| HS Code | 261696 |
| Product Name | RESOMER LR 706 S Bioresorbable L/DL-Lactide Medical Grade |
| Chemical Name | Poly(L-lactide-co-D,L-lactide) 70:30 |
| Monomer Ratio | L-lactide:D,L-lactide = 70:30 (molar) |
| Inherent Viscosity | 3.6 dL/g |
| Molecular Weight | Approximately 240,000 g/mol |
| Appearance | White to off-white granules |
| Form | Granules |
| Glass Transition Temperature | Approximately 55°C |
| Density | 1.25 g/cm³ |
| Solubility | Soluble in chloroform, dichloromethane, and tetrahydrofuran; insoluble in water |
| End Group | Ester end group |
| Biodegradability | Bioresorbable and hydrolytically degradable |
| Biocompatibility | Biocompatible |
| Storage Conditions | Store in a dry place at 2-8°C, protected from moisture |
| Manufacturer | Evonik Industries |
| Grade | Medical grade |
| Cas Number | 9051-31-4 |
| Sterility | Non-sterile |
| Application | Medical implants, drug delivery systems, and tissue engineering |
As an accredited RESOMER LR 706 S Bioresorbable L/DL-Lactide Medical Grade factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | Medical-grade RESOMER LR 706 S is supplied in a 1 g glass bottle, sealed under nitrogen and protected from moisture. |
| Container Loading (20′ FCL) | 20′ FCL loading: RESOMER LR 706 S Bioresorbable L/DL-Lactide Medical Grade palletized, shrink-wrapped, secured, kept dry, clean, and at controlled temperature. |
| Shipping | RESOMER LR 706 S is shipped as a non-hazardous, non-regulated solid. It is packaged in sealed, moisture-barrier aluminum foil bags under inert gas, placed in labeled outer drums. Transport at ambient temperature, protected from moisture, heat, and light. Not classified as dangerous goods; avoid package damage or contamination. |
| Storage | Store RESOMER LR 706 S in its original, tightly closed container in a cool, dry, well-ventilated place. Keep refrigerated at 2–8°C if recommended by the supplier. Protect from moisture, heat, light, and contamination. Keep away from oxidizing agents and ignition sources. Use clean, dry tools under inert gas where possible. Follow first-in, first-out inventory and manufacturer’s instructions. |
| Shelf Life | Recommended shelf life is 24 months when stored unopened at -20°C, protected from moisture and light. |
RESOMER LR 706 S is dissolved in dichloromethane at 0.8–2.5% w/v for oil-in-water microsphere fabrication; the selected concentration is matched to target mean particle size 20–125 µm. The dispersed phase is filtered through 0.22 µm PTFE membrane and combined with a dissolved or suspended active pharmaceutical ingredient. The continuous phase consists of poly(vinyl alcohol) with 85–89% hydrolysis at 0.25–1.0% w/v in 10 mM sodium phosphate buffer pH 7.4. Emulsification is performed with a rotor-stator disperser equipped with a 10 mm dispersing tool at 6,000–13,500 min⁻¹ for 60–180 s; the primary emulsion is monitored by optical microscopy at 400× magnification for droplet circularity and edge coalescence. Solvent extraction progresses in a jacketed hardening vessel at 20–30°C with marine impeller agitation at 500–700 rpm for 2–4 h. Hardened microspheres are collected by wet sieving through 20 µm and 125 µm stainless steel meshes, rinsed with sterile water for injection, and freeze-dried at −40°C and ≤0.01 mbar for 24–36 h.
Residual dichloromethane is measured by headspace gas chromatography with flame ionization detection and limited to 600 ppm under ICH Q3C(R8) Class 2 residual solvent requirements. Release testing includes USP <71> sterility, USP <85> bacterial endotoxin, ISO 10993-5:2009 cytotoxicity, and ISO 10993-6:2016 local effects after implantation; lactide monomer content is determined by high-performance liquid chromatography. Aseptic manufacturing under EU GMP Annex 1 is required because terminal gamma irradiation at device-relevant doses initiates chain scission in L/DL-lactide copolymers. Terminal product is a vialed injectable depot powder with mean particle size distribution 20–125 µm. The deepest process conflict is hardening kinetics: rapid solvent extraction lowers residual DCM but produces porous surface morphology, while slow extraction allows internal void collapse during freeze-drying.
