| HS Code | 374143 |
| Productname | RESOMER RG 502 H |
| Manufacturer | Evonik Industries |
| Chemicalname | Poly(D,L-lactide-co-glycolide) 50:50 |
| Polymertype | Bioresorbable aliphatic polyester |
| Lactideglycolideratio | 50:50 |
| Endgroup | Carboxylic acid (acid terminated) |
| Inherentviscosity | 0.16-0.24 dL/g (0.1% in chloroform at 25°C) |
| Molecularweight | Mw 7,000-17,000 g/mol |
| Glasstransitiontemperature | 40-50°C |
| Appearance | White to off-white granules or powder |
| Crystallinity | Amorphous |
| Density | 1.2 g/cm³ (typical) |
| Solubility | Soluble in dichloromethane, chloroform, ethyl acetate, acetone, tetrahydrofuran; insoluble in water, ethanol, hexane |
| Degradationmechanism | Hydrolytic degradation |
| Degradationproducts | Lactic acid and glycolic acid |
| Bioresorbable | Yes |
| Biocompatible | Yes |
| Watercontent | <0.5% |
| Residualmonomer | <0.5% |
| Tincontent | <200 ppm |
| Heavymetals | <10 ppm |
| Sulfatedash | <0.1% |
| Storageconditions | Store at 2-8°C in a tightly closed container, protected from moisture and light |
| Shelflife | 2 years |
| Application | Drug delivery systems, microparticles, nanoparticles, implants |
| Casnumber | 26780-50-7 |
| Qualitygrade | Drug delivery grade |
As an accredited RESOMER RG 502 H Bioresorbable PLGA Drug Delivery Grade factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | Packaged in 1 g amber glass vials, nitrogen-flushed and foil-sealed with desiccant; labeled RESOMER RG 502 H Bioresorbable PLGA Drug Delivery Grade. |
| Container Loading (20′ FCL) | 20′ FCL container loading: RESOMER RG 502 H Bioresorbable PLGA Drug Delivery Grade, securely packed and shipped under controlled conditions. |
| Shipping | RESOMER RG 502 H Bioresorbable PLGA Drug Delivery Grade is shipped as a non-hazardous, moisture-sensitive solid in sealed, light-resistant containers. It requires cool, dry transport, protected from heat, humidity, and direct sunlight. Packages include product identification, lot number, and storage instructions; no UN dangerous-goods classification applies. |
| Storage | Store RESOMER RG 502 H in a tightly closed, moisture-proof container, preferably under inert gas, at −20°C. Protect from light, heat, and humidity; use desiccant. Allow sealed vial to equilibrate to room temperature before opening to prevent condensation. Avoid repeated temperature cycling and prolonged storage above 8°C to preserve molecular weight. Follow supplier instructions. |
| Shelf Life | Shelf life is typically two years when stored at -20°C in sealed, dry conditions, protected from moisture. |
RESOMER RG 502 H is a bioresorbable 50:50 poly(D,L-lactide-co-glycolide) with acid termination and a low inherent viscosity specified on supplier certificates at 0.16–0.24 dL/g in 0.1% chloroform at 25 °C. The glass transition temperature is typically reported between 38 °C and 45 °C; the copolymer is amorphous and remains soluble in dichloromethane, acetone, ethyl acetate, dimethyl sulfoxide, and N-methyl-2-pyrrolidone under ambient conditions. Because the grade is designated as drug delivery material, batch release documentation includes residual D,L-lactide and glycolide monomers, residual solvents, catalyst residues such as tin, and heavy metals, with data supplied under current good manufacturing practice. The material is not supplied sterile and is not intended for direct clinical use without further processing.
