| HS Code | 487429 |
| Product Name | Prefillable Syringes Pharma Grade API for Tablet / Capsule / Granule / Injection, Oral & Injectable |
| Product Category | Pharmaceutical-grade prefillable syringe and API delivery component |
| Material | Pharma-grade glass or cyclic olefin polymer |
| Barrel Type | Clear or amber |
| Capacity Range | 0.5 mL to 50 mL |
| Sterilization Method | Ethylene oxide or gamma irradiation |
| Grade | Pharma Grade |
| Api Compatibility | Compatible with tablet, capsule, granule, oral, and injectable API formulations |
| Route Of Administration | Oral and injectable |
| Dosage Form Support | Tablet, capsule, granule, and injection |
| Closure System | Luer lock, luer slip, or staked needle |
| Needle Type | Fixed or removable |
| Plunger Type | Elastomeric stopper with lubricant coating |
| Fill Volume Accuracy | ±1% to ±5% |
| Regulatory Compliance | USP Class VI, ISO 11040, and cGMP |
| Shelf Life | 24 to 36 months |
| Storage Conditions | Controlled room temperature, protected from light |
| Packaging | Nest and tub or blister tray |
| Biocompatibility | Non-pyrogenic and non-cytotoxic |
| Leachables And Extractables | Low extractables and leachables profile |
As an accredited Prefillable Syringes Pharma Grade API for Tablet / Capsule / Granule / Injection, Oral & Injectable factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | For oral and injectable pharma-grade API: sterile prefillable syringes, 100 per tamper-evident, temperature-controlled, pharmaceutical-grade carton with protective outer packaging. |
| Container Loading (20′ FCL) | 20′ FCL container loading of pharma-grade prefillable syringes/API for tablets, capsules, granules, oral and injectable use; securely packed, temperature-controlled, compliant. |
| Shipping | Ship in validated, temperature-controlled packaging (typically 2–8°C) with data loggers, shock protection, and light-resistant secondary containment. Maintain sterile integrity, tamper-evident seals, and GDP/GMP compliance. Include batch, MSDS/SDS, and chain-of-custody documentation. Handle as pharmaceutical API; avoid freezing, extreme heat, and delays. Use qualified couriers and monitor excursions. |
| Storage | Store in original, sealed, light-resistant containers at controlled room temperature (15–25°C), protected from moisture, direct sunlight, and contamination. Keep dry, well-ventilated, and away from incompatible materials, oxidizers, and ignition sources. Store upright; do not freeze unless manufacturer specifies. Do not use if packaging is damaged. Maintain segregation by grade/status and follow label, SDS, and GMP requirements. Use first-in, first-out inventory. |
| Shelf Life | Shelf life typically 24–36 months when stored sealed in original packaging under recommended conditions; protect from light, heat, and moisture. |
For the prefillable-syringe-compatible API grade in direct compression of a 12.0 wt% API-loaded tablet without prior granulation, the API particle-size distribution is controlled within a D90 of 180 µm and a fines fraction below 15.0 %. The API is passed through a 710 µm stainless-steel mesh and preblended with microcrystalline cellulose PH102 at a 1:4 ratio in a 600 L bin blender operating at 12 rpm for 8 minutes. The preblend is then charged with croscarmellose sodium at 2.0 wt%, colloidal silicon dioxide at 0.5 wt%, and magnesium stearate at 0.5 wt%; total blend time is limited to 15 minutes because lubrication beyond 18 minutes increases tablet disintegration time above 180 seconds in USP <701> testing. Compression is run on a 45-station rotary press at a main compression force of 12–18 kN, targeting tablet hardness of 70–100 N and friability below 0.8 wt% after 100 revolutions. Batch records specify a weight variation limit of ±5.0 % for average tablet weight and individual dosage unit uniformity per USP <905>. Dissolution acceptance is set at Q=80 % in 30 minutes using USP <711> Apparatus 2 at 50 rpm in 900 mL of 0.1 M hydrochloric acid. ICH Q3D elemental impurity risk assessment and residual solvent limits under USP <467> are applied to the API release before compression. The terminal product is a film-coated immediate-release tablet, finished with an aqueous film-coating dispersion at 3.0 wt% weight gain and pan bed temperature of 45 °C.