Coating of magnesium-based interference screws and other resorbable osteofixation substrates uses a filtered solution of RESOMER LR 706 S at 2.0–3.5% w/v in 80:20 ethyl acetate/acetone. The substrate is cleaned with alkaline detergent, rinsed with deionized water, and activated with oxygen plasma at 13.56 MHz and 100 W for 2 min. Ultrasonic atomizer coating proceeds at 1.0–2.0 mL/h feed rate, nozzle-to-substrate distance 40–60 mm, and mandrel rotation 20–30 min⁻¹. Each pass deposits 2–4 µm; total dry thickness is held at 8–15 µm to limit swelling stress on the underlying implant surface. Samples are dried at 22±2°C in laminar flow, then vacuum-dried at 35°C for 12–16 h. Residual solvent is verified by headspace gas chromatography; the internal release limit for total residual ethyl acetate and acetone is 250 ppm. ICH Q3C(R8) classifies ethyl acetate as Class 3 with permitted daily exposure of 50 mg/day, but medical device extraction studies per ISO 10993-12:2021 must confirm patient exposure below that threshold.
Coating adhesion is evaluated with ISO 2409:2020 cross-cut on flat witness coupons; delamination greater than 5% area after immersion in phosphate-buffered saline at 37°C for 24 h is rejected. Biological evaluation follows ISO 10993-1:2018, with subchronic implantation per ISO 10993-6:2016. Terminal product is a sterile implant assembly integrated into a trauma fixation kit, not a primary structural layer. The known production bottleneck is edge coverage at thread roots and drive recesses, where film defects occur when coating viscosity exceeds 15 mPa·s at 25°C.
High molar mass L-lactide homopolymer monofilament can be modified by compounding 15–25 wt% RESOMER LR 706 S to reduce bending stiffness and modify knot security. The blend is pre-dried at 45°C under ≤10 mbar for 18–24 h; residual moisture is confirmed below 250 ppm by Karl Fischer titration. Extrusion uses a 16 mm co-rotating twin-screw extruder with L/D 25:1, barrel zones 165–185°C, and melt pressure 40–70 bar behind a 30 µm sintered metal filter. The melt exits a 0.5–1.0 mm die into a water quench bath at 18–22°C. Two-stage drawing at 3.5–4.5× is carried out in water baths at 60–75°C and 75–85°C, followed by annealing at 80°C for 6–12 h under a nitrogen sweep. Melt flow rate is monitored by ISO 1133-1:2022 at 190°C/2.16 kg for blend consistency; tensile properties are measured by ISO 527-2:2012 type 5 specimens. Knot-pull strength is determined with the USP suture test configuration at 300 mm/min crosshead speed.
The resulting monofilament diameter is 0.08–0.30 mm. Biological evaluation includes ISO 10993-1:2018, ISO 10993-5:2009, and ISO 10993-6:2016. Terminal product is a resorbable suture component. The major extrusion limitation is that higher copolymer fractions suppress melt strength; above 25 wt% LR 706 S, draw resonance at the quench bath appears as periodic diameter variation above ±8%. Published data for exact modulus loss at 25 wt% in drawn monofilament are limited, so qualification must be performed on the production line.
Drug-loaded rods are produced from RESOMER LR 706 S by hot-melt extrusion at active pharmaceutical ingredient loadings between 5 wt% and 15 wt%. Active ingredient and polymer are blended in a low-shear tumble mixer for 20–30 min at 25°C and ≤15% RH; the blend is conditioned at 35°C for 4–6 h before extrusion. A 16 mm co-rotating twin-screw extruder with L/D 40:1 is configured with kneading elements offset at 30° and 60° in the central mixing zone, with vacuum venting at −0.8 bar relative. Barrel zone temperatures are 100°C, 120°C, 130°C, and 135°C; screw speed is 100–200 rpm. Melt temperature at the die is controlled between 125°C and 145°C; residence time above 15 min at melt temperature beyond 150°C causes monomer regeneration and number-average molecular weight loss exceeding 10%. Die diameter is 1.0–2.0 mm; rods are cut to 10–30 mm lengths by a rotary cutter under dry nitrogen.