Polymer solutions in dichloromethane at 5–20 wt% are prepared in jacketed reactors under nitrogen and filtered through 0.2 µm hydrophobic membranes. The drug phase is emulsified into the polymer-dichloromethane solution at aqueous-to-organic ratios between 1:5 and 1:20 using a rotor-stator disperser. The resultant primary emulsion is transferred into aqueous poly(vinyl alcohol) with a continuous-phase concentration of 0.5–2.0% w/v; the PVA degree of hydrolysis and molecular weight alter interfacial tension and must be controlled batchwise because the same rotor speed can shift median particle size by several microns. Hardening is carried out by controlled solvent extraction at 35–40 °C under reduced pressure for 2–6 h, after which microspheres are wet-sieved, washed, and lyophilized. Particle size is measured by laser diffraction in water with an obscuration range of 10–20% according to ISO 13320:2020, and residual moisture is determined by Karl Fischer titration per USP <921>. The accepted residual dichloromethane limit for parenteral microspheres is 600 ppm under ICH Q3C Option 2; residual PVA must be quantified and justified because no universal pharmacopoeial limit applies.
Release kinetics from RG 502 H microspheres are governed by PLGA molecular weight, particle size, drug loading, and continuous-phase processing. The acid terminal group increases water uptake and accelerates ester hydrolysis relative to ester-capped 50:50 PLGA of equivalent inherent viscosity. In vitro release in phosphate-buffered saline at 37 °C and sink conditions frequently exhibits a burst of 5–25% of the loaded drug within 24 h, followed by a diffusion-controlled phase and a final erosion-controlled phase; however, published data for this specific configuration is limited. Release testing is performed with USP Apparatus 2 or 4 at 50–100 rpm and 37 °C, with sampling through low-binding filters. Microsphere formulations intended for once-monthly depot injection require a reproducible outer porous layer and a mean particle size above 20 µm to reduce phagocyte-mediated clearance, while sub-10 µm particles are removed more quickly and increase systemic exposure. Each batch must be characterized for glass transition by differential scanning calorimetry at 10 °C/min according to ASTM E1356 after lyophilization because residual solvent plasticization lowers the measured Tg.
| Parameter | Typical operating range | Measurement method | Release response |
|---|---|---|---|
| Polymer concentration in dichloromethane | 5–20 wt% | Gravimetric solids after vacuum drying | Higher concentration increases matrix density and delays initial diffusion |
| Continuous-phase PVA concentration | 0.5–2.0% w/v | Total organic carbon | Higher concentration reduces droplet size and burst release |
| Primary water-in-oil ratio | 1:5–1:20 | Volumetric ratio | Higher aqueous phase volume raises internal porosity and burst |
| Solvent extraction temperature | 35–40 °C | Jacketed vessel temperature probe | Faster extraction densifies surface and reduces residual dichloromethane |
| Lyophilization moisture target | <2.0% | Karl Fischer per USP <921> | Lower moisture minimizes hydrolytic degradation during storage |
For nanoprecipitation and subsequent lyophilization, RESOMER RG 502 H is dissolved at 10–25 mg/mL in acetone or acetonitrile and injected through a 20–28 gauge needle into an aqueous stabilizer phase containing poloxamer 188 or polysorbate 80 at 0.1–0.5% w/v under magnetic or high-shear stirring. Nanoprecipitation produces particles with Z-average diameters of 80–200 nm and polydispersity indices below 0.2 when the solvent-to-nonsolvent ratio exceeds 1:10 and the organic phase is introduced rapidly. Dynamic light scattering per ISO 22412:2017 reports intensity-weighted size; lyophilization requires cryoprotectant addition at 5–10% w/v trehalose or sucrose to prevent aggregation. Residual acetone and acetonitrile are Class 3 solvents with ICH Q3C limits of 5000 ppm and 410 ppm, respectively. The low molecular weight of RG 502 H reduces organic-solvent viscosity, but drug-polymer phase separation during solvent diffusion can reduce encapsulation efficiency below 30% for crystalline APIs with log P above 4. Aqueous-phase pH adjustment with dilute hydrochloric acid or sodium hydroxide is used when the API exhibits pH-dependent solubility. Terminal sterile filtration through 0.22 µm membranes is only feasible for particles below 100 nm; larger particles require aseptic processing.