Low-dose encapsulation below 5.0 mg per unit is treated as a pharmaceutical mixing problem rather than a flow problem. The API is geometrically diluted in a 1:10, 1:10, 1:10 sequence with lactose monohydrate 200M to reach a final API concentration of 0.1–1.0 wt%. Sodium stearyl fumarate at 0.5 wt% is preferred over magnesium stearate because its hydrophobicity is lower and disintegration time drift in HPMC capsules is reduced. The final blend is screened through a 355 µm sieve and loaded into a dosator-type capsule filler with powder bed depth held at 50–60 mm. Dosator compression plates are set to a plug compression stroke of 3–5 mm; lower stroke values generate weight variability above 7.5 % RSD, while higher values cause plug retention in the dosator tip. Capsule bodies are filled to a target net fill weight of 220–260 mg for size 1 HPMC shells conditioned at 40 % RH for 2 hours. In-process checks are taken every 15 minutes for weight variation; acceptance is ±5.0 % for average fill weight and not more than two of twenty capsules outside 5.0 % deviation per 21 CFR 211.110. Disintegration is monitored with USP <701> using water at 37 °C, with a limit of NMT 15 minutes for uncoated HPMC capsules. The terminal product is a two-piece HPMC capsule, banded with a 30 % w/v gelatin solution at 60 °C to prevent tampering and seal moisture ingress.
In fluid-bed granulation campaigns, the API is loaded at 25.0–45.0 wt% into a top-spray conical granulator with a 1200 L bowl and 1500 m³/h inlet airflow. A 5.0 wt% povidone K30 solution in purified water is sprayed at 10–14 g/min/kg of dry blend through a 1.2 mm two-fluid nozzle atomized at 2.0 bar. Inlet air temperature is set to 65 °C, product temperature is maintained at 35–38 °C, and dew point is controlled below 5.0 °C to prevent over-wetting. Endpoint is defined by a loss-on-drying value of 1.8–2.5 wt% and a granule D50 of 150–220 µm measured by laser diffraction according to USP <429>. The wet granules are dried until moisture is below 2.5 wt%, then milled through a 1.0 mm conical screen at 1,200 rpm. Fines below 75 µm are limited to 10.0 wt% to prevent downstream tablet lamination. Granules are mixed with extragranular disintegrant at 2.0 wt% and lubricant at 0.25 wt% for 5 minutes. The terminal product is either a 500 mg single-dose sachet filled by auger filler with a fill-weight RSD below 3.0 %, or a compression-grade granule that is tableted into sustained-release matrices after coating with ethylcellulose 7FP at 10.0 wt% solids in anhydrous ethanol. Release acceptance for the sachet is Q=85 % in 30 minutes by USP <711> Apparatus 2 at 50 rpm in pH 6.8 phosphate buffer.