In-process measurements include melt torque, die pressure, laser diameter, and transmission Fourier-transform infrared spectroscopy for lactide monomer index. Release testing follows ISO 10993-1:2018, ISO 10993-5:2009, and ISO 10993-6:2016; for combination products, USP <71> and USP <85> apply to the finished sterile rod. Terminal product is a single-use implantable rod for local drug release. The main process conflict is simultaneous maintenance of low melt temperature and sufficient plasticization for torque at or below 5 N·m on a 16 mm extruder; above this torque, shear heating degrades the L/DL-lactide backbone and narrows the processing window.
Solvent casting of a 0.05 mm resorbable film uses RESOMER LR 706 S dissolved at 8.0–12.0% w/v in ethyl acetate. The filtered solution is degassed under 50 mbar for 15–20 min, then cast onto a PTFE-coated glass plate using a knife gap of 0.4–0.6 mm. Primary solvent removal occurs at 25°C and ≤30% RH for 12–16 h; secondary vacuum drying at 35°C and ≤5 mbar continues until residual ethyl acetate is below 500 ppm by headspace gas chromatography. The dried film is cut into 50×50 mm or 100×100 mm sheets using a rotary die. Packaging uses Tyvek/PE pouches sealed under nitrogen. Terminal sterilization at 15 kGy gamma radiation is applied; intrinsic viscosity is measured before and after sterilization according to ISO 1628-1:2021 and ISO 13781:2017.
Mechanical competence is tested by ASTM D882-18 for thin film tensile, and tear resistance is measured by ASTM D1938-19 trouser tear. Biological requirements are ISO 10993-5:2009 and ISO 10993-6:2016. The terminal product is a sterile single-use barrier film for temporary tissue separation. The process limitation is brittleness when residual solvent falls below 200 ppm; conditioning at 35–45% RH before converting prevents edge cracking and die-cut delamination.
Electrospinning of RESOMER LR 706 S from 1,1,1,3,3,3-hexafluoro-2-propanol or chloroform/dimethylformamide mixtures at 6.0–10.0% w/v produces nonwoven membranes with fiber diameter 0.4–1.5 µm. A syringe pump delivers the solution at 0.5–2.0 mL/h to a 21 G blunt needle at potential 14–20 kV; collector distance is 12–18 cm. Collector humidity is maintained at 35–45% RH because higher humidity introduces surface pore defects and lower humidity increases charge accumulation and fiber breakage. Membrane thickness is built to 0.2–0.5 mm over 3–6 h, followed by vacuum drying at 35°C for 12–18 h. Residual solvent analysis includes an internal toxicological risk assessment for HFIP, which is not assigned an ICH Q3C(R8) permitted daily exposure. Pore size is measured by mercury intrusion porosimetry with target pore size 5–20 µm; tensile screening uses ISO 527-2:2012 type 5 specimens.
Biological evaluation follows ISO 10993-1:2018, ISO 10993-5:2009, ISO 10993-6:2016, and ISO 13781:2017 for in vitro degradation. Terminal product is a resorbable fibrous membrane for dural repair. The process conflict is that single-needle productivity is below 0.2 g/h, while multi-jet arrays introduce local field interference and broaden the fiber diameter distribution beyond the range acceptable for reproducible tissue integration.
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Evonik RESOMER LR 706 S is a bioresorbable poly(L-lactide-co-DL-lactide) 70:30 medical-grade resin supplied as white to off-white granules for implantable medical devices, parenteral drug delivery systems, and controlled-release applications. The product is amorphous, with differential scanning calorimetry indicating a glass transition temperature of 55–60 °C and no crystalline melting endotherm. The manufacturer’s certificate-of-analysis specification places inherent viscosity at 2.5–3.5 dL/g when measured as a 0.1% w/v solution in chloroform at 25 °C. Residual monomer, water, and solvent are controlled to limits of 0.5%, 0.5%, and 0.1%, respectively. The 70:30 L-lactide-to-DL-lactide ratio disrupts chain stereoregularity and suppresses crystallization, producing near-isotropic mechanical behavior in molded, extruded, or cast forms. Because the polymer contains no glycolide, hydrolytic degradation releases lactic acid rather than glycolic acid. The medical-grade designation concerns purity, residual contaminant control, and supporting documentation; it does not imply that the raw granulate is sterile or that a finished device is cleared for clinical use.
