Products

PURASORB PDLG 75016A Drug Delivery Acid-Terminated PLGA

    • Product Name: PURASORB PDLG 75016A Drug Delivery Acid-Terminated PLGA
    • Factroy Site: Yudu County, Ganzhou, Jiangxi, China
    • Price Inquiry: admin@ascent-chem.com
    • Manufacturer: Ascent Petrochem Holdings Co., Limited
    • CONTACT NOW
    Specifications
    HS Code 984990
    Productname PURASORB PDLG 75016A
    Manufacturer Corbion
    Chemicalname Poly(D,L-lactide-co-glycolide)
    Casnumber 26780-50-7
    Monomerratio 75:25 D,L-lactide:glycolide
    Polymertype Random copolymer
    Endgroup Acid-terminated (carboxylic acid)
    Inherentviscosity 0.16 dL/g
    Inherentviscositymethod Chloroform at 25 °C
    Molecularweight Approximately 10,000-15,000 Da (typical)
    Appearance White to off-white powder or granules
    Form Solid powder/granules
    Solubility Soluble in chloroform, dichloromethane, ethyl acetate, tetrahydrofuran; practically insoluble in water
    Glasstransitiontemperature Approximately 40-50 °C
    Thermalbehavior Amorphous; no sharp melting point
    Density Approximately 1.2 g/cm³
    Storageconditions Store at -20 °C, desiccated, protect from moisture
    Stability Moisture-sensitive; hydrolytically degradable
    Degradation Hydrolytic degradation; suitable for sustained release
    Application Drug delivery, microparticles, implants, sustained-release formulations
    Residualmonomercontent <0.5% (typical)
    Heavymetals <10 ppm (typical)
    Moisturecontent <0.5% (typical)
    Shelflife Typically 1-2 years when stored properly

    As an accredited PURASORB PDLG 75016A Drug Delivery Acid-Terminated PLGA factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing Supplied as 1 kg of PURASORB PDLG 75016A in a sealed, moisture-resistant amber container with desiccant and tamper-evident label.
    Container Loading (20′ FCL) PURASORB PDLG 75016A Drug Delivery Acid-Terminated PLGA loaded in 20′ FCL, palletized drums, securely stowed, sealed, shipped under controlled conditions.
    Shipping PURASORB PDLG 75016A is shipped as a non-hazardous, non-regulated polymer. It is packed in sealed, moisture-resistant containers and transported at ambient temperature, protected from light, heat, and humidity. No DOT/IATA/IMDG hazardous labels are required. Follow local regulations and store under recommended conditions.
    Storage Store PURASORB PDLG 75016A (acid-terminated PLGA) in a tightly sealed, moisture-proof container at 2–8°C, preferably under dry nitrogen or argon. Protect from light, heat, humidity, and oxidizing agents. Allow to equilibrate to room temperature before opening to prevent condensation. Avoid repeated temperature cycling, and store away from incompatible materials. Follow the SDS and local regulations.
    Shelf Life PURASORB PDLG 75016A shelf life: about 24 months sealed, dry, at 2–8°C, protected from moisture, heat, and light.
    Application of PURASORB PDLG 75016A Drug Delivery Acid-Terminated PLGA

