGA 50:50 improves flexibility but accelerates release. Compliance includes ISO 10993-5 for cytotoxicity, ISO 10993-10 for skin irritation and sensitization, ISO 10993-18 for leachables, and ISO 13485:2016 for manufacturing controls; terminal patch assembly is conducted in ISO 14644-1 Class 7 cleanrooms. Finished product types include dissolvable vaccine patches, transdermal lidocaine microneedle arrays, and cosmetic hyaluronic acid delivery patches with 100–400 needles per cm².

    Solvent-cast bioresorbable adhesion barrier films using PLG 1017 are produced by dissolving the copolymer at 8–15% w/v in chloroform or ethyl acetate, casting onto release liners, and drying in controlled laminar-air ovens at 30–50°C. Films with thicknesses of 20–80 µm are cut to 5×5 cm or 10×10 cm sheets and sterilized by ethylene oxide at 45–55°C. The acid-terminated 10:90 L:G composition yields a degradation window of approximately 4–8 weeks in mesothelial tissue, which is frequently too short for full peritoneal healing; therefore blend formulations with 20–40 wt% PLGA 50:50 or 75:25 grades are typical. Addition ratios for PLG 1017 in these blends range from 10–35 wt% of total polymer solids, balancing flexibility and hydrolysis rate. Residual ethylene oxide, ethylene glycol, and ethylene chlorohydrin are controlled per ISO 10993-7:2008/Amd1:2019 with maximum daily dose allowances specific to patient contact duration. Compliance includes ISO 10993-5 for cytotoxicity, ISO 10993-6 for local implantation, ISO 10993-10 for skin sensitization, and ASTM F2902-16 for absorbable polymeric implant assessment. Terminal finished products include absorbable anti-adhesion sheets, pericardial patches, and pelvic surgery barrier films. Films with PLG 1017 content above 30 wt% may exhibit brittle handling when dried below glass transition; thermal annealing at 35–45°C for 2–4 h reduces curl and static charge during die cutting.

    When Low Molar Mass PLGA 10:90 Modifies Guided Tissue Regeneration Membranes

    In dental guided tissue regeneration, PLG 1017 functions as a low-molecular-weight absorbable modifier in solvent-cast or electrospun barrier membranes where faster hydrolysis of the 10:90 fraction creates microporosity and promotes cell infiltration after the initial barrier period. PLG 1017 addition at 5–20% w/w of total polymer solids is blended with PLGA 75:25 or poly(ε-caprolactone) before electrospinning from 8–12% w/v solutions in hexafluoroisopropanol or chloroform/ethanol 80:20 v/v. Electrospinning is performed at 12–20 kV, a flow rate of 0.5–2.0 mL/h through 22G needles, and a collector distance of 10–18 cm, producing nanofibrous membranes with fiber diameters of 300–900 nm. A critical process conflict is that PLG 1017 reduces solution viscosity and may cause droplet formation or beading when added above 20 wt%; electrospinning trials therefore require repeated adjustment of flow rate and voltage. Compliance includes ISO 22803:2004 for dental barrier membranes, ISO 10993-1:2018 biological evaluation, ISO 10993-5 for cytotoxicity, ISO 10993-6 for implantation, and ISO 10993-18 for chemical characterization. Terminal finished products include resorbable dental guided tissue regeneration membranes, socket preservation barriers, and periodontal defect repair sheets supplied in sterile double-peel pouches.

    Free Quote

    Competitive PURASORB PLG 1017 Medical Device Lactide-Glycolide Copolymer prices that fit your budget—flexible terms and customized quotes for every order.

    For samples, pricing, or more information, please contact us at +8618136850665 or mail to admin@ascent-chem.com.

    We will respond to you as soon as possible.

    Tel: +8618136850665

    Email: admin@ascent-chem.com

    Inquiry

    Get Free Quote of Ascent Petrochem Holdings Co., Limited

    Flexible payment, competitive price, premium service - Inquire now!