| Parameter | Specified value or limit | Method or standard reference |
|---|---|---|
| Polymer composition | 70:30 L-lactide/DL-lactide | Manufacturer specification |
| Inherent viscosity | 2.5–3.5 dL/g | 0.1% w/v in chloroform, 25 °C, capillary viscometry |
| Glass transition temperature | 55–60 °C | Differential scanning calorimetry |
| Residual monomers | ≤0.5% | High-performance liquid chromatography |
| Water content | ≤0.5% | Karl Fischer titration |
| Residual solvent | ≤0.1% | Headspace gas chromatography |
| Heavy metals | ≤10 ppm | Inductively coupled plasma optical emission spectrometry |
| Tin catalyst residue | ≤200 ppm | Inductively coupled plasma optical emission spectrometry |
These values are raw-material acceptance limits and do not replace device-level specifications. In the manufacturer’s standard specification, capillary viscometry serves as the primary molecular-weight surrogate because intrinsic viscosity correlates with chain length under defined solvent and temperature conditions. Differential scanning calorimetry confirms the absence of crystallinity, while Karl Fischer titration, high-performance liquid chromatography, and headspace gas chromatography control water, residual lactide monomers, and volatile process solvents. Metal residues are limited by inductively coupled plasma optical emission spectrometry, with tin controlled separately because organotin compounds are commonly used as polymerization catalysts. Biological reactivity data according to USP 88 Class VI are often supplied within change-control documentation for medical-grade materials; however, the finished implant, drug-device combination product, or parenteral formulation still requires biological evaluation under ISO 10993-1:2018.
Compared with poly(L-lactide) homopolymer, RESOMER LR 706 S eliminates crystalline domains entirely. A PLLA homopolymer of analogous chain length typically shows a melting endotherm near 180 °C and may exhibit slower water penetration through ordered lamellae. LR 706 S, in contrast, shows only the 55–60 °C glass transition and permits hydrolytic degradation to proceed more uniformly across the polymer matrix. The absence of crystallinity reduces anisotropic mechanical behavior in injection-molded or solvent-cast parts and allows solvent removal or shaping at lower temperatures than semicrystalline PLLA. Compared with poly(lactide-co-glycolide) copolymers containing glycolide, LR 706 S degrades more slowly because the lactide backbone is more hydrophobic, and hydrolysis releases lactic acid rather than glycolic acid. This difference can moderate the local pH drop observed with glycolide-rich PLGA devices, although the magnitude is formulation-dependent.
Within the L/DL-lactide LR series, the 706 S code occupies a mid-viscosity position. Lower-viscosity grades are used when dilute solution injection, fine droplet formation, or reduced melt pressure is required. Higher-viscosity grades are selected where greater mechanical strength and longer degradation are primary requirements. The 2.5–3.5 dL/g inherent viscosity range of LR 706 S therefore supports a compromise between solution processability, melt extrusion behavior, and controlled-release control in extended-release systems. The chemical composition remains constant across the LR series; the principal difference between adjacent LR grades is molecular weight, not lactide stereochemistry or monomer ratio.
For oil-in-water microsphere fabrication, the polymer is dissolved in a volatile organic solvent at concentrations typically in the 5–20% w/v range; dichloromethane and ethyl acetate are common process solvents. The organic phase is emulsified into an aqueous continuous phase containing a stabilizer such as polyvinyl alcohol, after which solvent extraction and evaporation harden the particles. The inherent viscosity range of 2.5–3.5 dL/g directly influences organic-phase viscosity and droplet breakup in rotor-stator, static mixer, or membrane emulsification systems. Higher viscosity shifts particle size upward at fixed impeller speed, while lower viscosity can produce finer droplets but may reduce encapsulation efficiency for lipophilic actives. Dynamic viscosity of LR 706 S solutions is not provided as a single-point universal value, so formulation-specific rheology measurements under design-of-experiment methodology are required during scale-up. Residual solvent content in finished microspheres is controlled by gas chromatography and must comply with ICH Q3C or USP 467 residual solvent limits for the finished dosage form.
