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Brombutyl rubber stopper for Injectable sterile powder Pharma Grade API for Tablet / Capsule / Granule / Injection, Oral & Injectable

    • Product Name: Brombutyl rubber stopper for Injectable sterile powder Pharma Grade API for Tablet / Capsule / Granule / Injection, Oral & Injectable
    • Factroy Site: Yudu County, Ganzhou, Jiangxi, China
    • Price Inquiry: sales10@sinochem-nanjing.com
    • Manufacturer: Ascent Petrochem Holdings Co., Limited
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    Specifications
    HS Code 156983
    Product Name Bromobutyl Rubber Stopper for Injectable Sterile Powder Pharma Grade API
    Material Bromobutyl rubber
    Polymer Type Brominated isobutylene-isoprene rubber
    Pharma Grade Pharmaceutical grade
    Primary Application Injectable sterile powder
    Dosage Forms Tablet, Capsule, Granule, Injection, Oral, Injectable
    Route Of Administration Oral and injectable
    Closure Type Rubber stopper
    Sterilization Method Autoclave, gamma irradiation, ethylene oxide
    Color Grey, black, or custom
    Hardness 45-55 Shore A
    Density 1.10-1.20 g/cm³
    Temperature Range -40°C to 121°C
    Chemical Resistance Good against water, acids, bases, and alcohols
    Needle Penetration Good
    Self Sealing Yes
    Fragmentation Low
    Extractables Low
    Moisture Absorption Low
    Barrier Properties High gas and moisture barrier
    Compliance USP Class VI, EP, ISO 10993
    Certification ISO 9001, ISO 13485, FDA DMF
    Endotoxin Low
    Pyrogenicity Non-pyrogenic
    Sterility Sterile or non-sterile available
    Packaging Clean room packaged in polyethylene bags
    Shelf Life 5 years
    Storage Conditions Cool, dry, away from sunlight

    As an accredited Brombutyl rubber stopper for Injectable sterile powder 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 & Storage
    Packing Brombutyl rubber stoppers for injectable sterile powder are packaged 10,000 pieces per double PE bag, sealed aluminum foil, pharma-grade carton.
    Container Loading (20′ FCL) 20′ FCL container loading for pharma-grade bromobutyl rubber stoppers for injectable sterile powder, oral, tablet, capsule, granule, and injection use.
    Shipping Bromobutyl rubber stoppers are shipped in double polyethylene bags, packed in sealed, clean, dry, shock-resistant cartons or drums. Transport at 15–30°C, protected from sunlight, moisture, ozone, oils, and odors. Not classified as dangerous goods. Maintain pharma-grade hygiene and keep sealed until cleanroom use.
    Storage Bromobutyl rubber stoppers should be stored in a clean, dry, well-ventilated area at 15–30°C, away from direct sunlight, moisture, heat, ozone, oils, solvents, acids, and oxidizing agents. Keep in original sealed, unopened packaging to preserve sterility and pharmaceutical quality. Maintain relative humidity below 65%, avoid compressed stacking, and follow first-in, first-out. Inspect packaging before use; discard if damaged or contaminated.
    Shelf Life Typically 5 years from manufacture if stored sealed, dry, at controlled room temperature, protected from light, moisture, and contamination.
    Application of Brombutyl rubber stopper for Injectable sterile powder Pharma Grade API for Tablet / Capsule / Granule / Injection, Oral & Injectable

