| HS Code | 871820 |
| Productname | RESOMER R 203 H Bioresorbable Injectable Poly(D,L-lactide) |
| Chemicalname | Poly(D,L-lactide) |
| Abbreviation | PDLLA |
| Polymercomposition | 100% D,L-lactide homopolymer |
| Endgroup | Free carboxylic acid (acid-terminated; H grade) |
| Casnumber | 26680-10-4 |
| Molecularformula | (C3H4O2)n |
| Appearance | White to off-white granules or powder |
| Form | Solid granules or powder |
| Solubility | Soluble in dichloromethane, chloroform, acetone, ethyl acetate, and tetrahydrofuran; insoluble in water and ethanol |
| Density | 1.2–1.3 g/cm3 |
| Glasstransitiontemperature | Approximately 45–60 °C |
| Inherentviscosity | 0.3 dL/g nominal; range approximately 0.25–0.35 dL/g (chloroform, 25 °C) |
| Residualmonomer | ≤0.5% |
| Watercontent | ≤0.5% |
| Heavymetals | ≤10 ppm |
| Storageconditions | Store at 2–8 °C, protected from moisture, light, and oxygen |
| Shelflife | 24 months when stored as recommended |
| Biodegradability | Hydrolytically biodegradable to lactic acid |
| Biocompatibility | Biocompatible and bioresorbable |
| Sterilizationmethod | Gamma irradiation or aseptic processing; terminal sterilization may reduce molecular weight |
| Application | Injectable sustained-release drug delivery, microparticles, nanoparticles, and implants |
As an accredited RESOMER R 203 H Bioresorbable Injectable Poly(D,L-lactide) factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | The chemical is packaged as 5 g in a securely sealed, labeled glass bottle for laboratory use. |
| Container Loading (20′ FCL) | 20′ FCL loaded with RESOMER R 203 H bioresorbable injectable poly(D,L-lactide), securely palletized in sealed drums under dry, controlled conditions. |
| Shipping | RESOMER R 203 H is shipped as a non-hazardous, bioresorbable poly(D,L-lactide) powder in tightly sealed, moisture-barrier containers, typically under nitrogen, at ambient temperature. No UN number, hazard class, or packing group is required. Protect from moisture, heat, and light; store at -20°C upon receipt. |
| Storage | Store RESOMER R 203 H in its original, tightly closed, moisture-proof container under cool, dry conditions. Recommended storage is 2–8°C, or −20°C for extended periods, protected from light, heat, and moisture. Before opening, allow the sealed package to equilibrate to room temperature to prevent condensation. Avoid repeated temperature cycling, as moisture uptake can hydrolyze the polyester. |
| Shelf Life | Shelf life is 2 years when stored unopened at −20°C, protected from moisture, heat, and light; see label expiry. |
RESOMER R 203 H is an amorphous acid-terminated poly(D,L-lactide) with an inherent viscosity of 0.25–0.35 dL/g measured at 0.1% w/v in chloroform at 25 °C and a glass transition temperature near 38–45 °C. The low molar mass reduces solution viscosity relative to higher-inherent-viscosity poly(D,L-lactide) grades and accelerates bulk hydrolytic degradation. Downstream application segments are therefore concentrated in injectable, thin-walled, or low-residual-solvent bioresorbable systems in which syringeability, low processing temperature, and degradation within a clinically useful timeframe are required.
