| HS Code | 221904 |
| Product Name | Procaine Benzylpenicillin (Sterile) Pharma Grade API |
| Generic Name | Procaine benzylpenicillin / Procaine penicillin G |
| Chemical Formula | C29H38N4O6S |
| Molecular Weight | 570.70 g/mol |
| Cas Number | 6130-64-9 |
| Api Grade | Pharma Grade |
| Sterility | Sterile |
| Physical Form | White or almost white crystalline powder |
| Solubility | Sparingly soluble in water; soluble in alcohol and methanol; practically insoluble in fixed oils |
| Therapeutic Category | Beta-lactam antibiotic (penicillin group) |
| Mechanism Of Action | Inhibits bacterial cell wall synthesis by binding to penicillin-binding proteins, causing bactericidal effect |
| Indications | Treatment of infections caused by penicillin-sensitive Gram-positive bacteria, including streptococcal, pneumococcal, and susceptible staphylococcal infections |
| Route Of Administration | Oral and injectable |
| Compatible Dosage Forms | Tablet, capsule, granule, and injection |
| Storage Conditions | Store in tightly sealed, moisture-proof container, protected from light and heat |
| Pharmacopoeial Compliance | USP/Ph.Eur./BP |
| Shelf Life | Typically 24 to 36 months under recommended storage conditions |
As an accredited Procaine Benzylpenicillin (sterile) 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 | Sterile Procaine Benzylpenicillin API supplied in 25 kg drums with double polyethylene lining, sealed for oral and injectable pharmaceutical formulations. |
| Container Loading (20′ FCL) | Loading 20′ FCL: palletized sterile Procaine Benzylpenicillin API in sealed drums; ensure clean, dry, secure stowage, no contamination. |
| Shipping | Shipped under strict temperature-controlled conditions to maintain sterility and stability. Packaged in sealed, inert pharmaceutical-grade containers with tamper-evident seals, protective cushioning, and documented cold-chain monitoring. Fully compliant with international hazardous goods and pharmaceutical transport regulations, ensuring safe, traceable delivery for oral and injectable formulations. |
| Storage | Store Procaine Benzylpenicillin (sterile) API in its original, tightly closed container, protected from light, moisture, and heat. Recommended storage: below 25°C in a cool, dry, well-ventilated area. Avoid exposure to direct sunlight and humidity. Maintain container integrity for sterility. Discard unused portion. Keep out of reach of children. |
| Shelf Life | Shelf life is 2 years from manufacture when stored in original sealed container under recommended cool, dry conditions. |
Sterile dry-powder injectable processing of procaine benzylpenicillin begins with release of the API against the current pharmacopoeial monograph for procaine benzylpenicillin injection, not only for chemical assay but for sterility to be confirmed after aseptic transfer and powder handling. The solid is moved into a Grade B envelope and then into an open-front Grade A isolator operating under ISO 14644-1 class 5 conditions with unidirectional airflow 0.45 m/s ± 20%. Terminal sterilization of the filled vial is not assigned to this molecule because solid-state beta-lactam degradation accelerates at elevated temperature and the marketed presentation is a dry powder. The fill line uses a 316L stainless steel auger or gravimetric dosator fitted with a polytetrafluoroethylene-coated hopper; the hopper discharge cone angle is maintained at not less than 70° to prevent bridging. In-process fill weight checks are taken every 15 min; if the relative standard deviation exceeds 2.0%, the line is stopped and the affected vials are 100% checkweighed. Residual moisture is measured using USP <921> Method Ia; free water above the filed release limit accelerates hydrolysis to penicilloic acid. Sterility testing is run by membrane filtration on both fluid thioglycollate medium and soybean-casein digest medium as described in USP <71>. Because the API and the procaine moiety can inhibit growth of challenge organisms, method suitability is repeated with 100 CFU inocula and must demonstrate recovery. Bacterial endotoxin is determined by the kinetic chromogenic method in USP <85>; dilution fluids are checked for beta-glucan interference. After reconstitution with sterile water for injection, the product is a suspension rather than a solution; particulate matter is therefore assessed according to USP <788> Method 1 if the particle counter can tolerate the opacity, otherwise Method 2 is used. Container closure integrity is validated by vacuum decay or helium leak under USP <1207>; the chlorobutyl stopper is qualified for penetrability and fragmentation according to USP <381>. Penicillin finishing suites are separated from cephalosporin and non-beta-lactam areas under 21 CFR 211.46 and 21 CFR 211.67; cleaning validation uses surface swabs and rinse samples with HPLC detection below the health-based exposure limit.