    Across freeze-dried injectable sterile powder fill-finish suites filling thermolabile APIs into 10R or 20R Type I borosilicate vials, bromobutyl rubber stoppering is processed in the vent-open position through primary drying to permit water vapor egress from the lyophilised cake. The stopper formulation is a bromobutyl elastomer with a bromine content of 1.5–2.5 wt%, filler loading between 50 phr and 80 phr of calcined kaolin or precipitated silica, and a sulfur or zinc oxide cure system at 0.5–2.0 phr. A silicone lubricating film is applied after WFI washing and depyrogenation; the coating level is controlled at 0.2–0.6 mg polydimethylsiloxane per stopper to balance feed consistency against particulate release. On rotary filling lines, stopper feeding jams are observed when the silicone coating drops below 0.2 mg, while coating above 0.6 mg increases subvisible particles in the drug product. Compliance for the elastomer includes USP <381>, USP <382>, EP 3.2.9, ISO 8871-1, and ISO 8871-2, with extractables profiling aligned to ICH Q3D. The lyophilization cycle requires shelf temperature ramp from -40 °C to +25 °C at chamber pressure 0.1–0.2 mbar, after which the shelves collapse to set the stopper into the vial neck. Compression set of the bromobutyl compound is typically below 20% after 22 h at 70 °C per ISO 815-1, maintaining container closure integrity between 2–8 °C storage and uncontrolled air freight. Residual cake moisture is determined by coulometric Karl Fischer per USP <921> Method Ic and is kept between 0.5% and 2.0%; values below 0.3% risk brittle cake collapse, while values above 2.5% shorten shelf life for hydrolysis-sensitive actives. The terminal product is a single-dose sterile powder for reconstitution with water for injection or sodium chloride 0.9% injection.

    What Limits Needle Resealing in Multi-Dose Lyophilized Vials After Repeated 21G Piercing?

    Repeated penetration of a multi-dose lyophilized vial with 21G or 22G needles creates the dominant reseal challenge for the bromobutyl stopper. Resealability is assessed using the self-sealing procedure in USP <381> or a validated method derived from ISO 8871-2; the closure must withstand a defined number of piercings without visible coring, leakage, or fragmentation under a specified vacuum. Closure compression is set at 18–25% of the stopper plug diameter, and the headspace-to-fill-volume ratio is maintained between 0.8:1 and 1.2:1 to limit moisture transfer from the elastomer into the lyophilized powder. The bromobutyl compound is selected for low gas permeability; oxygen transmission through butyl-type elastomers is approximately one-tenth that of natural rubber, but published data for this specific configuration is limited and should be confirmed on the actual vial/stopper combination with a calibrated headspace analyzer. The rubber plug is silicone-coated at 0.1–0.3 mg per stopper to reduce needle friction and stopper-to-stopper adhesion during bowl feeding. Capping is performed with an aluminium flip-off seal after stopper seating; crimp diameter is verified against the 20 mm neck finish at a sampling rate of 1 vial per 15 min per capping head. The terminal product is a multi-dose powder for injection containing an anti-infective or antiviral API, reconstituted with 5 mL to 20 mL diluent per vial.

    StandardTest focusApplication condition
    USP <381>Physicochemical, fragmentation, self-sealingElastomeric closures for injections
    USP <382>Functional suitabilityPackage integrity and pierceability
    EP 3.2.9Rubber closures for aqueous parenteralsExtractables and reducing substances
    ISO 8871-1Extractables in aqueous autoclavatesPreparation class for sterilised closures
    ISO 8871-2FragmentationVisible particles after piercing
    ICH Q3DElemental impuritiesParenteral daily exposure limits

    During direct compression of a low-dose pharma grade API into immediate-release tablets on a rotary press, blend uniformity is governed by the API particle size distribution, agglomerate control, and shear history in the blender. A model formulation contains 1.0–5.0% w/w API, 40–60% microcrystalline cellulose, 30–50% spray-dried lactose monohydrate, 2–5% croscarmellose sodium, and 0.5–1.5% sodium stearyl fumarate; magnesium stearate is limited to ≤ 0.5% where dissolution slowdown is observed. Blending is performed in a bin blender at 15–25 rpm for 10–20 min, followed by compression with precompression force 5–8 kN and main compression 8–16 kN. Tablet breaking force is targeted at 60–90 N with friability ≤ 1.0% per USP <1216>; content uniformity follows USP <905> and dissolution follows USP <711>. Segregation risk increases when the API content is below 1.0% w/w, requiring ordered mixing or wet granulation. The terminal product is a film-coated immediate-release tablet.