Residual dichloromethane content and particle size distribution are the two dominant release and regulatory constraints in this segment. The downstream production process uses a water-in-oil-in-water double emulsion: an aqueous drug solution is emulsified into an organic phase consisting of R 203 H dissolved in dichloromethane at 5–15% w/v using a rotor-stator homogenizer at 10,000–24,000 rpm for 1–3 min; the primary emulsion is then dispersed into an external aqueous poly(vinyl alcohol) solution of 0.25–1.0% w/v at an organic-to-aqueous phase ratio between 1:10 and 1:20. Solvent extraction and evaporation are carried out under reduced pressure at 4–25 °C before tangential-flow filtration and lyophilization. The formulation addition ratio for R 203 H to active pharmaceutical ingredient ranges from 3:1 to 10:1 w/w for low-dose peptides and from 10:1 to 20:1 w/w for high-potency small molecules, with final drug loading typically 10–30 wt%. Compliance is assessed under USP <711> dissolution testing, USP <788> particulate matter for injections, ICH Q3C(R8) residual solvent limits with dichloromethane Class 2 limit of 600 ppm, and ISO 10993-1:2018 biological evaluation, with aseptic filling under ISO 13485:2016 quality systems. Terminal product types include long-acting injectable suspensions of naltrexone, risperidone, leuprolide acetate, and octreotide acetate, supplied as dry microsphere vials reconstituted with an aqueous diluent immediately before intramuscular or subcutaneous administration. On production-scale lines, batch-to-batch variation in primary emulsion viscosity is a recurrent bottleneck; if dispersed-phase viscosity drifts outside the calibrated range, satellite droplet formation increases and the microsphere span widens beyond release specification.
When the polymer–solvent mixture contacts aqueous tissue fluid, the organic solvent diffuses outward and water diffuses inward, precipitating R 203 H into a porous depot. The downstream production process for an aseptic injectable solution consists of dissolving R 203 H and the active ingredient in N-methyl-2-pyrrolidone or dimethyl sulfoxide in jacketed vessels, preclarifying through 25 µm and 5 µm capsule filters, and filling under nitrogen into single-dose syringes; terminal sterilisation is not used because gamma irradiation reduces molar mass and accelerates free-acid generation, so aseptic processing under ISO 13485:2016 is mandatory. The formulation addition ratio for R 203 H in the organic solvent is between 30 wt% and 50 wt%, with active-to-polymer weight ratios typically 1:5 to 1:10. At this concentration range the dynamic viscosity of the solution is sufficiently low for 18–21 G needle penetration but high enough to limit rapid solvent exchange. Industry compliance standards for this configuration include ICH Q3C(R8) for residual solvent limits, USP <787> subvisible particulate matter where applicable, USP <790> visible particulates, and biological evaluation per ISO 10993-1:2018 including local tolerance after implantation. Terminal product types include leuprolide acetate depot, doxycycline hyclate periodontal in-situ gel, and veterinary sustained-release injectable depots. The critical operational boundary is the initial burst release: because the depot precipitates rapidly, drug dissolved in the solvent front partitions into the surrounding tissue before the polymer matrix solidifies; this is controlled by increasing polymer concentration and by selecting a solvent with a slower phase inversion rate, but the resulting high solvent load can produce injection-site myotoxicity at volumes above 1 mL per site.
Application of poly(D,L-lactide) coatings to stent struts requires a low-viscosity solution that yields a continuous film without bridging between struts. The downstream production process uses a coaxial ultrasonic spray nozzle operating at a nozzle frequency in the 40–120 kHz range and a spray head travel speed of 10–30 mm/s, with a dilute polymer–drug solution in acetone or a dichloromethane–acetone mixture deposited onto rotating cobalt-chromium or platinum-chromium stents. The polymer-to-drug ratio is typically set between 1:1 and 3:1 w/w, and the final dry coating thickness is held between 2 µm and 6 µm to avoid delamination during balloon expansion. R 203 H at 0.5–2.0% w/v in acetone is used as a matrix layer or topcoat because its low molecular weight reduces solution viscosity and enables higher drug loading without gelation. Compliance for bioabsorbable stent coatings is evaluated under ISO 25539-1 and ISO 25539-2 for cardiovascular and endovascular prostheses, ISO 10993-4 for hemocompatibility, ISO 10993-5 for cytotoxicity, and ISO 10993-6 for local implantation effects. Terminal product types include drug-eluting coronary stents and peripheral artery stents with a bioabsorbable PDLLA carrier layer. The principal limitation is the low glass transition temperature of R 203 H; if coated stents are stored above 35 °C or crimped onto balloon catheters with excessive radial force, coating deformation and drug migration within the amorphous layer may alter the release profile.