| Dosage form | Critical process control | Reference method | Release or in-process target |
|---|---|---|---|
| Direct compression tablet | Blend particle size and compression force | USP <429> / USP <905> | D90 ≤ 180 µm, hardness 70–100 N |
| Dosator capsule fill | Plug stroke and powder bed depth | 21 CFR 211.110 / USP <701> | Fill weight RSD ≤ 5.0 %, disintegration NMT 15 min |
| Top-spray fluid-bed granule | Product temperature and loss on drying | USP <429> / USP <921> | D50 150–220 µm, LOD 1.8–2.5 wt% |
A sterile injectable presentation is prepared by dissolving the API at 20.0–50.0 mg/mL in Water for Injection together with mannitol at 4.0 wt% and sodium chloride at 0.9 wt% as crystallizing bulking agents. Aseptic processing follows 21 CFR 210 and 21 CFR 211. The solution pH is adjusted to 4.5–5.5 with 0.1 M hydrochloric acid or 0.1 M sodium hydroxide only after the API is fully dissolved, because direct pH adjustment during mixing produces local supersaturation and amorphous precipitate. The formulation is filtered through a 0.22 µm PVDF membrane cartridge at 1.0–1.5 L/min and filled into 10 mL molded vials with a fill volume of 3.0–5.0 mL. The lyophilization cycle uses a freeze ramp of 0.5 °C/min to -45 °C, an annealing hold at -20 °C for 2 hours, primary drying at -25 °C shelf temperature and 0.150 mbar chamber pressure for 24 hours, and secondary drying at 40 °C for 4 hours. Product temperature is monitored with thermocouples placed at the center bottom of each vial; if the product exceeds the collapse temperature by more than 2.0 °C, the batch is rejected for collapsed cake structure. Residual moisture acceptance is NMT 1.0 wt% by Karl Fischer titration per USP <921> Method Ia. Reconstitution time is required to be less than 60 seconds with 5.0 mL of Sterile Water for Injection. Parenteral release includes endotoxin NMT 0.20 EU/mg per USP <85> and subvisible particulate counts per USP <788>. The terminal product is a lyophilized injectable cake sealed with bromobutyl stoppers under vacuum, intended for single-dose vial reconstitution. When transferred into a dual-chamber prefillable syringe, the lyophilized cake is paired with a 2.0 mL diluent chamber and a bypass stopper meeting ISO 11040-4:2015 barrel dimensions.
Prefillable syringe filling requires the API to be evaluated for extractable spallation, silicone oil droplet growth, and subvisible particle evolution over 24 months at 25 °C / 60 % RH. For a solution formulation, the API is dissolved at 10.0–30.0 mg/mL in a buffer system of 10 mM sodium citrate pH 5.0 with 0.9 % w/v sodium chloride and 0.01 % w/v polysorbate 80. The solution is passed through a 0.22 µm polyethersulfone filter and filled under ISO 5 in-line conditions into 1.0 mL long glass barrels with glued needle, using a rotary piston pump with a fill volume tolerance of ±1.0 % and nitrogen overlay at 0.5 L/min. Stopper insertion is performed under vacuum with a plunger rod retraction of 1.5–2.5 mm to minimize bubble height. Silicone oil applied to the barrel interior is controlled at 0.4–0.8 mg per barrel because levels above 1.0 mg produce subvisible silicone droplets that interfere with USP <788> light obscuration particle counting. Gliding force is measured on a texture analyzer at 100 mm/min and must remain below 25 N for a 23G thin-wall needle. Terminal sterilization is allowed only when the API shows no degradation at 121 °C for 15 minutes in a saturated steam autoclave; otherwise aseptic filtration is used without terminal heat. Published data for this specific API under terminal moist-heat conditions is limited; the sterilization decision therefore requires forced-degradation data generated in the intended buffer system. The terminal product is a single-dose prefillable syringe used directly in emergency or chronic injection settings, with closure integrity tested by dye ingress per 21 CFR 211.94 and dimensional checks per ISO 11040-4:2015.