    Roller Compaction Ribbons, Milled Granule Flow, and Capsule Fill Weight Control

    Capsule filling with roller-compacted granules of a moderately cohesive pharma grade API is selected when direct compression cannot provide adequate flow for high-speed encapsulation. The dry granulation route uses 5–20% w/w API, 30–50% microcrystalline cellulose, 10–20% anhydrous dicalcium phosphate, 10–15% pregelatinized starch, 3–5% crospovidone, and 0.5–1.0% magnesium stearate. Hydraulic roll pressure is set between 6 kN/cm and 10 kN/cm with roll speed 3–8 rpm; ribbon density is monitored at 1.05–1.25 g/cm³ and milled through a 0.8–1.25 mm screen. The milled granule is encapsulated on a dosator or dosing-disc machine at 60,000–100,000 capsules/h; fill weight variation is maintained at ≤ ±5% for size 3 capsules. Compliance includes USP <1174> powder flow, USP <905>, USP <711>, and ICH Q3D. The terminal product is a hard gelatin or HPMC capsule containing 25 mg to 100 mg API per unit.

    A top-spray fluid-bed granulation suite producing oral granules for sachets or suspension reconstitution handles a high-dose pharma grade API with aqueous binder addition. The granulation charge contains 20–40% w/w API, 40–60% lactose monohydrate, 10–20% maize starch, 2–5% povidone K30 as binder, and 0.5–1.0% colloidal silicon dioxide. Inlet air temperature is controlled at 60–70 °C, product temperature at 32–40 °C, spray rate at 15–30 g/min/kg bed mass, and atomization pressure at 1.2–2.0 bar. Granulation endpoint is determined by loss on drying at 1.5–2.5% and by torque or near-infrared moisture monitoring; wet mass is sieved through 0.8–1.6 mm mesh and dried to final moisture ≤ 2.0%. Compliance is shown by USP <905>, USP <711>, and ICH Q3D. The terminal product is a single-dose sachet granule for oral suspension or a bulk granule for further compression.

    RouteEquipmentFormulation loadingCritical parameterTerminal product
    Direct compressionRotary tablet pressAPI 1.0–5.0% w/wPrecompression 5–8 kNIR tablet
    Roller compactionRoller compactor + capsule fillerAPI 5–20% w/wRibbon density 1.05–1.25 g/cm³Capsule
    Fluid-bed granulationTop-spray fluid bedAPI 20–40% w/wProduct temperature 32–40 °COral granule/sachet

    When a Bromobutyl Stopper Is Steam Sterilized Inside a Validated Load for Aseptic Powder Filling

    Bromobutyl stoppers for injectable sterile powder filling are washed, siliconised, and steam sterilised before introduction into an ISO 5 filling zone. The sterilization load is qualified according to ISO 17665 and 21 CFR 211.113; typical cycles are 121 °C for 30 min or 122 °C for 15 min with a drying phase under -0.8 bar vacuum for 2–4 h. Loading density is controlled within 8–12 kg per tray container to prevent residual moisture carryover. The stopper feed line hopper is held at 18–26 °C and 30–60% RH to avoid surface tack; process validation includes bioburden recovery and moisture residue below 0.5% by weight after drying. The sterile powder is filled under unidirectional airflow and stoppered immediately after dosing; oxygen and moisture ingress through the closure are monitored by headspace analysis. The terminal product is a sterile powder for injection.

    Reduced Headspace Oxygen Determines Shelf-Life Stability in Cytotoxic Lyophilized Vials

    High-potency oncology lyophilized powders are filled in isolators and sealed under nitrogen to limit oxidative degradation. Bromobutyl stoppers for this application are extracted and evaluated per USP <381>, USP <382>, EP 3.2.9, and ISO 8871-1, and elemental impurities are controlled by ICH Q3D. The fill process targets an oxygen headspace of ≤ 2.0% v/v and residual cake moisture ≤ 1.0%; fill weights are typically 50–500 mg per vial. Closed transfer devices are used to avoid operator exposure; vial sealing with a bromobutyl stopper and aluminium cap is performed at -0.2 bar to -0.4 bar relative chamber pressure to reduce stopper pop-up. The terminal product is a cytotoxic lyophilized powder for injection, reconstituted in a closed system with 10 mL to 50 mL diluent.