For intradermal and subdermal volumizing products, the acid-terminated poly(D,L-lactide) grade R 203 H is processed into microspheres with a mean particle diameter of 30–80 µm and suspended in a carboxymethylcellulose gel carrier for aseptic pre-filled syringes. The production process begins with oil-in-water solvent evaporation or spray drying of the polymer from dichloromethane or ethyl acetate; the microspheres are sieved to remove particles below 20 µm that may be internalised by macrophages, washed to remove residual surfactant, and lyophilised before aseptic dispersion in the carrier gel. The formulation addition ratio of R 203 H microspheres to the injection vehicle is typically 20–40 mg/mL, corresponding to 2–4 wt% of the final injectable volume; polymer-to-carrier ratios above 4 wt% produce syringe extrusion forces that exceed hand-injection limits for 30 G needles. Industry compliance standards include ISO 10993-1:2018 for biological evaluation, USP <788> particulate matter testing for the carrier phase, ICH Q3C(R8) residual ethyl acetate where applicable, and ISO 11608-1:2022 for needle-based injection system container performance under the medical device regulation. Terminal product types include sterile injectable PDLLA dermal fillers intended to stimulate collagen deposition, supplied in single-use pre-filled syringes of 0.5 mL to 2.0 mL. A specific operational boundary is vascular occlusion: inadvertent intravascular injection of microspheres larger than 20 µm is a clinical risk, so the product label and injection training must enforce needle aspiration and low-pressure delivery.
In a calcium phosphate–polymer composite intended for percutaneous injection, the continuous phase is R 203 H dissolved in N-methyl-2-pyrrolidone or dimethyl sulfoxide and the dispersed phase is beta-tricalcium phosphate or hydroxyapatite granules. The downstream production process involves dry blending and sieving of 100–400 µm ceramic granules, followed by mixing with the polymer solution under vacuum to eliminate air bubbles, then packing into pre-sterilised syringes under aseptic conditions. The formulation addition ratio of R 203 H to the ceramic phase is between 10:90 and 20:80 w/w polymer-to-ceramic, equivalent to a polymer content of 10–20 wt% of the total composite; higher polymer fractions improve cohesiveness but delay osseointegration because the acidic degradation products reduce local pH. Compliance for this segment is evaluated under ISO 13779-1 for hydroxyapatite ceramics where applicable, ASTM F1635 for in vitro degradation of hydrolytically degradable polymers, ISO 10993-6 for local tissue reaction, and ICH Q3C(R8) for residual solvent control. Terminal product types include injectable bone void fillers, dental socket preservation grafts, and craniofacial defect fillers supplied in 1–5 mL syringes. The critical process boundary is the suspension stability window: because R 203 H solutions with N-methyl-2-pyrrolidone have limited shelf life at temperatures above 25 °C, compounded syringes are typically stored refrigerated and used within 24–48 h after mixing to prevent settling of the ceramic phase and premature solvent loss.
Intravitreal sustained-release implants manufactured from low-molecular-weight acid-terminated PDLLA require a low-residual-solvent process to prevent retinal toxicity, so hot-melt extrusion or solvent-free compression molding is used instead of solvent casting. R 203 H is blended with the active agent at a drug-to-polymer ratio between 1:1 and 1:3 w/w, then extruded through a single-screw or twin-screw extruder with barrel temperatures of 80–120 °C; the extrudate is drawn to a diameter of 0.3–0.5 mm and cut into rods of 6–8 mm length for insertion through a 22 G needle. The low melt viscosity of R 203 H permits processing below 120 °C, which is necessary for heat-labile corticosteroids and peptides, but the screw speed and residence time must be controlled because the acid end group accelerates chain scission in the presence of moisture. Compliance for this configuration is assessed under ISO 10993-1:2018 biological evaluation, ISO 10993-5 cytotoxicity using retinal pigment epithelial cell lines, ICH Q3C(R8) residual solvent limits, and ASTM F1635 in vitro hydrolytic degradation testing. Terminal product types include intravitreal dexamethasone implants and experimental sustained-release rods for anti-VEGF agents. The operational boundary is moisture control: the polymer must be dried to ≤ 0.5% (w/w) water before hot-melt extrusion, otherwise steam bubble formation and molecular weight loss during compounding produce implant diameter variability and premature erosion. Published data for R 203 H in this specific intravitreal configuration is limited, so process validation relies on internal degradation studies combined with ASTM F1635 in vitro hydrolytic degradation testing.