Residual moisture becomes a critical process variable when hot-melt extrusion is selected for drug-eluting implant or pellet manufacture. The certificate-of-analysis upper limit for water is 0.5% w/w; exceeding this value before melt processing can initiate hydrolytic chain scission and reduce molecular weight during extrusion. The amorphous granules are therefore vacuum-dried below the 55–60 °C glass transition temperature, typically in a vacuum oven at pressures below 10 mbar, until the water limit is restored. Twin-screw extruders with L/D ratios from 25:1 to 40:1 are commonly used for dispersing heat-sensitive active pharmaceutical ingredients into the polymer matrix. The mid-range viscosity of LR 706 S raises melt pressure relative to lower-IV grades, and strand pelletizing may require water bath temperatures below 25 °C to prevent strand tackiness.
Batch-to-batch variation within the 2.5–3.5 dL/g specification can shift melt pressure, torque, and strand diameter. Production-scale operators commonly adjust barrel temperature set points by 5–10 °C or modify screw speed to maintain strand geometry and pellet quality. Prolonged exposure at elevated melt temperatures promotes thermal degradation of the aliphatic ester backbone, so screw configuration, barrel residence time, and specific mechanical energy input must be controlled. Capillary rheometry at controlled residence time is more informative for this material than ISO 1133-1:2022 melt flow rate testing, because standard melt flow test temperatures may introduce degradation during the measurement itself. The amorphous nature of the copolymer also means that no semicrystalline reinforcement masks early thermal or hydrolytic damage, so viscosity reduction during processing is detected more directly in torque and die pressure trends.
Gamma irradiation at doses commonly used for terminal sterilization, such as 25 kGy, can reduce molecular weight and alter mechanical behavior through chain scission. Dose-setting studies under ISO 11137 should therefore include post-irradiation viscosity, strength, or degradation profiling from the final device geometry rather than from raw granulate alone. Ethylene oxide processing may require elevated humidity and temperature; for LR 706 S, the amorphous glass transition of 55–60 °C limits practical chamber temperature if shape distortion is to be avoided during sterilization. Steam autoclaving is generally unsuitable for this polyester because moisture and high temperature accelerate ester hydrolysis. Published data on terminal sterilization of LR 706 S in specific implant geometries is limited; cycle development is device-specific and cannot be inferred from raw-material stability data alone.
Medical-grade status is supported by supply under a quality management system certified to ISO 13485:2016; it is not conferred by raw-material certification alone. Biological evaluation of the finished device follows ISO 10993-1:2018, and the polymer may be tested according to USP 88 Biological Reactivity Tests for Class VI plastics. Cytotoxicity, sensitization, implantation, and systemic toxicity endpoints are evaluated on the final product because processing residues, sterilization changes, and geometric factors can alter biological response. Residual tin catalyst is controlled at ≤200 ppm and heavy metals at ≤10 ppm to limit extractable metal burden. Residual monomer and solvent limits are specific to the medical grade and must be considered alongside finished-product monographs or ICH Q3C residual solvent guidance when solvent-based processing is used.
Storage conditions materially affect process repeatability. The granules are supplied in sealed packaging intended to exclude humid air. At relative humidity above 60%, moisture uptake can exceed the certified 0.5% water limit and require re-drying before melt processing. The polymer should not be held in aqueous media above pH 7 for prolonged periods before intended resorption, because alkaline conditions accelerate ester hydrolysis and can reduce molecular weight unpredictably. These constraints apply to raw material handling and to intermediate manufacturing steps such as aqueous emulsion hardening or buffer exposure during coating.
Production-scale handling on hot-melt extrusion lines has shown that the amorphous granules can become tacky when exposed simultaneously to warmth and humidity; sealed storage and controlled room-temperature handling are therefore part of the standard material procedure. In solvent-based microsphere processes, batch-to-batch variation within the 2.5–3.5 dL/g specification can shift particle size distribution if emulsification speed or organic-phase concentration is not adjusted for the actual certificate-of-analysis viscosity. The final application of RESOMER LR 706 S as a bioresorbable L/DL-lactide medical product depends on device configuration, sterilization modality, drug-polymer interaction, and regulatory submission; no single processing cycle defines the material across all applications.