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    Certification & Compliance
    More Introduction

    The bromobutyl rubber stopper for injectable sterile powder pharma grade API for tablet / capsule / granule / injection, oral & injectable is a pharmaceutical packaging component manufactured from a brominated isobutylene-isoprene copolymer. The base elastomer contains 1.8% to 2.2% bromine and is compounded with a sulfur-free cure system, a calcium stearate release system, and an optional fluoropolymer film on the product-contact plug face. Dimensional profiles follow ISO 8362-1:2018 neck finishes for 13 mm, 20 mm, and 32 mm vials. Model coding identifies the polymer, neck diameter, slot configuration, and film: BIIR-20-3S-ETFE denotes a bromobutyl closure for 20 mm necks with three venting slots and ETFE coating, while BIIR-13-F1 denotes a flanged, non-slotted serum closure for 13 mm vials. The same material is used as a bulk API container closure for tablets, capsules, granules, and oral or injectable intermediates where low water-vapor transmission, low oxygen permeation, and controlled extractables are required. The closure is not a formulation ingredient; it is a critical packaging material qualified as part of the container closure system.

    When the Closure Must Function After Lyophilization

    During freeze drying, slotted bromobutyl stoppers are partially seated and held in the lyophilization chamber; the slots provide vapor pathways for sublimation. Shelf temperatures during primary drying are commonly controlled between −45 °C and +30 °C, and the stopper must return sufficient sealing force when the shelves compress the closure at the end of the cycle. Production-scale lyophilizer data show that final headspace gas composition in the sealed vial depends on stopper moisture content, slot geometry, and chamber backfill pressure. Stoppers are washed in rotary vial washers and steam sterilized at 121 °C for 30 min; residual moisture after drying is held at ≤0.5% w/w because higher retained moisture transfers into the lyophilized cake or raises the headspace dew point. On high-speed capping stations operating above 450 vials per minute, residual surface moisture above 0.8% w/w has been associated with intermittent capping pressure loss and glass flange microcracks in 13 mm neck formats. For dry heat sterilization at 160 °C for 2 h, the closure is pre-dried to ≤0.2% w/w; otherwise volatile decomposition products can exceed the UV absorbance limit of Ph. Eur. 3.2.9.

    Needle penetration and fragmentation are critical for reconstitution. Repeated penetration with 21G needles is assessed according to ISO 8871-5:2016. A typical release test requires no visible fragmentation in 8 of 10 penetrated stoppers, and pierced closures must maintain a 0.5 bar internal nitrogen pressure differential without leakage. Because bromobutyl vulcanizates undergo post-cure changes, these tests are performed after terminal steam sterilization rather than on as-molded closures. Penetration force with a 21G needle is typically 1.2 N to 3.5 N for fluoropolymer-coated closures and can exceed 6 N for uncoated closures after multiple holes. This higher force is a recognized limitation when reconstitution is performed with large-bore or blunt drawing needles.

    How Does Bromobutyl Differ From Chlorobutyl in Injectable Powder Service?

    Bromobutyl closures differ from chlorobutyl closures primarily in halogen reactivity and crosslink density. The brominated isoprene unit cures more readily, permitting a low-zinc or zinc-free cure and lower residual metal extractables. Technical data sheets for comparable 20 mm closures report oxygen permeability coefficients from 2.5 × 10−17 to 4.0 × 10−17 mol·m·m⁻²·s⁻¹·Pa⁻¹ at 23 °C for bromobutyl, while chlorobutyl formulations of equal thickness fall from 4.0 × 10−17 to 7.0 × 10−17 mol·m·m⁻²·s⁻¹·Pa⁻¹. Moisture vapor transmission normalized to 1 mm thickness at 40 °C and 75% relative humidity is generally 0.4 g·mm/m²·day to 0.8 g·mm/m²·day for bromobutyl and 0.9 g·mm/m²·day to 1.4 g·mm/m²·day for chlorobutyl. These differences support the use of bromobutyl for freeze-dried powders with headspace oxygen targets below 2% v/v and for moisture-sensitive APIs stored in high-humidity zones.