Typically, an oral suspension containing the same API is compounded when solid dosage forms are unsuitable for pediatric or geriatric administration. The API is dispersed at 10.0 mg/mL in a 20 mM citrate buffer pH 4.5 containing 0.30 wt% xanthan gum, 1.20 wt% microcrystalline cellulose-carboxymethyl cellulose co-processed stabilizer, 20.0 wt% sorbitol, and 0.10 wt% sodium benzoate. The aqueous phase is hydrated in a vacuum mixer at 800 rpm for 30 minutes before API addition; the API is prewetted with 10.0 wt% propylene glycol to prevent aggregation, then incorporated under high shear at 3,000 rpm for 15 minutes. The suspension is deaerated at -0.8 bar for 10 minutes and passed through a 0.3 mm sieve to remove agglomerates. Viscosity is adjusted to 100–300 mPa·s at 25 °C measured with a Brookfield RVT spindle 2 at 50 rpm; values below 80 mPa·s cause rapid sedimentation, while values above 400 mPa·s prevent acceptable pourability. Sedimentation volume is monitored at 24 hours and resuspendability is tested by 10 manual inversions. The terminal product is a 100 mL amber PET bottle with child-resistant closure, filled to 105.0 % of labeled volume. Release criteria include assay, pH 4.2–4.8, preservative efficacy per USP <51>, and absence of visible mold growth.
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Prefillable syringe compatible pharma-grade active pharmaceutical ingredient (API) for tablet, capsule, granule, oral, and injectable formulation is supplied as a multi-compendial material produced under current good manufacturing practice. The material is specified for residual solvents per ICH Q3C, elemental impurities per ICH Q3D, microbial enumeration per USP <61>, specified microorganisms per USP <62>, and bacterial endotoxins per USP <85>. The API is intended for direct compression and wet granulation tableting, hard-shell capsule filling, granule and oral suspension manufacture, oral solution compounding, and sterile injectable solution or suspension filling into prefilled syringes. The product scope includes staked-needle and needle-free syringe formats, with barrel dimensions selected from 1 mL long, 2.25 mL, 5 mL, and 10 mL nominal volumes where the container system conforms to ISO 11040-4:2015 for glass or ISO 11040-6:2012 for plastic.
Container closure model selection is assigned at the syringe system level rather than as a single catalogue number. Glass barrels are Type I borosilicate, and plastic barrels are typically cyclic olefin polymer or polypropylene. Plunger stoppers are chlorobutyl or bromobutyl elastomer, either uncoated or fluoropolymer-laminated, and are qualified against USP <381> and Ph. Eur. 3.2.9. Staked needles, where present, are low-tungsten designs to limit tungsten extractables that can appear as subvisible particles after filling and storage. The tip closure is either an elastomeric tip cap or a rigid cap with elastomeric liner, selected to maintain sterility and container closure integrity under transportation and low-temperature storage.
For tablet and capsule manufacture, the API is processed by direct compression or high-shear wet granulation. On production-scale rotary tablet presses, the blend is characterized before compression using particle size distribution by laser diffraction per USP <429>, bulk and tapped density per USP <616>, and flow through an orifice per USP <1174>. Compaction behavior is evaluated with an instrumented press or compaction simulator to detect capping and lamination risks. Capsule filling on intermittent-motion dosator or tamping-pin machines requires control of powder bed height and stratified blend sampling. Granulation endpoint is controlled by loss on drying per USP <731> and Karl Fischer titration per USP <921>; the dried granule is milled and sieved using USP <786> analytical sieving.
Blend uniformity is assessed according to USP <905> and dissolution according to USP <711> with apparatus selected for the dosage form. Because oral solid dosage forms do not require depyrogenation or sterility, oral-grade material may be produced on multiproduct equipment with cleaning validation appropriate to the lower microbiological risk. The injectable grade, by contrast, is manufactured in dedicated equipment or in validated multiproduct campaigns with cleaning verification per ICH Q7 and 21 CFR 211.67.
For granule and oral suspension manufacture, the API is wet-massed with a binder solution in a high-shear mixer or fluid-bed granulator. Spray rate, inlet air temperature, and atomization pressure are adjusted to prevent overwetting and API migration. The dried granule is milled and sieved; residual moisture is controlled by loss on drying per USP <731> and Karl Fischer titration per USP <921>. Sachet fill weights are verified with in-process checkweighers, and final blend uniformity is assessed by stratified sampling. Published data for this specific configuration is limited.