    PURASORB PDLG 75016A is supplied as a dry, acid-terminated poly(D,L-lactide-co-glycolide) with a nominal 75:25 molar ratio and an inherent viscosity midpoint of 0.16 dL/g measured in chloroform at 25°C at 0.1 g/dL. The acid-terminated chain ends are quantified on the certificate of analysis by titration and are selected for long-acting injectable microspheres because they increase water uptake and accelerate bulk hydrolysis. A double-emulsion solvent-evaporation process is used for peptide-loaded depot formulations. The organic phase is prepared as 180–250 mg/mL polymer in dichloromethane. The inner aqueous phase contains the peptide at 5–10% w/v and may include trehalose or mannitol at 5–10% w/v as a lyoprotectant. Primary emulsification is performed with a Silverson L5M-A rotor-stator equipped with a square-hole high-shear screen at 6,000–10,000 rpm for 60–120 s. The primary water-in-oil emulsion droplet size is typically 1–5 µm by optical microscopy before transfer. The resulting emulsion is transferred into a continuous aqueous phase containing 0.5–2.0% w/v poly(vinyl alcohol) at 2–8°C, followed by secondary emulsification at 2,500–4,000 rpm. Solvent extraction and matrix hardening proceed in an aqueous bath at 15–25°C with a water-to-organic phase ratio of at least 10:1 v/v. Hardened microspheres are retained on a 20 μm stainless-steel sieve and collected below an 80 μm sieve, washed with water for injection, and lyophilized. A prolonged hold above 20°C beyond 8 h during hardening has been observed on production batches to cause surface pitting and a reduction in weight-average molecular mass of more than 10%, due to autocatalytic hydrolysis of the free carboxyl chain ends. Residual dichloromethane after vacuum drying at 25°C for 24 h is typically below 100 ppm, and the release limit is 600 ppm per ICH Q3C. Residual poly(vinyl alcohol) determined by size-exclusion chromatography is limited to 2.0% w/w. In-vitro release testing uses USP Apparatus 4 flow-through cells with phosphate-buffered saline pH 7.4 at 37°C. Representative batches of this acid-terminated grade show an initial 24 h release of ≤10% and a lag phase of 2–5 days before erosion-controlled release; this lag phase is shorter than the corresponding ester-terminated 75:25 grade under identical process conditions. The final microsphere suspension is assessed according to ISO 10993-1:2018 subacute implantation, USP <71> sterility, USP <85> bacterial endotoxins, and USP <788> particulate matter. Sterilization is by gamma irradiation at 25–40 kGy because steam autoclaving induces bulk polymer degradation before sterility can be achieved. Particle size is measured by laser diffraction per ISO 13320:2020, with a target volume mean diameter of 30–70 μm for intramuscular injection.

    Residual solvent limits relevant to PLGA microsphere manufacture under ICH Q3C Option 2
    SolventICH Q3C ClassConcentration limit in final drug product
    DichloromethaneClass 2600 ppm
    N-Methyl-2-pyrrolidoneClass 2530 ppm
    AcetoneClass 35000 ppm
    Ethyl acetateClass 35000 ppm

    When Acid-Terminated PLGA Is Dissolved in N-Methyl-2-Pyrrolidone for In Situ Depot Formation

    For subcutaneous in situ-forming depot systems, PURASORB PDLG 75016A is dissolved in N-methyl-2-pyrrolidone at 35–50% w/w under low-shear agitation for 12–24 h at 25°C. The drug substance is then incorporated by planetary mixing at 25 rpm for 16 h in a 2 L Teflon-coated anchor mixer. The resulting solution viscosity at 25°C is 3,000–6,000 mPa·s at 10 s⁻¹ as measured by cone-and-plate rheometry. The solution is filled into a 5 mL glass syringe with a 21-gauge needle. Upon injection into subcutaneous tissue, NMP exchanges with aqueous tissue fluid and the polymer precipitates to form a coherent depot. The higher carboxyl end-group density of this acid-terminated grade increases the initial water uptake of the precipitated matrix, and comparative release data show a shortening of the induction phase by 1–3 days relative to ester-terminated 75:25 PLGA at equivalent polymer concentration. Polymer concentrations below 30% w/w produce fragmented or particulate depots rather than a coherent implant, and burst release exceeds 30% of drug in the first 12 h. At NMP concentrations above 60% w/w, rapid solvent efflux collapses the outer skin and similarly increases burst release. The formulation is therefore maintained within 35–50% w/w polymer. Filtration through a 0.2 μm sterilizing-grade PTFE membrane is not feasible because of the high solution viscosity. Terminal gamma irradiation at 25 kGy is used, but irradiation of NMP solutions generates free radicals that reduce polymer molecular mass by an additional 5–8%; this reduction is accounted for in release design. Residual NMP in the implanted matrix falls below 1% w/w after 7 days in vivo based on published phase-inversion depot studies. The prefilled syringe system is assessed under USP <790> visible particulates, USP <788> subvisible particulate matter, ISO 11040-4 prefilled syringes, and ISO 10993-6:2016 implantation testing. The final product is a sterile, single-use prefilled subcutaneous depot.