Competitive RESOMER R 203 H Bioresorbable Injectable Poly(D,L-lactide) 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
Flexible payment, competitive price, premium service - Inquire now!
RESOMER R 203 H is a bioresorbable poly(D,L-lactide) bearing a free carboxylic acid terminal group. The grade is produced by ring-opening polymerization of D,L-lactide and is supplied as an amorphous, white to off-white powder or granules with no crystalline melting endotherm. The product designation is systematic: the prefix R identifies a poly(D,L-lactide) homopolymer, 203 denotes the nominal inherent-viscosity grade, and H identifies acid termination. The target inherent viscosity is 0.25–0.35 dL/g measured at 0.1 g/dL in chloroform at 25°C. The polymer is intended as a formulation excipient for injectable depots, microparticles, nanoparticles, and other parenteral drug-delivery matrices; it is not supplied as a ready-to-inject solution.
The presence of a single free carboxylic acid group per chain distinguishes RESOMER R 203 H from ester-terminated poly(D,L-lactide) grades of similar molar mass. Acid termination increases chain-end hydrophilicity, provides a reactive site for conjugation or ion-pair formation, and contributes to local acid-catalyzed hydrolysis once water ingress occurs. In hydrated matrices, the terminal acid group can promote autocatalytic ester hydrolysis, which tends to produce heterogeneous degradation with faster internal molecular-weight loss than surface erosion. Published data for this specific grade is limited; however, studies on low-molecular-weight poly(D,L-lactide) generally report that acid-terminated polymers exhibit faster initial water uptake and hydrolysis than ester-terminated analogs of comparable molecular weight. The amorphous character of poly(D,L-lactide) arises from the random stereochemical distribution of D- and L-lactide units, which suppresses crystallization and supports solubility in a range of water-miscible organic solvents.
Lot-release documentation for RESOMER R 203 H typically includes inherent viscosity, residual lactide monomer, residual solvents, and tin catalyst content. Inherent viscosity is not a direct molecular-weight measurement; it is a solution-viscosity parameter that depends on solvent, concentration, temperature, and polymer-solvent interactions. Molecular weight may be estimated by gel-permeation chromatography with polystyrene calibration, but published Mark-Houwink coefficients for poly(D,L-lactide) in chloroform vary, so comparative values should state the calibration standard and eluent conditions. The table below summarizes parameters commonly reported in certificates of analysis or manufacturer technical data.
| Parameter | Target or Typical Range | Analytical Basis |
|---|---|---|
| Inherent viscosity | 0.25–0.35 dL/g | ISO 1628-1; 0.1 g/dL in chloroform, 25°C |
| Appearance | White to off-white powder or granules | Visual inspection |
| Residual lactide monomer | Typically below 0.5 wt% | Gas chromatography with flame ionization detection |
| Residual solvent | Typically below 0.5 wt% | Headspace gas chromatography |
| Tin content | Lot-specific; typically below 200 ppm | Inductively coupled plasma optical emission spectrometry after acid digestion |
Release limits are lot-specific and should be confirmed against the manufacturer’s certificate of analysis. For injectable applications, additional pharmacopeial testing may be required for bacterial endotoxins, sterility, and biological reactivity. No single certificate-of-analysis value replaces end-product testing of the finished drug product.
In formulation development, the 0.25–0.35 dL/g inherent-viscosity range creates a measurable trade-off between injectability and depot coherence. Lower-viscosity lots dissolve more readily and produce lower solution viscosity at equal polymer concentration, but they may generate softer depots and faster release. Higher-viscosity lots typically increase solution viscosity and depot mechanical integrity while potentially extending release duration. Because this grade spans approximately 0.1 dL/g, individual lots may require adjustment of solvent ratio, polymer concentration, or injection speed to maintain consistent syringeability and burst control.