Reconstitution volume and syringeability are process-linked. The dry powder is formulated to wet rapidly without forming a hard cake; caking at the vial base occurs when the API is over-milled and electrostatic charge binds the particles. A 21-gauge needle is used to withdraw the suspension, and the bolus dose is administered by deep intramuscular injection only. The manufacturing dossier does not assign intravenous administration to this formulation because procaine benzylpenicillin is a depot salt. On a production scale, the most frequent loss parameter is not chemical assay but particulate matter from stopper fragments and fill-line elastomer shedding. Therefore the fill volume acceptance limit for subvisible particles is checked after reconstitution with particle-free WFI; the acceptance criteria follow USP <788> or the harmonized pharmacopoeial monograph. Published data for terminal sterilization of this specific dry-powder configuration is limited; aseptic processing remains the regulatory default.
Tableting procaine benzylpenicillin at a drug load exceeding 70% w/w forces a dry granulation route because the API shows poor compactibility and high interparticulate friction. Direct compression produces capping and lamination on rotary presses with 10 mm round biconvex tooling. The dry granulation line begins with a low-shear bin blender operating at 10–15 rpm for 15–25 min; microcrystalline cellulose and dibasic calcium phosphate dihydrate are used as brittle diluents. Crospovidone is added intragranularly at 2–5% w/w; sodium starch glycolate is added extragranularly at 1–3% w/w; magnesium stearate is added at 0.5–1.0% w/w. Over-lubrication above 1.0% w/w coats the granules and increases tablet disintegration time. Roller compaction is performed with hydraulic roll pressure 4–8 MPa, roll speed 3–5 rpm, and gap 1.5–2.5 mm as development starting conditions. Ribbon solid fraction is held between 0.60 and 0.80; ribbons below 0.60 generate excess fines, while ribbons above 0.80 reduce granule compressibility. The ribbons are milled through an oscillating mill with 0.8 mm or 1.0 mm round-hole screens. Sieve analysis is conducted according to USP <786>; the fraction retained above 850 µm is controlled because large granules cause weight variation, and the fraction passing 150 µm is controlled because fines increase punch sticking. Compression uses a rotary tablet press with precompression 25–50 kN and main compression 60–120 kN for 10 mm tooling; tablet hardness is maintained at 80–120 N. Hardness below 60 N raises friability above 1.0%; hardness above 140 N can delay disintegration. Disintegration is tested in 900 mL purified water at 37 °C per USP <701>. Dissolution is tested in 900 mL phosphate buffer pH 6.8 at 37 °C using USP <711> apparatus II at 50 rpm; the acceptance limit is set in the approved filing. The principal degradation products, penicilloic acid and penilloic acid, are monitored by stability-indicating HPLC under ICH Q3B.