    A solvent-displacement route for nanoparticle formation starts with PURASORB PDLG 75016A dissolved at 5–10 mg/mL in acetonitrile or acetone. The organic solution is introduced dropwise into an aqueous stabilizer phase containing 0.1–0.5% w/v poloxamer 188 or D-α-tocopheryl polyethylene glycol 1000 succinate under magnetic stirring at 400–800 rpm. Rapid diffusion of the water-miscible solvent produces nanoparticles with a z-average diameter of 90–180 nm and a polydispersity index of 0.08–0.15 measured by dynamic light scattering at 25°C according to ISO 22412:2017. At pH 7.4, the carboxylic acid end groups are ionized, giving the particle surface a zeta potential of −25 to −45 mV in 1 mM KCl. For ligand conjugation, the terminal carboxyl groups are reacted with 1-ethyl-3-(3-dimethylaminopropyl)carbodiimide and N-hydroxysuccinimide at a molar ratio of 5:1 to carboxyl sites in 0.1 M MES buffer at pH 5.5. Residual acetonitrile is removed by rotary evaporation at 30°C under 200 mbar and by nitrogen stripping; the drug product limit is 410 ppm under ICH Q3C. Unencapsulated drug is removed by tangential flow filtration on a 100 kDa regenerated cellulose membrane, yielding entrapment efficiency above 70% for hydrophobic actives. Lyophilization is performed with sucrose or trehalose at 5–10% w/w using a cycle with primary drying at −30°C shelf temperature and 50 mTorr chamber pressure for 24 h, followed by secondary drying at 20°C for 6 h. In-vitro release in phosphate-buffered saline pH 7.4 at 37°C shows a biphasic profile: 5–15% release in the first 24 h followed by sustained release over 10–20 days. The finished nanoparticle product is intended for intravenous or intratumoral administration and is tested according to ISO 10993-5:2009 cytotoxicity, USP <85> endotoxins, and USP <788> particulate matter. The process is limited to 2 L batch volumes in a flameproof enclosure because solvent flammability and adiabatic heating in high-shear homogenizers accelerate polyester degradation.

    How Does Hot-Melt Extrusion Avoid Solvent Residuals in Subdermal Rod Manufacture?

    On a vented twin-screw extruder with a 16 mm screw diameter and an L/D ratio of 25:1, PURASORB PDLG 75016A is melt-processed into subdermal rods. Pre-drying is performed at 30°C and 5 mbar for 24 h because acid-terminated PLGA undergoes autocatalytic hydrolysis if moisture exceeds 500 ppm. The feed zone is set at 60°C, the mixing zone at 75°C, and the die at 80°C; melt temperature at the die is 78–85°C. Screw speed is limited to 50–100 rpm to prevent shear heating, and motor torque remains below 4 N·m. Residence time is kept below 120 s. At die temperatures above 100°C, the weight-average molecular mass loss exceeds 10% in a single pass and the extrudate becomes discolored. The drug substance is pre-blended with a portion of the polymer and fed as a physical mixture; loadings of 10–25% w/w process without phase separation. At loadings above 30% w/w, the melt viscosity falls below 200 Pa·s and strand dimensional stability is lost. A circular die of 1.2 mm diameter produces rods that are cooled on a 4°C stainless-steel belt and cut to 5–10 mm lengths. The rods are annealed at 40°C for 12 h under dry nitrogen to reduce residual stress. The final subdermal rods are tested under ISO 13781:2017 for lactide-based surgical implant polymers, USP <905> uniformity of dosage units, and USP <788> particulate matter. In-vitro release in phosphate-buffered saline pH 7.4 at 37°C from a 1.2 mm rod with 20% w/w drug loading shows an initial 24 h release below 10% and near-zero-order release over 14–21 days. The principal production failure mode is strand breakage when feed continuity is interrupted; batch-to-batch inherent viscosity variation of ±0.02 dL/g can shift die pressure by 10–15% and requires feed-rate compensation of 5–10%.