    Certification & Compliance
    More Introduction

    Manufactured under an ISO 13485 quality system, PURASORB PLG 1017 Medical Device Lactide-Glycolide Copolymer is a bioresorbable poly(L-lactide-co-glycolide) grade supplied as off-white granules for melt-fabricated implantable devices. The resin is based on a 10:90 molar ratio of L-lactide to glycolide and carries an inherent viscosity mark of 1.7 dL/g. That composition distinguishes it from amorphous 50:50 D,L-lactide/glycolide grades used in drug delivery: the high glycolide content produces semicrystalline morphology after cooling, while the high molar mass contributes melt strength and oriented mechanical properties in sutures, clips, and orthopaedic fixation components. Batch certification documentation for the grade typically reports residual monomer, residual solvent, tin catalyst, water content, and elemental impurities against method-defined limits. The polymer is processed by injection moulding, extrusion, or compression moulding, but thermal and hydrolytic chain scission impose narrow processing boundaries.

    Specification controls and batch release limits

    Release limits for PURASORB PLG 1017 are method-defined and should be interpreted against the test standards shown below. Inherent viscosity is measured in chloroform at 25°C and 0.1 g/dL according to ISO 1628-1; the release band is commonly 1.601.80 dL/g, bracketing the 1.7 dL/g midpoint. Residual lactide and glycolide are quantified by gas chromatography with flame ionization detection, with a limit of ≤ 0.50% w/w. Residual solvent is controlled by headspace gas chromatography. Tin catalyst is reported after acid digestion and inductively coupled plasma mass spectrometry, with a limit of ≤ 50 ppm. Water content is determined by ISO 760 Karl Fischer titration. Elemental impurities are assessed against USP <232>/<233> or Ph. Eur. 2.4.20, with heavy metals limited to ≤ 10 ppm where included in the specification.

    Batch release parameters for PURASORB PLG 1017
    ParameterControl rangeTest method
    Inherent viscosity1.601.80 dL/gISO 1628-1, chloroform, c = 0.1 g/dL, 25°C
    Residual monomers0.50% w/wGC-FID
    Residual solvent0.50% w/wHeadspace GC
    Tin catalyst50 ppmICP-MS after acid digestion
    Water content0.50% w/wISO 760

    The specification values above are not substitutes for dry-before-melt limits. A water content of 0.10% w/w may be acceptable for incoming QC release but still too high for extrusion of high-glycolide copolymer. For melt processing, the polymer should be dried to ≤ 0.05% w/w to limit hydrolytic chain scission and maintain molecular weight.

    What melt-processing constraints apply to high-glycolide PLG 1017?

    Moisture control is the limiting variable. Glycolide-rich copolymers are hygroscopic, and open-hopper operation in relative humidity above 60% can produce rapid moisture uptake. Pre-drying under vacuum at 120°C for 4 h to 6 h is typical for high-glycolide PLG resins; drying above 140°C should be avoided because granule sintering and hopper bridging can occur. After drying, the material should be transferred to the feed throat under dry nitrogen or sealed hopper conditions. Residual moisture above 0.05% w/w measured by ISO 760 can generate melt viscosity loss, gas evolution, and reduced mechanical strength in finished parts.

    Melt compounding of high-glycolide PLG has been described on co-rotating twin-screw extruders with 25:1 to 40:1 L/D ratios and vented barrels. Barrel zones are typically profiled from 180°C to 215°C, with a die temperature not exceeding 230°C. Published data for PLG 1017-specific extrusion on production lines is limited; these settings must be confirmed by melt-pressure and torque monitoring. Thermal degradation accelerates when melt residence time exceeds 10 min at elevated temperature. Glycolide-rich chains undergo random chain scission and unzipping to monomer, producing a sharp rise in residual glycolide and a drop in melt pressure. The material should not be purged with oxygen-containing gases or held in the barrel during extended line stoppages.

    Injection moulding of thin-wall devices from PLG 1017 normally uses mould temperatures between 40°C and 80°C to balance crystallinity, part stiffness, and demoulding. Holding pressures in the 8001200 bar range are common for PLGA melt processing, but high-viscosity PLG 1017 may require higher pressure; the required clamp force should be calculated from the melt pressure and projected area of the part. Short-shot failures on cold-runner tools are addressed by raising manifold temperature within the thermal window rather than by increasing screw speed, which introduces shear heating and local degradation. Melt flow rate under ISO 1133-1 is not routinely reported for this high-molecular-weight grade because standard conditions may not produce meaningful flow; capillary rheometry is preferred for process-design data.