Hard capsule filling with procaine benzylpenicillin uses a pre-granulated blend rather than raw API. Raw API has low bulk density and entrains air, so the fill weight relative standard deviation cannot remain below 2.0% on a tamping-pin machine without granulation. The capsule shell is selected by equilibrium moisture: gelatin shells hold 13–16% water at 45% relative humidity, while HPMC shells hold 3–7% under the same conditions. If the filled granulate has free water above the API limit, water migrates to the shell and causes gelatin softening or HPMC seam deformation. The target fill weight for a size 0 capsule is typically 400 mg; the powder bed height and tamping pin immersion depth are adjusted until the fill weight relative standard deviation is maintained below 2.0%. Content uniformity is run by USP <905>; the acceptance value must not exceed 15.0. Segregation of granulate fractions during transfer hoppers is controlled by minimizing free-fall height and using mass-flow hoppers with 70° discharge angles. Disintegration is tested in 900 mL water at 37 °C per USP <701>. Dissolution follows USP <711>; if the capsule shell is HPMC, the dissolution medium temperature is strictly controlled at 37 °C because HPMC shell behavior can alter release. Delayed-release capsules are not a common downstream configuration for procaine benzylpenicillin, and published data for this specific configuration is limited.
Granules for oral suspension are manufactured by low-shear wet granulation or fluid-bed granulation to limit excipient exposure to water and heat. The granulation vehicle contains a citrate buffer system because procaine benzylpenicillin shows maximum aqueous stability in the pH 6.0–6.5 range; pH is tested by USP <791> after reconstitution and after 7 days at 25 °C. A downward pH drift below 5.0 indicates acid-catalyzed beta-lactam ring opening and requires batch investigation. Suspending agents are selected to generate yield stress without overdrying the granulate; xanthan gum at 0.1–0.3% w/w or microcrystalline cellulose/carboxymethyl cellulose sodium at 0.5–1.5% w/w is sufficient for redispersion after shaking. Multi-dose presentations require antimicrobial effectiveness testing according to USP <51> with challenge organisms; the preservative system is validated in the reconstituted suspension, not in the dry granulate. Dry granule loss on drying is measured by USP <921> Method Ia; fluid-bed inlet air temperature is selected so that product temperature does not exceed 45 °C. Redispersibility testing is performed by shaking the finished container for 15 seconds, waiting 30 seconds, and sampling the upper, middle, and lower zones; the assay difference between zones should not exceed 5.0%. The dry granulate is filled into HDPE bottles with child-resistant polypropylene caps; if filling is performed at ambient relative humidity above 40%, the product is held in sealed drums prior to line introduction.
| Presentation | Critical control point | Test method | Observed failure mode |
|---|---|---|---|
| Sterile dry-powder injectable | Residual moisture and particulate after reconstitution | USP <921>, USP <788> | Penicilloic acid formation or visible stopper fragments |
| Tablet | Ribbon solid fraction and tablet hardness | USP <786>, USP <701> | Dissolution delay or capping/lamination |
| Capsule | Fill weight variation and shell moisture exchange | USP <905>, USP <921> | Softened gelatin shell or seam deformation |
| Oral suspension granules | pH and redispersibility after storage | USP <791>, USP <51> | Acidic shift or zone assay difference |
When oral tablets or capsules are packed in cold-form aluminum foil blisters, the sealing process is monitored by peel strength and blue dye ingress. PVC mono-film is not used for high-humidity climatic zones because it fails moisture barrier requirements for beta-lactam powders. A cold-form aluminum laminate with 25 µm aluminum foil is selected; the sealing head temperature is set at 180 °C, and the seal width is held above 2 mm. Stability protocols follow ICH Q1A; packages are exposed to 40 °C/75% RH for 6 months accelerated and 30 °C/65% RH long-term. Desiccant sachets are included when the calculated moisture vapor transmission rate of the package exceeds the API’s maximum water capacity; the sachet mass is checked by weight gain at each pull point.