Syringeability of solutions of RG 502 H in N-methyl-2-pyrrolidone is governed by polymer concentration, solution temperature, needle gauge, and injection rate. At polymer loadings of 20–40 wt%, viscosity measured by cone-plate rheometry at 10 s−1 and 25 °C per ISO 3219-1:2021 remains below 2 Pa·s, allowing manual injection through 21–23 G needles. When dimethyl sulfoxide is substituted for NMP, the solution may exhibit lower viscosity but faster solvent exchange with surrounding water, leading to rapid liquid-liquid demixing and a less uniform depot. The acid-terminal groups of RG 502 H reduce solution stability in the presence of trace water; polymer solutions are therefore prepared under dry nitrogen and stored in glass syringes with low moisture vapor transmission.
Upon subcutaneous or intramuscular injection, NMP concentration at the depot boundary decreases below the critical concentration for polymer precipitation, and a gel shell forms within 30–120 s; final depot geometry depends on injection volume and tissue back pressure. Release from these depots is controlled first by solvent extraction and later by bulk erosion. For a low-molecular-weight acid-terminated 50:50 PLGA, degradation within an aqueous environment is measurable by gel-permeation chromatography within 7–14 days, but published data for this specific formulation is limited. Residual NMP in a parenteral product is classified as a Class 2 solvent with an ICH Q3C limit of 530 ppm; however, depot products are evaluated based on total administered solvent and the elution profile at the injection site. Terminal sterilization of in-situ forming implants is limited to aseptic manufacturing in most cases; gamma irradiation at 25 kGy reduces molecular weight and changes syringeability due to chain scission.
| Solvent | ICH Q3C class | Concentration limit | Process route using RG 502 H |
|---|---|---|---|
| Dichloromethane | Class 2 | 600 ppm | Microspheres, spray coating |
| N-Methyl-2-pyrrolidone | Class 2 | 530 ppm | In-situ forming depot |
| Dimethylformamide | Class 2 | 880 ppm | Electrospinning |
| Acetonitrile | Class 3 | 410 ppm | Nanoprecipitation |
| Acetone | Class 3 | 5000 ppm | Nanoprecipitation |
| Ethyl acetate | Class 3 | 5000 ppm | Spray coating, film casting |
Electrospinning of RG 502 H as the sole polymer is constrained by the low molecular weight of the grade. Solutions at 15–30 wt% in chloroform-dimethylformamide or hexafluoroisopropanol often require blending with a higher-inherent-viscosity PLGA or polycaprolactone at 20–50 wt% of total polymer to stabilize the jet and reduce bead defects. Fibers collected at 15–25 kV on a rotating mandrel show diameters of 400–1200 nm by scanning electron microscopy; the presence of acid-terminal end groups accelerates fiber hydration and mechanical relaxation in phosphate-buffered saline at 37 °C. Residual dimethylformamide must be reduced below 880 ppm under ICH Q3C; vacuum drying below 50 °C is necessary to avoid thermal degradation. Electrospun constructs containing RG 502 H lose tensile strength and break elongation after 7–14 days in aqueous media, but published data for this specific configuration is limited. This route is more relevant for topical or mucosal delivery where drug release occurs within days, not for long-term load-bearing scaffolds.
Compounding of RG 502 H by twin-screw extrusion is carried out with a barrel configuration of 20:1–40:1 L/D ratio and temperature zones set between 90 °C and 120 °C. The low melt viscosity produces torque below 15 N·m at screw speeds of 50–200 rpm, but the processing window narrows sharply above 130 °C. At that threshold, hydrolytic and thermal backbone scission occurs, and measurable reduction in molecular weight by gel-permeation chromatography can be detected after 5–10 min residence time. Feedstock must be dried under vacuum at 40–50 °C for 24–48 h to a moisture content below 0.5%, because the acid terminal groups catalyze hydrolysis in the presence of residual water. API loadings of 10–30 wt% are processed; amorphous drug recrystallization during storage is a known failure mode when drug-polymer miscibility is exceeded, and physical stability is assessed by differential scanning calorimetry with a heating rate of 10 °C/min.