For oral solutions, the API is dissolved in a suitable solvent system, and pH is adjusted to maintain solubility and stability. Preservative effectiveness is tested per USP <51> where applicable. Homogeneity is verified by sampling from top, middle, and bottom of the mixing vessel. The oral liquid process does not require sterility, but bioburden is controlled to acceptance criteria based on the intended route.
The injectable grade is differentiated by low bioburden, absence of specified microorganisms, controlled endotoxin content, particulate matter limits per USP <788> or USP <787> as applicable, and elemental impurity limits calculated by ICH Q3D Option 1. Residual solvents are limited per ICH Q3C, with Class 1 solvents controlled at the following concentrations: benzene 2 ppm, carbon tetrachloride 4 ppm, 1,2-dichloroethane 5 ppm, 1,1-dichloroethene 8 ppm, and 1,1,1-trichloroethane 1500 ppm. An oral-grade API may not carry endotoxin, particulate, or sterility specifications because the final dosage form is not presented as a parenteral. Substitution of oral-grade material into an injectable process would violate 21 CFR 211.84 because the material would not have been tested against the quality attributes appropriate for its intended use.
Compared with uncoated elastomer plunger stoppers, fluoropolymer-laminated stoppers reduce leachable zinc and sulfur species and often lower visible particle counts in stability studies. However, the laminate can shift break-loose and glide force profiles. Mechanical testing is therefore performed on the finished syringe according to ISO 11040-8:2016. Break-loose force and glide force are measured using a constant-rate tensile/compression tester with a load cell appropriate to the expected force range; acceptance criteria are product-specific and are established during design verification. Published data for this specific configuration is limited, so universal numeric values are not applicable.
Prefilled syringe systems introduce contact materials that are not present in glass vials: silicone oil, elastomer stoppers, tip cap rubbers, tungsten residues from needle insertion, and potential adhesive or ink components. Extractables screening is conducted per USP <1663> using extraction solvents matched to the formulation polarity and exaggerated temperatures, such as 40 °C for 30 days or 50 °C for 7 days. Leachables testing is then performed per USP <1664> on stability samples. The analytical evaluation threshold is derived from the safety concern threshold or permitted daily exposure; published data for this specific configuration is limited, so the threshold is calculated case-by-case.
Silicone oil can be detected as subvisible droplets by flow imaging, and tungsten residues can appear as discrete particles if low-tungsten needles are not used. On high-speed filling lines, silicone oil redistribution after autoclaving can produce visible droplet rings at the barrel shoulder; this is controlled by validated silicone oil application and curing before filling. Fluoropolymer-laminated stoppers reduce extractables compared with uncoated elastomers, but may require different insertion vacuum settings to avoid bubble formation or stopper deformation. Stopper insertion speed and vacuum level are adjusted during engineering runs to keep residual bubble size below the reject limit established for the product.
For injectable solution preparation, the API is dissolved in Water for Injection, pH adjusted, and filtered through a 0.22 µm rated membrane. Filter integrity is tested before and after filling with a bubble point or diffusive flow method per ASTM F838-20 or equivalent. The solution is filled aseptically on a rotary piston or peristaltic pump line inside a restricted access barrier system or isolator. Fill volume is verified by in-process checkweighing, and visible particles are controlled according to USP <790>. Subvisible particulate matter is measured per USP <788>; for containers not greater than 100 mL, the light obscuration limits are not more than 6000 particles per container at ≥10 µm and not more than 600 particles per container at ≥25 µm.
Terminal sterilization of a prefilled syringe is considered only when the API demonstrates degradation below the specification threshold under moist heat at 121 °C for 15 min. Silicone oil redistribution and plunger stopper compression set are evaluated after autoclaving. For heat-sensitive formulations, aseptic filtration and filling are required. Container closure integrity is tested per USP <1207> using deterministic methods such as vacuum decay or helium leak. The test must demonstrate no breach of the sealed syringe across the intended shelf life, including after thermal cycling and drop testing.