For injectable in situ forming depots, RESOMER R 203 H is commonly dissolved at 10–40 wt% in water-miscible solvents such as N-methyl-2-pyrrolidone, dimethyl sulfoxide, or 2-pyrrolidone. N-Methyl-2-pyrrolidone is classified as Class 2 under ICH Q3C with a permitted daily exposure of 5.3 mg/day, while dimethyl sulfoxide is Class 3. Solvent choice affects solution viscosity, phase-inversion rate, polymer precipitation morphology, and residual-solvent clearance from the implant site. High polymer concentrations above 30 wt% may require pre-warming or larger needle diameters to maintain acceptable extrusion force through 21–25 G needles. Solution viscosity should be characterized with a cone-and-plate or parallel-plate rheometer at 25°C and shear rates representative of syringe flow, typically 10–100 s⁻¹, because non-Newtonian shear-thinning behavior may be significant at higher polymer loadings.
Phase-sensitive depot formation occurs when a polymer-solvent solution contacts an aqueous physiological medium. The water-miscible solvent partitions into the surrounding fluid, water diffuses inward, and phase inversion precipitates the polymer into a solid or semi-solid depot. For acid-terminated poly(D,L-lactide), rapid solvent exchange can produce a porous or open-cell interior that influences the initial release phase. Slower phase inversion using less water-miscible solvents or higher polymer concentrations generally yields a denser outer skin and reduces burst, but it also increases solution viscosity and may compromise injectability.
On production-scale mixing, dual-asymmetric centrifugal mixers or low-shear propeller mixers are preferred for dissolution because high-shear rotor-stator devices can generate localized heating and may induce chain scission. Dissolution should be performed under dry inert gas where possible; moisture ingress during mixing promotes hydrolysis and can reduce inherent viscosity before terminal sterilization. Batch-to-batch variation within the 0.25–0.35 dL/g specification can change filter pressure drop across a 0.22 µm membrane by a factor that is dependent on polymer concentration, solvent, and temperature. Prefiltration through a 0.45 µm membrane is commonly used to protect the sterile filter. Sterile filtration of viscous polymer solutions may require elevated temperature up to 40°C, but prolonged heating accelerates degradation and should be minimized.
Syringeability is not an intrinsic polymer property. It must be measured with the intended primary container, plunger stopper, needle gauge, and flow rate. A typical bench characterization uses a constant-rate syringe pump at 0.5–2.0 mL/min and records the maximum glide force or plateau force. Acceptance limits are device-specific and should account for user population, injection volume, and needle length. Extrusion force increases with polymer concentration and molecular weight and decreases with needle diameter and temperature.
RESOMER R 203 H degrades by hydrolytic chain scission of ester linkages. Water absorption precedes molecular-weight loss, and mass loss lags behind molecular-weight reduction because low-molecular-weight fragments must become sufficiently water-soluble to diffuse from the matrix. In amorphous poly(D,L-lactide), degradation is bulk-dominated rather than surface-erosion-dominated. The free carboxylic acid end groups in R 203 H contribute to a locally acidic microenvironment, especially in the core of larger depots or microparticles where acidic oligomers cannot rapidly diffuse out. This autocatalytic effect can create a faster-degrading core and a slower-degrading shell, a heterogeneous pattern that has direct consequences for drug-release linearity and mechanical integrity.
Release from R 203 H matrices may be diffusion-controlled, degradation-controlled, or mixed, depending on drug solubility, drug loading, matrix geometry, and polymer molecular weight. For low-molecular-weight acid-terminated poly(D,L-lactide), the initial release phase is often governed by drug diffusion through water-swollen polymer and by solvent exchange if an organic solvent is used. Later release accelerates when the matrix undergoes bulk degradation and loses barrier function. Published data for this specific grade under standardized in vitro conditions is limited; release profiles should be generated experimentally in pharmacopeial dissolution media with appropriate sink conditions and temperature control.