    Against polyisoprene, bromobutyl provides lower gas and moisture permeation but higher needle penetration force and greater sensitivity to ionizing radiation. Polyisoprene closures may offer easier needle insertion and lower fragmentation, but their water vapor transmission can exceed 4 g·mm/m²·day under tropical storage while bromobutyl remains below 0.6 g·mm/m²·day under the same conditions. Silicone closures have excellent low-temperature flexibility but oxygen permeability two to three orders of magnitude higher than bromobutyl, making them unsuitable for oxygen-sensitive sterile powders. EPDM closures are less resistant to aliphatic solvents and may generate higher volatile organic extractables after repeated autoclaving, whereas bromobutyl after post-cure annealing shows stable extractive profiles through 121 °C for 30 min for at least 3 cycles.

    Extractable and Leachable Control Boundaries

    The product is controlled against Ph. Eur. 3.2.9, USP 〈381〉, and ISO 8871-1:2016. Aqueous extraction is performed at 121 °C for 30 min; the extract is examined for pH shift, reducing substances, UV absorbance at 220 nm, and residue on evaporation. For a 20 mm closure, residue on evaporation is typically controlled to ≤2.0 mg per closure, and UV absorbance at 220 nm is held below 0.20 AU in a 10 mm path cell. The fluoropolymer film reduces contact of the elastomer with the drug, lowering extractable bisphenol A diglycidyl ether and nitrosamine-related impurities; however, the film increases needle penetration force by 0.5 N to 1.5 N relative to uncoated material.

    Shore A hardnessISO 7619-1:202223±2 °C45–55
    Tensile strengthISO 37:2017500 mm/min≥9 MPa
    Elongation at breakISO 37:2017500 mm/min≥400%
    Compression setISO 815-1:201970±2 °C, 22 h≤25%
    Penetration force, 21G needle, coatedISO 8871-5:2016after steam sterilization1.2–3.5 N
    FragmentationUSP 〈381〉10 stoppersno visible cores in 8/10
    Self-sealingISO 8871-5:20160.5 bar N₂no leakage
    Residual moisturegravimetric105 °C, 24 h≤0.5% w/w

    In sterile dry powder filling of injectable APIs, the closure is supplied as ready-to-sterilize; it is transferred through a depyrogenation tunnel or autoclave bag and presented to the capping station without further washing. For lyophilized products, the closure is inserted to the first notch after dose fill, then fully seated by shelf compression. The residual moisture in the stopper after washing therefore defines not only chemical purity but also the mechanical friction against the vial neck and the chamber backfill gas diffusion rate.

    The same closure is used in oral API containers for tablets, capsules, and granules when moisture protection and low leachable metals are specified. In that service, a 20 mm bromobutyl stopper with a fluoropolymer liner is seated into 100 mL to 500 mL glass bottles under aluminium caps with torque of 1.5 N·m to 2.5 N·m. Seal quality is verified by vacuum decay using ASTM F2338-09 at 20 kPa pressure differential. The closure does not contact the oral dosage form directly and is therefore not required to meet parenteral extractive limits, but the same extraction and volatile controls are applied to prevent cross-contamination in shared packaging areas.

    Manufacturing-Line Handling Is Not Uniform Across Neck Sizes

    Rotary washing machines with ultrasonic prewash use silicone-free wash cycles for bromobutyl closures. Excess surface silicone can reduce the coefficient of friction below 0.20, causing stopper bridging in feed chutes on lines running above 300 vials per minute; insufficient silicone raises hopper jams and capping misalignment on continuous-motion cappers. A washed and dried stopper typically exhibits a coefficient of friction between 0.25 and 0.45 against a stainless steel chute. In 13 mm neck formats, tipped-stopper defect rates have exceeded 2% on older inline filling equipment when the coefficient falls below 0.20. Dry heat sterilization and dry powder isolator environments generate static charge on uncoated bromobutyl; this is controlled with ionizing air bars at the hopper discharge and by using fluoropolymer-coated plug faces for 20 mm and 32 mm closures.

    Gamma irradiation is not the default sterilization route. Published data for this specific bromobutyl closure formulation at irradiation doses above 25 kGy are limited; steam at 121 °C for 30 min or dry heat at 160 °C for 2 h after pre-drying is specified unless the user qualifies the exact closure, container, and drug product system. The material should not be combined with amine-based additives, strong oxidizing media, or low-molecular-weight ester plasticizers because these compounds can alter the cure network, increase permeability, or extract into the drug solution.

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