On an aseptic filling line, batch-to-batch variance in stopper coating thickness can produce a bimodal distribution of break-loose force. Production-scale failure modes include syringe tip cap pop-off during vacuum leak testing, needle shield misalignment, and silicone oil droplet accumulation at the barrel shoulder after terminal sterilization. These are addressed with incoming component dimensional inspection per ISO 11040-4:2015 and ISO 11040-5:2012, and with periodic force testing on a tensile/compression tester. In-process rejection of visible particles is recorded by automated inspection; recurrent rejection spikes require investigation of stopper lot, needle lot, and silicone oil application conditions.
The API is released by HPLC assay under a validated method per ICH Q2(R1), with system suitability requirements for resolution, tailing, and replicate injection precision. Impurities are controlled at reporting, identification, and qualification thresholds per ICH Q3A. Enantiomeric or polymorphic form is controlled where relevant by X-ray powder diffraction or chiral HPLC. Residual solvents are determined by headspace gas chromatography. Elemental impurities are determined by inductively coupled plasma mass spectrometry per ICH Q3D.
| Requirement | Standard / method | Controlled parameter or acceptance basis |
|---|---|---|
| Residual solvents | ICH Q3C | Class 1 limits: benzene 2 ppm, carbon tetrachloride 4 ppm, 1,2-dichloroethane 5 ppm, 1,1-dichloroethene 8 ppm, 1,1,1-trichloroethane 1500 ppm |
| Elemental impurities | ICH Q3D Option 1 | Parenteral PDE: As 15 µg/day, Cd 2 µg/day, Pb 5 µg/day, Hg 3 µg/day |
| Particulate matter in injections | USP <788> | For containers ≤ 100 mL: ≥10 µm ≤ 6000 per container; ≥25 µm ≤ 600 per container |
| Bacterial endotoxins | USP <85> | Limit = K/M; K = 5 EU/kg for intravenous except intrathecal, which uses 0.2 EU/kg |
| Sterility | USP <71> | No microbial growth after 14 days incubation |
| Container closure integrity | USP <1207> | Deterministic leak method; no leak path exceeding product-specific limit |
| Elastomeric closures | USP <381> | Physicochemical and biological tests; turbidity and pH shift controlled |
| Glass barrels | ISO 11040-4:2015 | Dimensional, hydrolytic resistance, and internal pressure performance |
| Element | Oral PDE (µg/day) | Parenteral PDE (µg/day) | Inhalation PDE (µg/day) |
|---|---|---|---|
| Arsenic | 15 | 15 | 2 |
| Cadmium | 5 | 2 | 2 |
| Lead | 5 | 5 | 5 |
| Mercury | 30 | 3 | 1 |
Stability studies for the prefillable syringe product are conducted under ICH Q1A(R2) conditions: 25 °C/60% RH for room temperature storage, 40 °C/75% RH for accelerated, and 5 °C or -20 °C for refrigerated or frozen products. Test intervals include initial, 3, 6, 9, and 12 months, followed by annual intervals. The syringe may be stored tip-up or tip-down to detect orientation-dependent leachables or silicone oil migration. Published data for this specific configuration is limited.
Relative to a standard vial-and-stopper presentation, the prefilled syringe format eliminates a transfer step at point of administration and reduces dose measurement variability, but it adds contact with silicone oil and a narrower container closure geometry. Compared with oral tablet or capsule grades, the injectable grade requires depyrogenation, particulate and endotoxin controls, and more extensive stability testing under ICH Q1A(R2) and ICH Q5C as applicable. Compared with a syringe supplied empty for clinical use, the prefilled system is regulated as a drug-device combination product in some jurisdictions and must address extractables, leachables, and device functional performance. The material is not interchangeable with technical-grade or oral-grade API unless the container closure and route-specific quality attributes are met.