    Solvent-cast bioresorbable films for periodontal pocket insertion are prepared by dissolving PURASORB PDLG 75016A at 10–15% w/w in acetone or ethyl acetate under rolling agitation at 25°C for 6–12 h. The solution is cast onto a silicone-coated polyester release liner using a knife-over-roll coater with a wet gap of 0.5–1.0 mm. Drying is performed in a two-zone forced-air oven: the first zone at 25°C for 30 min to limit skin formation, and the second zone at 35°C for 2–4 h under reduced pressure to drive off residual solvent. The dried film thickness is 150–300 μm. The acid-terminated grade yields films with higher water permeability than ester-terminated PLGA of equivalent inherent viscosity; this property is used to control drug release in gingival crevicular fluid. Uniformity of drug content is evaluated by USP <905>. Mechanical properties are determined by tensile testing per ASTM D882-18; elongation at break typically remains above 5% at 23°C and 50% RH. The residual ethyl acetate limit is 5000 ppm under ICH Q3C. Films are cut to 10 mm × 10 mm or 5 mm × 20 mm and packaged in nitrogen-purged aluminum foil. Placement into the periodontal pocket is intended for local delivery of an antimicrobial agent over 7–14 days. In-vitro dissolution testing uses USP Apparatus 5 paddle-over-disk in synthetic gingival crevicular fluid at 37°C. The final product is assessed under ISO 10993-5:2009 cytotoxicity and ISO 10993-10 irritation testing; sterility may be by gamma irradiation at 25 kGy if the drug substance is radiation-stable.

    Drug-Eluting PLGA Coatings for Orthopaedic Trauma Hardware: Adhesion and Release

    For orthopaedic trauma hardware, PURASORB PDLG 75016A is dissolved at 1–2% w/v in ethyl acetate or acetone to form an ultrasonic spray-coating solution. Titanium or stainless-steel screws are cleaned with 70% isopropanol and dried with nitrogen before coating. An ultrasonic nozzle operating at 60 kHz with a flow rate of 0.5–1.0 mL/min deposits alternating polymer and drug-containing layers onto the implant surface held at 40–60°C. The target coating thickness is 5–15 μm. Drug loading is 5–10% w/w relative to polymer mass. The coated screws are annealed at 40°C for 24 h to remove residual solvent and to improve adhesion. Coating adhesion is assessed by a tape test at room temperature per ASTM D3359-23; for implant use, additional scoring and peel testing are performed according to the sponsor's coating qualification protocol. Residual ethyl acetate is limited to 5000 ppm under ICH Q3C. Release testing in phosphate-buffered saline pH 7.4 at 37°C from a 10 µm coating with 10% w/w drug loading typically shows release over 21–35 days, with an initial 24 h release of 10–20%. The coated implant is assessed for biocompatibility under ISO 10993-6:2016 implantation and ISO 10993-5:2009 cytotoxicity. The primary failure mode is delamination at the metal-polymer interface when the implant is subjected to insertion torque above 4 N·m; published data for this specific low-IV acid-terminated grade on orthopaedic hardware is limited, so adhesion under clinical insertion must be verified on the final geometry.

    Free Quote

    Competitive PURASORB PDLG 75016A Drug Delivery Acid-Terminated PLGA 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

    PURASORB PDLG 75016A is an acid-terminated poly(D,L-lactide-co-glycolide) produced for parenteral drug-delivery and implant applications. The product code identifies the key structural variables: the 75 designation corresponds to a DL-lactide:glycolide molar ratio of 75:25, the 016 corresponds to an inherent-viscosity midpoint of 0.16 dL/g, and the A designates carboxylic acid end-group functionality. Inherent viscosity is determined in chloroform at 25 °C and 0.1% w/v according to USP <911>. The D,L-lactide repeat units suppress crystallinity, and differential scanning calorimetry under ISO 11357-2 generally reports the glass transition between 45 °C and 50 °C. Size-exclusion chromatography in tetrahydrofuran with polystyrene calibration commonly reports weight-average molar mass in the 10,000–20,000 g/mol range for this viscosity class; such values are relative to calibration standards and do not represent absolute molar mass unless MALS detection is used. The free carboxylic acid terminus produces an acid number typically in the 3–7 mg KOH/g range by methanolic potassium hydroxide titration.