Extrudate from RG 502 H can be pelletized and injection molded into solid implants at barrel temperatures of 100–120 °C and mold temperatures of 20–25 °C; cold mold surfaces reduce dimensional distortion but may induce orientation. The molded implants are tested for molecular weight retention by gel-permeation chromatography; a reduction above 10% relative to unprocessed polymer generally indicates thermal degradation or inadequate drying. Sterilization of extruded implants by gamma irradiation at 25 kGy is common for implantable devices but requires post-irradiation gel-permeation chromatography and dissolution testing because chain scission reduces Tg and alters release. Ethylene oxide is generally not recommended for low-Tg PLGA because gas absorption and residual ethylene oxide and chlorohydrin limits create additional analytical burden.
Ophthalmic depot products formulated with RG 502 H must address residual monomer and oligomer levels more tightly than non-ocular parenterals. D,L-lactide and glycolide monomers are quantified by gas chromatography from supplier certificates, typically reported as weight percent relative to polymer. Residual monomer accelerates acidification and water uptake in the vitreous cavity; local pH excursions can contribute to vitreous opacity or cellular toxicity. Finished product testing includes ophthalmic particulate limits per USP <789> and visible particulate inspection per USP <790>, with rejection of aggregates above 100 µm. In vitro release in simulated vitreous humor at 37 °C often shows an initial hydration lag during the first 24–72 h, followed by diffusion and erosion phases; published data for this specific configuration is limited.
Particle size measurement by laser diffraction per ISO 13320:2020 is combined with pH monitoring of release media; a pH drop below 6.5 is undesirable for ocular formulations. Cytotoxicity evaluation per ISO 10993-5 and extractables profiling per ISO 10993-12 are used to assess polymer impurities, including tin residues and residual monomers. Terminal sterilization by gamma irradiation is possible at 15–25 kGy, but molecular weight distribution must be verified before release. Aseptic manufacturing is the primary route when particle suspensions or in-situ depots are filled into prefilled syringes.
Spray coating of metallic or polymeric implant surfaces uses RG 502 H at 1–5 wt% in dichloromethane or ethyl acetate, applied with ultrasonic atomization. Coating thicknesses of 2–20 µm are measured by step profilometry or scanning electron microscopy cross-section; the low glass transition of 38–45 °C necessitates low-temperature drying below 50 °C. Adhesion failure occurs on cobalt-chromium alloy surfaces unless a silane or plasma treatment is used. Residual dichloromethane in the finished device must be below 600 ppm; extractables profiling according to ISO 10993-12 is required. Simulated deployment testing includes light microscopy after crimping or balloon expansion, and particulates in rinse solutions are counted per USP <788>. Gamma irradiation at 25 kGy is used for device sterilization; however, molecular weight reduction and coating-brittleness changes must be assessed, and published data for this specific configuration is limited.
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RESOMER RG 502 H Bioresorbable PLGA Drug Delivery Grade is a poly(D,L-lactide-co-glycolide) copolymer with a 50:50 molar lactide:glycolide ratio, free carboxylic acid end groups, and a low-viscosity specification that positions it for solvent-based microencapsulation, nanoparticle formation, and short-duration implantable depot systems. The PLGA backbone is identified by CAS 26780-50-7; the H suffix in the grade name designates acid termination, whereas the corresponding ester-terminated grade is designated RG 502. Typical release-control specification values include an inherent viscosity of 0.16–0.24 dL/g measured as a 0.1% w/v solution in chloroform at 25 °C using ISO 1628-1 or ASTM D2857, and a glass transition temperature of 42–46 °C determined by differential scanning calorimetry according to ISO 11357-2. Residual moisture is normally specified below 0.5% by Karl Fischer titration per USP ⟨921⟩, and residual monomer content is typically reported below 0.5% on vendor certificates of analysis.
The material is soluble in dichloromethane, chloroform, acetone, and ethyl acetate, and is insoluble in water. This solubility profile allows oil-in-water emulsification, organic-phase coacervation, spray drying, and phase-inversion processing without high-temperature melt extrusion. The low inherent viscosity lowers the organic-phase viscosity of polymer solutions, which can support filtration through 0.2 µm membranes when dilute solutions in the 5–10 wt% range are used. The same low viscosity limits melt strength and makes the grade less suitable for load-bearing injection-molded implants than higher-viscosity PLGA grades.