Facilities that handle procaine benzylpenicillin in oral and injectable campaigns operate under segregated beta-lactam containment. The oral-to-injectable cross-contamination risk is not only chemical but allergenic; trace penicillin exposure on shared equipment can induce sensitization. Dedicated suites, air handling, garments, and utensils are assigned under 21 CFR 211.46 and 21 CFR 211.67; cleaning validation measures surface residues by swab and rinse using HPLC with a limit of detection below the health-based exposure limit. In a multi-product suite, the beta-lactam campaign is followed by a verified cleaning program and an analytical hold time. Aseptic gowning and material transfer are repeated for each sterile lot; the line clearance includes verification that no lactose-containing oral granulate remains in the injectable area. Environmental monitoring uses settle plates, contact plates, and active air sampling; alert levels are set according to EU GMP Annex 1, and the resulting data are trended for quarterly review.
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Procaine benzylpenicillin (sterile), identified by CAS Registry Number 6130-64-9, is a white to off-white crystalline monohydrate used as a pharma-grade active pharmaceutical ingredient for oral solid-dose and injectable suspension products. Commercial material is supplied under a manufacturer-specific grade code that designates sterile micronized, non-pyrogenic powder; the pharmacopoeial descriptor remains benzylpenicillin procaine. The compound is an equimolar salt of benzylpenicillin and procaine. With the molecular formula C13H20N2O2·C16H18N2O4S·H2O and a relative molecular mass of approximately 588.7 g/mol, the theoretical procaine content is approximately 40.1% by mass and the theoretical water of hydration is approximately 3.1% by mass. The aqueous solubility at 20 °C is approximately 4 mg/mL, which is substantially lower than the freely soluble benzylpenicillin potassium and sodium salts and gives the procaine salt its prolonged-release behaviour after intramuscular injection. The sterile grade is distinguished from non-sterile procaine benzylpenicillin by compliance with Ph. Eur. 2.6.1 and USP <71> sterility tests, by a validated bacterial endotoxin limit, and by particle-size distribution controls appropriate to aseptic dispersion. The product is intended for formulation into tablets, capsules, granules, and injectable suspensions; it is not suitable for intravenous, intrathecal, or ophthalmic administration.
The replacement of the alkali-metal counterion with procaine alters dissolution kinetics, aqueous stability, and injection-site tolerability. Benzylpenicillin potassium and sodium salts dissolve rapidly in water, generate high early plasma concentrations after parenteral administration, and are suitable for intravenous infusion after reconstitution. In contrast, procaine benzylpenicillin hydrates slowly from a microcrystalline depot after intramuscular injection, yielding measurable plasma concentrations for approximately 12 to 24 hours while limiting peak plasma levels. The procaine cation provides a local anaesthetic effect that reduces injection-site pain in aqueous suspension formulations. The low aqueous solubility introduces processing constraints: the powder cannot be reconstituted into a true solution at clinically useful concentrations and cannot be sterilised by terminal steam processes without beta-lactam hydrolysis. The solubility difference also affects oral dosage design: the procaine salt is less hygroscopic than the potassium salt but exhibits slower dissolution in gastric fluid, so oral tablets and capsules require particle-size and formulation controls to achieve pharmacopoeial dissolution acceptance ranges. Benzathine benzylpenicillin, a benzylpenicillin salt with even lower aqueous solubility, typically extends intramuscular release to 2–4 weeks, while procaine benzylpenicillin occupies an intermediate duration position. This intermediate release profile makes the sterile API suitable for formulations where prolonged, but not depot-length, systemic exposure is required.