Compared with RESOMER R 202 H, which has a lower target inherent viscosity of 0.16–0.24 dL/g, R 203 H provides higher solution viscosity at equal concentration, typically lower initial burst, and a more mechanically coherent depot. Compared with RESOMER RG 502 H, a 50:50 poly(D,L-lactide-co-glycolide) with acid termination and 0.16–0.24 dL/g inherent viscosity, R 203 H lacks glycolide repeat units. Glycolide increases hydrophilicity and accelerates hydrolysis, so RG 502 H generally degrades faster than R 203 H under identical conditions. Compared with ester-terminated RESOMER R 203 or higher-viscosity grades such as R 205, the acid-terminated R 203 H has a more hydrophilic chain end and reduced chain length, making it more suitable for solvent-based injectable systems and less suited to load-bearing implants requiring long-term mechanical strength.
| Resomer Grade | Backbone Composition | Terminal Group | Target Inherent Viscosity | Typical Formulation Implication |
|---|---|---|---|---|
| R 202 H | Poly(D,L-lactide) | Acid | 0.16–0.24 dL/g | Lower solution viscosity, faster degradation, easier sterile filtration |
| R 203 H | Poly(D,L-lactide) | Acid | 0.25–0.35 dL/g | Intermediate solution viscosity, injectable depots and microparticles |
| R 203 | Poly(D,L-lactide) | Ester | 0.25–0.35 dL/g | Reduced terminal acid content, potentially slower initial hydrolysis |
| RG 502 H | Poly(D,L-lactide-co-glycolide) 50:50 | Acid | 0.16–0.24 dL/g | Higher hydrophilicity, faster degradation, shorter release duration |
Aseptic processing is preferred for terminal sterilization of R 203 H formulations. Steam sterilization of bulk polymer powder or aqueous suspensions is generally unsuitable because moisture and elevated temperature accelerate hydrolytic degradation. Gamma irradiation at 25 kGy may reduce inherent viscosity and generate free radicals, so post-irradiation characterization of molar mass and degradation products is required. Ethylene oxide sterilization may be applied to dry polymer, but residual gas limits must comply with ISO 10993-7. For polymer solutions, sterile filtration through 0.22 µm membranes is used when viscosity permits; if sterile filtration is not feasible, aseptic handling of gamma-sterilized bulk polymer may be required. End-product depots, microparticles, and nanoparticle dispersions must be evaluated for bacterial endotoxins, sterility, and particulate matter according to the relevant pharmacopeial monographs.
Processing and storage boundaries for RESOMER R 203 H reflect the hydrolytic sensitivity of the polyester backbone. The polymer should be stored in tightly closed containers under dry inert gas at reduced temperature, typically below 5°C for long-term stability. Before melt processing or solvent use, moisture content should be verified by coulometric Karl Fischer titration; pre-drying under vacuum at ambient temperature or slightly above is common, but drying above 40°C for prolonged periods can initiate thermal degradation. Prolonged exposure above 140°C during melt extrusion or injection molding is not typical for this low-molecular-weight grade and may generate lactide monomer while reducing molar mass. Compatibility with active pharmaceutical ingredients, solvents, and additives must be confirmed experimentally because acidic terminal groups may interact with basic drugs or pH-sensitive compounds.
Regulatory evaluation of RESOMER R 203 H as an excipient in parenteral products should include biological safety assessment according to ISO 10993-1, endotoxin testing according to the relevant pharmacopeial method, and residual solvent compliance according to ICH Q3C. The manufacturer’s quality documentation should be retained as part of the drug master file or technical package. Because the polymer degrades to lactic acid, which enters normal metabolic pathways, its degradation products are generally regarded as resorbable, but the local acidification at the implant site remains a formulation-dependent safety consideration, particularly for large depots, high polymer mass, or poorly buffered tissues.
RESOMER R 203 H occupies a specific formulation space among bioresorbable injectable polyesters. Its acid-terminated, amorphous poly(D,L-lactide) structure and 0.25–0.35 dL/g inherent viscosity support injectable depot and microparticle applications where solvent solubility, phase inversion, and moderate release duration are required. Selection between this grade and alternatives such as R 202 H, R 203, or RG 502 H should be based on measured solution viscosity, injectability force, degradation rate, and drug-release profile under standardized test conditions rather than on nominal grade descriptors alone.