    Representative release limits appear below; the lot-specific certificate of analysis controls in all cases.

    Parameter Typical limit or range Method
    DL-lactide monomer ratio 74.0–76.0 mol% ¹H NMR
    Glycolide monomer ratio 24.0–26.0 mol% ¹H NMR
    Inherent viscosity 0.14–0.18 dL/g USP <911>
    Total residual monomers < 0.5% w/w HPLC
    Tin content < 200 mg/kg ICP-MS
    Water content < 0.5% w/w Karl Fischer titration
    Sulfated ash < 0.1% w/w Ph Eur 2.4.14
    Residual solvents ICH Q3C limits Headspace GC

    Because the average chain length is low, solutions at 10%–20% w/w in dichloromethane remain filterable through 0.22 μm membranes at moderate pressure. This differs from higher-inherent-viscosity grades, which may require elevated pressure or lower concentration to pass the same membrane. The polymer dissolves readily in dichloromethane, chloroform, and tetrahydrofuran; acetone and ethyl acetate require solubility screening at the target concentration. Sterilizing-grade filtration of the organic phase should include pre-wetting of the filter cartridge with the same solvent, and filter integrity can be verified by bubble point testing according to ISO 2942.

    Why Does Terminal Carboxylic Acid Functionality Alter Degradation and Drug-Binding Behaviour?

    PLGA hydrolysis proceeds by nucleophilic attack on ester linkages. In an acid-terminated grade, each polymer chain carries a free carboxylic acid group that can donate protons to the surrounding medium. During the early stages of degradation, the local pH within the polymer matrix decreases more rapidly than in an ester-capped analogue, accelerating ester hydrolysis through autocatalysis. This effect is not uniform; it produces a heterogeneous degradation front in particles above 10 μm, where acidic degradation products cannot diffuse out as quickly as they are generated. Monitoring by GPC with chloroform or tetrahydrofuran, mass loss, and pH measurement in phosphate-buffered saline at 37 °C and pH 7.4 is common; ASTM F1635-16 provides a reference framework for PLA-based materials but is not specific to acid-terminated PLGA.

    Drug-polymer interactions are altered by the ionised carboxylate form at physiological pH. The terminal carboxylic acid has an apparent pKa near 4; at pH 7.4 a substantial fraction is deprotonated. Cationic peptides and amine-containing active pharmaceutical ingredients can associate with the anionic terminus, increasing drug loading or altering burst release. Direct published comparisons for the 75:25 0.16 dL/g configuration are limited; therefore, formulation-specific binding studies should be conducted with the actual drug and polymer lot.

    During solvent-evaporation microsphere manufacture, the polymer is commonly dissolved in dichloromethane at 8%–15% w/w. A rotor-stator homogenizer generating 5,000–10,000 min-1 forms a primary water-in-oil emulsion for hydrophilic drugs, which is then dispersed into an aqueous poly(vinyl alcohol) phase under lower shear. Vacuum evaporation at 300–600 mbar and jacket temperature of 25–35 °C removes dichloromethane over 2–6 h. At 10 L reactor scale, the surface-to-volume ratio is lower than in laboratory glassware; therefore solvent removal is heat-transfer and mass-transfer limited, and the evaporation time must be extended or the vacuum increased. The free acid terminus accelerates hydrolysis in the aqueous environment, so the interval between emulsification and lyophilization should be minimized. After freeze-drying, residual moisture should remain below 0.5% w/w to limit storage hydrolysis. Because the solution viscosity is lower than that of 0.5–0.7 dL/g grades, the polymer fraction can be increased without exceeding the mixer manufacturer’s torque limit, but droplet breakup becomes viscosity-ratio dependent.