| Parameter | Procaine benzylpenicillin (monohydrate) | Benzylpenicillin potassium | Benzathine benzylpenicillin |
|---|---|---|---|
| Approximate aqueous solubility at 20 °C | 4 mg/mL | > 100 mg/mL | < 1 mg/mL |
| Intramuscular duration | 12–24 h | 4–6 h | 2–4 weeks |
| Suitable intravenous use | No; procaine toxicity and crystalline embolisation risk | Yes; after reconstitution and dilution | No; very low solubility |
| Oral formulation use | Tablet, capsule, granule; dissolution controlled by salt hydration | Rare; hygroscopic and acid-labile | Not common; extremely slow dissolution |
In oral tablet and capsule manufacture, the sterile-grade powder is typically introduced after pre-blending with dried excipients and then processed by dry granulation or roller compaction to avoid free-water exposure. Direct compression of procaine benzylpenicillin monohydrate may be limited by electrostatic charging and insufficient flow in high-speed rotary presses; roller compaction with sieve milling is therefore used to improve bulk density uniformity and reduce hopper bridging. Aqueous wet granulation is avoided unless the binder application rate is minimal and the drying endpoint is controlled at a loss on drying below 2.0% w/w, because residual moisture accelerates beta-lactam ring hydrolysis. Content uniformity is assessed according to Ph. Eur. 2.9.40 or USP <905> using high-performance liquid chromatography with ultraviolet detection. Dissolution testing for oral solid products is performed using apparatus II or IV at pH values corresponding to the intended release environment; published data for the dissolution behaviour of procaine benzylpenicillin granules under fed-state gastric conditions are limited, so formulation qualification should include a pH-switching dissolution method. The product is not inherently enteric-protected; when gastric acid protection is required, the granules or tablets must receive a compounding-specific polymer coating. Batch-to-batch variance in particle size can alter segregation in twin-shell V-blenders; colloidal silicon dioxide at 0.5%–1.5% w/w is commonly evaluated as a glidant.
Pharmacopoeial monographs for benzylpenicillin procaine, including Ph. Eur. and USP, define identity, assay, related substances, water content, and bacterial endotoxins for sterile parenteral grades. The release specification for the sterile API includes infrared absorption spectrophotometry according to Ph. Eur. 2.2.24 and high-performance liquid chromatography according to Ph. Eur. 2.2.29 for identification and assay. The assay is calculated and reported as the sum of benzylpenicillin and procaine contents on the anhydrous basis; the theoretical percentages are approximately 56.8% for benzylpenicillin and 40.1% for procaine, and monograph limits are applied to both moieties. Related substances are controlled by reversed-phase HPLC with detection of benzylpenicilloic acid, p-aminobenzoic acid, and other specified degradation products. Residual solvents are controlled according to Ph. Eur. 2.4.24 or USP <467>; the product is normally supplied as a non-pyrogenic powder with a bacterial endotoxin limit determined according to Ph. Eur. 2.6.14 or USP <85>. Water content is determined by Karl Fischer titration according to Ph. Eur. 2.5.12 and should remain within the hydration range appropriate for the monohydrate. Particle-size distribution is measured by laser diffraction according to Ph. Eur. 2.9.37; the oral solid-dose and injectable suspension variants normally carry different particle-size targets because flow, blend uniformity, sedimentation, and syringeability impose different requirements.
| Quality attribute | Method designation | Application boundary or purpose |
|---|---|---|
| Identity | Ph. Eur. 2.2.24 infrared absorption | Conforms to procaine benzylpenicillin reference spectrum |
| Assay | Ph. Eur. 2.2.29 HPLC | Benzylpenicillin and procaine content on anhydrous basis |
| Related substances | Ph. Eur. 2.2.29 HPLC | Quantifies benzylpenicilloic acid, p-aminobenzoic acid, and total impurities |
| Water content | Ph. Eur. 2.5.12 Karl Fischer | Confirms monohydrate stoichiometry |
| Bacterial endotoxins | Ph. Eur. 2.6.14, USP <85> | Injectable-grade non-pyrogenic release |
| Sterility | Ph. Eur. 2.6.1, USP <71> | Sterile API for aseptic formulation |
| Particle size distribution | Ph. Eur. 2.9.37 laser diffraction | Controls D10, D50, D90 for oral and injectable variants |
| Residual solvents | Ph. Eur. 2.4.24, USP <467> | Conforms to Class 3 limits where applicable |
The bacterial endotoxin limit for the injectable grade is not a single universal value; it is calculated as K/M, where K is 5 EU/kg for intramuscular products and M is the maximum dose per kilogram. For a 1.2 g dose in a 70 kg adult, M is approximately 17.1 mg/kg and the corresponding endotoxin threshold is approximately 0.29 EU/mg. The exact limit is product-specific and must be justified in the marketing authorisation dossier. Microbiological purity of non-sterile oral grades is assessed according to Ph. Eur. 2.6.12 or USP <61> and <62>.