| Parameter | Typical value or range | Analytical method |
|---|---|---|
| Copolymer ratio | 50:50 D,L-lactide:glycolide | ¹H NMR or hydrolysis with HPLC |
| Inherent viscosity | 0.16–0.24 dL/g | ISO 1628-1 / ASTM D2857, 0.1% w/v in chloroform at 25 °C |
| Glass transition temperature | 42–46 °C | ISO 11357-2 differential scanning calorimetry |
| Residual monomers | <0.5% | HPLC, vendor certificate of analysis |
| Water content | <0.5% | USP ⟨921⟩ Karl Fischer titration |
| Solubility | Soluble in dichloromethane, chloroform, acetone, ethyl acetate; insoluble in water | Qualitative solvent miscibility |
The terminal functionality is the controlling structural difference between RG 502 H and RG 502. RG 502 H carries free carboxylic acid end groups; RG 502 carries ester end groups. The acid terminus increases water uptake and reduces the initial hydrophobic surface character of the matrix, which shortens the induction period before mass loss begins. In phosphate-buffered saline at pH 7.4 and 37 °C, acid-terminated 50:50 PLGA generally degrades faster than an ester-terminated 50:50 PLGA of equivalent inherent viscosity. This is not a compliance defect but a formulation tool: the acid-terminated grade is selected when rapid hydrolytic resorption is required, and the ester-terminated grade is selected when slower water penetration or reduced initial acid load is preferred.
The difference is particularly relevant for acid-labile active pharmaceutical ingredients. Carboxylic acid end groups can lower the local pH within the polymer matrix during hydrolytic degradation, and the resulting microclimate can promote degradation of proton-sensitive peptides, esters, or acid-labile small molecules. For amine-containing drugs, the acid end groups can form salt or ion-pair structures that alter encapsulation efficiency and release kinetics. In such cases, ester-terminated RG 502 may provide a more inert matrix environment, although release must still be confirmed because PLGA hydrolysis generates carboxylic acid groups regardless of the initial end-group state.
| Grade | End group | Lactide:glycolide ratio | Inherent viscosity | Typical processing and use |
|---|---|---|---|---|
| RG 502 H | Acid | 50:50 | 0.16–0.24 dL/g | Solvent-based microspheres, nanoparticles, short-term depots |
| RG 502 | Ester | 50:50 | 0.16–0.24 dL/g | Matrix formulations requiring slower water uptake or acid-sensitive payloads |
| RG 503 H | Acid | 50:50 | 0.32–0.44 dL/g | Longer-retention depot systems, films, more viscous organic phases |
Inherent viscosity is the primary specification that differentiates RG 502 H from higher-viscosity acid-terminated grades such as RG 503 H and RG 504 H. The 0.16–0.24 dL/g band for RG 502 H corresponds approximately to a reported weight-average molecular weight range of 7,000–17,000 g/mol in vendor literature, though batch-to-batch polydispersity influences degradation and release behavior. Because molecular weight is not a compendial release parameter for this polymer, viscosity-controlled specification bands are used to maintain lot-to-lot consistency. The glass transition temperature of 42–46 °C places the material close to ambient processing temperatures; long-term storage is therefore maintained at −20 °C with desiccant protection because moisture uptake above 0.5% initiates hydrolysis even in the solid state.
In pharmaceutical development, the glass transition has practical consequences for liquid handling and drying. Spray-dried powders produced from acetone or ethyl acetate solutions require outlet temperatures below 40 °C to avoid particle coalescence, because the operating temperature approaches the polymer glass transition. The inlet temperature window is typically held between 45 °C and 65 °C, and the outlet temperature is controlled by feed rate and gas flow. This narrow window is a process conflict: higher inlet temperature improves solvent evaporation but pushes the outlet temperature toward the glass transition, while lower inlet temperature reduces evaporation and increases residual solvent. The acid end groups do not eliminate this thermorheological boundary; they are relevant mainly to degradation and water interaction, not to the glass transition itself.
The low inherent viscosity of RG 502 H also reduces organic-phase viscosity in microencapsulation. A 20 wt% solution in dichloromethane has a significantly lower dynamic viscosity than a 20 wt% solution of RG 503 H, which reduces the required emulsification shear and lowers motor torque on production rotor-stator dispersers. This is critical when scaling from laboratory batch to production-scale mixers because lower torque permits longer continuous emulsification runs before the stator seal reaches its thermal limit. Published torque values for this specific polymer configuration are limited, and equipment-specific validation is required.