    The resin is incompatible with amine-based additives, alkaline cleaning agents, and high-pH buffers, which catalyze ester hydrolysis. It should not be compounded with oxidizing agents or heavy-metal salts that accelerate degradation. Cleaning of processing equipment should use neutral or mild acidic purging compounds, followed by complete purging of residual cleaner before re-introducing PLG 1017.

    When a semicrystalline 10:90 copolymer replaces amorphous 50:50 PDLG in an existing mould

    Replacement of an amorphous PLGA with PURASORB PLG 1017 is not a drop-in material change. The high glycolide content raises the melting transition above 200°C and narrows the processing window compared with amorphous PDLG grades. The comparative profile below summarizes the principal differences relevant to product development.

    Comparative profile of PURASORB PLG 1017 and selected PLGA grades
    GradeMonomer ratioInherent viscosity markMorphologyTypical application domain
    PURASORB PLG 101710:90 L-lactide/glycolide1.7 dL/gsemicrystallinesutures, clips, orthopaedic fixation
    PURASORB PDLG 501050:50 D,L-lactide/glycolide1.0 dL/gamorphousdrug delivery, microspheres
    PURASORB PDLG 750775:25 D,L-lactide/glycolide0.7 dL/gamorphouslonger-degrading drug delivery matrices

    PLG 1017 differs from PDLG 5010 and PDLG 7507 in three respects. First, it uses L-lactide rather than D,L-lactide, enabling crystallizable stereoregular segments. Second, the 90% glycolide content increases hydrolytic degradation rate and acid release per unit mass compared with 50:50 and 75:25 compositions. Third, the 1.7 dL/g viscosity mark is substantially higher than the 1.0 dL/g mark of PDLG 5010 and the 0.7 dL/g mark of PDLG 7507; this produces higher melt strength but also higher melt pressure. A mould fill simulation calibrated for PDLG 5010 will therefore underpredict pressure requirements when PLG 1017 is substituted.

    Devices made from PLG 1017 may retain mechanical strength during the first 23 weeks in aqueous environments, but published data for this specific configuration is limited; strength retention depends on initial molecular weight, crystallinity, sterilization, and implant geometry. The degradation rate after implantation is governed by water penetration, ester-bond hydrolysis, and the autocatalytic effect of accumulated glycolic acid oligomers, not by monomer ratio alone.

    In phosphate-buffered saline at 37°C, PLG 1017 undergoes bulk hydrolysis after water uptake. The high glycolide content produces glycolic acid-rich oligomers that lower local pH and accelerate degradation in the interior of thick devices. Mass loss follows strength loss, and the lag phase depends on initial inherent viscosity, residual monomer, and post-processing crystallinity. Device manufacturers should validate degradation under ISO 10993-13 and biological safety under ISO 10993-1, ISO 10993-5, ISO 10993-10, and ISO 10993-6 as applicable. Lactic acid and glycolic acid enter metabolic pathways, but the local acid depot from a 90% glycolide copolymer may exceed buffering capacity in poorly vascularized tissue sites. Biocompatibility therefore requires site-specific implantation data; it cannot be assumed from compositional information alone.

    Gamma irradiation at 2540 kGy reduces molecular weight and may accelerate subsequent hydrolytic degradation of PLG 1017. Validation according to ISO 11137 must include post-irradiation inherent viscosity and mechanical function, not simply sterility assurance level. Ethylene oxide sterilization according to ISO 11135 requires rigorous outgassing and residual ethylene oxide evaluation under ISO 10993-7 because glycolide-rich polyesters can retain sterilant residues. Bulk resin should be stored at −20°C to 5°C in sealed aluminium-lined bags with desiccant. After opening, the material should be resealed under dry nitrogen or dry air. Exposure to high-humidity cleanroom air should be limited to less than 24 h unless pre-drying is repeated immediately before melt processing.

    Batch-to-batch variation in residual monomer, tin content, and inherent viscosity has direct consequences for implant shelf life and process stability. A shift from 1.80 dL/g to 1.60 dL/g can alter melt pressure, fibre draw ratio, and orientation in extruded monofilament. Incoming QC should trend viscosity, moisture, and residual glycolide rather than accepting the release range as inert. Published data for PLG 1017 in multicavity tooling is limited; process capability studies should include cavity-to-cavity mass variation, weld-line strength, and ultrasonic welding or heat-sealing parameters for the intended finished device.

    Top