For injectable suspension manufacture, terminal sterilisation of procaine benzylpenicillin is not feasible because moist-heat exposure accelerates beta-lactam hydrolysis and procaine salt decomposition, and dry-heat exposure at temperatures above 50 °C increases related substances. The sterile API is therefore processed by aseptic dispersion: the micronized powder is weighed and transferred within an isolator or restricted-access barrier system operating under Grade A particle conditions with Grade B background according to EU GMP Annex 1 and USP <71> compliance. Inline particle-size reduction through a sterile cone mill or jet mill may be employed to control D90 below 50 µm, but the equipment must be qualified for yield, for the absence of metal particulate contamination, and for the absence of heat-induced agglomeration. The aqueous vehicle is sterilised by autoclaving and cooled before dispersion; suspending agents, buffers, and preservatives are selected to maintain pH between 6.0 and 6.8, where penicillin G stability is maximal. After dispersion, the suspension is filled into siliconised glass vials or prefilled syringes, and the filled product is tested for sterility, bacterial endotoxins, particulate matter according to Ph. Eur. 2.9.19, and syringeability through a 21 G needle. Because the salt is not soluble at therapeutic concentrations, reconstitution cannot be used as a clarity check; instead, suspension uniformity and sedimentation volume are part of batch release. Production-line failure modes observed during sterile powder handling include powder bridging in hoppers due to electrostatic charge, caking after exposure to relative humidity above 60%, and particle-size increase from pressure-induced agglomeration in screw-fed mills. These failures are controlled by humidity-controlled weighing suites and by periodic sieve or laser-diffraction checks after milling.
Compliance with current good manufacturing practice for sterile active substances is required under EU GMP Part II and ICH Q7 because the product is destined for aseptic processing. The API manufacturer's process validation should include media fills for aseptic powder handling, lyophilisation-free drying, and environmental monitoring data for Grade A and Grade B zones. Aseptic APIs are not released solely on the basis of sterility testing; parametric release may be used only where a defined sterilising stage exists, which is not applicable to the final procaine benzylpenicillin powder after crystallisation. Consequently, batch release is based on terminal sterility test results together with bioburden monitoring at pre-filtration and pre-filling stages, and on environmental monitoring trend reports.
In low-dose oral granule and powder formulations, the sterile API may be dry-blended with lactose, microcrystalline cellulose, croscarmellose sodium, and magnesium stearate; however, the blend must not include amine-containing excipients such as certain shellac or gelatin hydrolysates in the presence of free moisture, because primary amines can open the beta-lactam ring by nucleophilic substitution. Contact with copper, zinc, or iron surfaces in wet granulation equipment should be avoided because trace metal ions catalyse degradation and can reduce potency below the assay limit. Storage of the sterile API should be maintained at 2–8 °C in double-layer polyethylene bags inside sealed aluminium-laminated outer packaging; repeated opening of the package in an uncontrolled humidity environment above 60% RH requires prior moisture sorption verification because the monohydrate surface can adsorb free water and increase hydrolysis risk. Batch-to-batch variance in particle-size distribution and residual procaine-related impurities can alter suspension sedimentation behaviour and content uniformity; therefore incoming raw-material qualification should include laser diffraction, scanning electron microscopy, and HPLC impurity profiling against a qualified reference lot. The sterile API is not interchangeable with benzylpenicillin potassium or sodium on a weight-for-weight basis; dosing must be expressed in penicillin G units or in the procaine salt mass specified by the relevant pharmacopoeial monograph and converted using the assay value of the specific batch.