Oil-in-water emulsification is a primary route for preparing RG 502 H microspheres. The polymer is dissolved in dichloromethane at 10–30 wt%, the drug is either dissolved or dispersed in the organic phase, and the solution is injected or dispersed into an aqueous continuous phase containing 1–2% w/v polyvinyl alcohol at 2–8 °C. High-shear rotor-stator dispersers with tip speeds of 10–20 m/s are typically used to generate microspheres in the 10–100 µm size range. The low-viscosity acid-terminated grade allows higher polymer loading in the organic phase while maintaining droplet break-up under shear, which can improve encapsulation efficiency for hydrophobic drugs. However, higher polymer concentration also increases the residual solvent burden, and the hardening bath must be designed to remove dichloromethane without causing shell collapse.
The hardening step is a critical threshold. If solvent removal is too rapid, a dense polymer shell forms before the dispersed droplet has fully contracted, producing hollow or collapsed microspheres. If solvent removal is too slow, drug migration to the particle surface increases burst release and lowers encapsulation efficiency. Typical hardening protocols hold the emulsion below 4 °C for the first 2–3 h, then gradually warm to 25 °C under controlled stirring at 300–500 rpm. Residual dichloromethane after washing and lyophilization is typically targeted below 600 ppm because the ICH Q3C Class 2 limit for dichloromethane is 600 ppm. This is a finished-product specification, not a property of the polymer itself, but it drives the processing design for RG 502 H formulations.
For nanoparticle processing, the same low-viscosity grade can be used in nanoprecipitation or emulsion-solvent diffusion. A dilute organic phase of 5–10 wt% is injected into an aqueous surfactant phase, and the solvent is removed by vacuum stripping or dialysis. The acid end groups provide colloidal stability through electrostatic repulsion at neutral pH, but this effect is formulation-dependent and should not be substituted for appropriate surfactant or steric stabilization. The acid end groups can also interact with cationic lipids or amine-containing surfactants, which may reduce zeta potential and increase aggregation. Published data for this specific configuration is limited, and formulation-specific electrokinetic characterization is required.
The grade is also used in phase-inversion depot systems where a water-miscible solvent such as N-methyl-2-pyrrolidone or dimethyl sulfoxide is used to dissolve the polymer and drug. Upon injection into an aqueous environment, the solvent exchanges with water and the polymer precipitates as a depot. The low inherent viscosity of RG 502 H allows injection through smaller-gauge needles at lower force, but the trade-off is a faster water influx and often a higher initial burst than higher-viscosity grades. Burst release must be characterized by in vitro release testing under sink conditions; the test media and sampling intervals should be aligned with the intended route of administration.
Operational boundaries for RG 502 H include avoidance of long-term storage in organic solution, because even trace water can initiate ester hydrolysis. Stock solutions should be prepared under dry conditions, stored at −20 °C, and used within 24 h unless stability data support longer holding times. Melt processing should not exceed 120 °C because thermal depolymerization accelerates and may alter the lactide:glycolide ratio. If melt extrusion is used as a downstream blending step, twin-screw extruders with L/D ratios of 20:1 to 30:1 and barrel temperatures in the 80–110 °C range are more appropriate than injection molding, but solvent-based processing remains the primary route for this grade.
For biological qualification, the raw polymer is not a therapeutic product and cannot be evaluated as a finished device. Manufacturers must qualify the polymer as a starting material under ICH Q7 or ISO 13485 quality systems. Vendor documentation typically includes residual solvent, heavy metals, and endotoxin data, but final device evaluation is performed according to ISO 10993-1. Cytotoxicity testing is conducted on the finished article using ISO 10993-5, and parenteral products require endotoxin control per USP ⟨85⟩. Residual solvent and moisture limits are applied to the finished dosage form using USP ⟨467⟩ and USP ⟨921⟩, respectively, rather than being accepted solely from raw polymer certificates.