    Acid-Terminated 75:25 PLGA Is Not Chemically Inert in Aqueous Buffer

    In aqueous processing, the polymer should be treated as a reactive polyester rather than an inert excipient. The ester linkages undergo pseudo-first-order hydrolysis in the early degradation phase; the rate constant is dependent on temperature, pH, and local acid concentration. The acid-terminated grade shows a more pronounced initial hydrolysis rate than an ester-capped grade of the same monomer ratio and viscosity. This has practical importance during wet milling, emulsion quenching, or aqueous washing: prolonged exposure to water above 4 °C can reduce chain length before the polymer is dried. Buffers above pH 8 are particularly aggressive, and primary amine buffers may accelerate chain scission. Processing vessels and tubing should be dry or flushed with anhydrous solvent before introduction of the polymer.

    When Gamma Irradiation Is Applied to a Freeze-Dried PLGA Depot

    Terminal sterilization by gamma irradiation at 25 kGy is validated to achieve a sterility assurance level of 10-6 according to ISO 11137-1. For a low-molecular-weight acid-terminated PLGA, absorbed radiation causes free-radical-mediated chain scission, reducing molecular weight and potentially increasing the acid number. Quantitative dose-response data for this specific configuration are limited. Irradiation should be conducted under dry nitrogen or vacuum and at dry-ice temperatures below -20 °C to limit radical mobility. After irradiation, the product should be re-evaluated for inherent viscosity, GPC molecular weight, and residual monomer content because radiation-induced degradation may alter release performance. If irradiation is carried out in air at ambient temperature, the risk of oxidative chain scission and discoloration increases.

    Compared with an ester-capped 75:25 PLGA of the same inherent-viscosity midpoint, PURASORB PDLG 75016A has a higher acid number and a free terminal carboxylic acid per chain. The ester-capped grade has fewer ionizable end groups for the same chain length, which retards initial water uptake and autocatalytic degradation. Compared with a 50:50 PLGA of similar viscosity, the 75:25 composition is more hydrophobic because the higher lactide content reduces the density of glycolide units; degradation and release are therefore generally slower. Compared with a high-inherent-viscosity grade such as 0.50 dL/g, the 0.16 dL/g grade has a shorter average chain length, lower entanglement, a higher number of end groups per unit mass, and greater diffusivity of small molecules. These differences are most relevant for short-to-intermediate release profiles, but exact duration cannot be assigned without controlled in vitro and in vivo studies.

    Residual Monomer, Tin, and Solvent Compliance Boundaries for Parenteral Use

    Release documentation for PURASORB PDLG 75016A typically includes residual lactide and glycolide monomers, total residual solvent, residual tin from the polymerization catalyst, water content, and sulfated ash. Residual solvents must be controlled to ICH Q3C limits; for example, dichloromethane is Class 2 with a concentration limit of 600 ppm, and chloroform has a Class 2 limit of 60 ppm. Residual tin is typically controlled below 200 mg/kg by ICP-MS; monomer limits are typically below 0.5% w/w by HPLC. The polymer is intended primarily for solvent-based processing rather than melt extrusion; therefore residual solvent control is critical because residual chlorinated solvent in a final injectable depot is directly relevant to patient exposure. Suppliers may maintain a Type V Drug Master File with the United States FDA, but certification for a specific pharmaceutical product requires use of the applicant’s own data and approved specifications.

    Storage and handling boundaries are determined by hydrolytic sensitivity. Containers are closed under inert gas and stored at -20 °C or below. Before weighing, the container should reach ambient temperature in the closed state to prevent condensation. If the polymer is exposed to relative humidity above 60%, vacuum drying at <10 mbar and <25 °C for 24 h is recommended; drying above the glass transition can fuse particles. Residual moisture above 0.5% w/w by Karl Fischer titration promotes hydrolysis during storage. Strongly basic media, primary amines, and aqueous buffers above pH 8 are considered incompatible because they accelerate chain scission of the acid-terminated polyester. These boundaries are operational limits, not platform guarantees; each formulation should be qualified for moisture, residual solvent, and molecular weight at the point of use.

    Top