PILOT PLANT SCALE UP TECHNIQUES

PILOT PLANT SCALE UP TECHNIQUES
Prof. Dr. Basavaraj K. Nanjwade M. Pharm., Ph. D Department of Pharmaceutics KLE University College of Pharmacy BELGAUM , Karnataka, India Cell No: 23 August 2012 KLE College of Pharmacy, Nipani.

KLE College of Pharmacy, Nipani.
CONTENTS Introduction Objectives of the Pilot Plant Importance of the Pilot Plant Pilot plant design for tablets Pilot plant scale-up techniques for capsules Pilot plant scale-up techniques for Parenterals References 23 August 2012 KLE College of Pharmacy, Nipani.

Introduction What is Pilot plant : “Defined as a part of the pharmaceutical industry where a lab scale formula is transformed into a viable product by the development of liable practical procedure for manufacture.” R & D Production Pilot Plant Scale-up : “The art of designing of prototype using the data obtained from the pilot plant model.” 23 August 2012 KLE College of Pharmacy, Nipani.

Objectives of Pilot Plant
“Find mistakes on small scale and make profit on large scale.” To produce physically and chemically stable therapeutic dosage forms. Review of the processing equipment. Guidelines for productions and process control. Evaluation and validation. To identify the critical features of the process. To provide master manufacturing formula. 23 August 2012 KLE College of Pharmacy, Nipani.

Importance of Pilot Plant
Examination of formulae. Review of range of relevant processing equipments. The specification of the raw materials. Production rates. The physical space required. Appropriate records and reports to support GMP. 23 August 2012 KLE College of Pharmacy, Nipani.

Pilot Plant design for Tablets
The primary responsibility of the pilot plant staff is to ensure that the newly formulated tablets developed by product development personnel will prove to be efficiently, economically, and consistently reproducible on a production scale. The design and construction of the pharmaceutical pilot plant for tablet development should incorporate features necessary to facilitate maintenance and cleanliness. If possible, it should be located on the ground floor to expedite the delivery and shipment of supplies. 23 August 2012 KLE College of Pharmacy, Nipani.

Extraneous and microbiological contamination must be guarded against by incorporating the following features in the pilot plant design: Fluorescent lighting fixtures should be the ceiling flush type. The various operating areas should have floor drains to simplify cleaning. The area should be air-conditioned and humidity controlled. High -density concrete floors should be installed. The walls in the processing and packaging areas should be enamel cement finish on concrete. Equipment in the pharmaceutical pilot plant should be similar to that used by production division- manufacture of tablets. 23 August 2012 KLE College of Pharmacy, Nipani.

23 August 2012 KLE College of Pharmacy, Nipani.

Material handling system
In the laboratory, materials are simply scooped or poured by hand, but in intermediate- or large-scale operations, handling of this materials often become necessary. If a system is used to transfer materials for more than one product steps must be taken to prevent cross contamination. Any material handling system must deliver the accurate amount of the ingredient to the destination. The type of system selected also depends on the characteristics of the materials. More sophisticated methods of handling materials such as vacuum loading systems, metering pumps, screw feed system. 23 August 2012 KLE College of Pharmacy, Nipani.

Material handling system
Vacuum loading machine 23 August 2012 KLE College of Pharmacy, Nipani.

Dry Blending Powders to be used for encapsulation or to be granulated must be well blended to ensure good drug distribution. Inadequate blending at this stage could result in discrete portion of the batch being either high or low in potency. Steps should also be taken to ensure that all the ingredients are free of lumps and agglomerates. For these reasons, screening and/or milling of the ingredients usually makes the process more reliable and reproducible. 23 August 2012 KLE College of Pharmacy, Nipani.

Dry Blending The equipment used for blending are: V- blender Double cone blender Ribbon blender Slant cone blender Bin blender Orbiting screw blenders vertical and horizontal high intensity mixers. SCALE UP CONSIDERATIONS Time of blending . Blender loading. Size of blender. 23 August 2012 KLE College of Pharmacy, Nipani.

Dry Blending V – cone blender Double cone blender 23 August 2012 KLE College of Pharmacy, Nipani.

Dry Blending Ribbon blender 23 August 2012 KLE College of Pharmacy, Nipani.

Granulation The most common reasons given to justify granulating are: To impart good flow properties to the material, To increase the apparent density of the powders, To change the particle size distribution, Uniform dispersion of active ingredient. Traditionally, wet granulation has been carried out using, Sigma blade mixer, Heavy-duty planetary mixer. 23 August 2012 KLE College of Pharmacy, Nipani.

Granulation Sigma blade mixer Planetary mixer 23 August 2012 KLE College of Pharmacy, Nipani.

Granulation Wet granulation can also be prepared using tumble blenders equipped with high-speed chopper blades. 23 August 2012 KLE College of Pharmacy, Nipani.

Granulation More recently, the use of multifunctional “processors” that are capable of performing all functions required to prepare a finished granulation, such as dry blending, wet granulation, drying, sizing and lubrication in a continuous process in a single equipment. 23 August 2012 KLE College of Pharmacy, Nipani.

Granulation Binders: Used in tablet formulations to make powders more compressible and to produce tablets that are more resistant to breakage during handling. In some instances the binding agent imparts viscosity to the granulating solution so that transfer of fluid becomes difficult. This problem can be overcome by adding some or all binding agents in the dry powder prior to granulation. 23 August 2012 KLE College of Pharmacy, Nipani.

Granulation Some granulation, when prepared in production sized equipment, take on a dough-like consistency and may have to be subdivided to a more granular and porous mass to facilitate drying. This can be accomplished by passing the wet mass through an oscillating type granulator with a suitably large screen or a hammer mill with either a suitably large screen or no screen at all. 23 August 2012 KLE College of Pharmacy, Nipani.

Drying The most common conventional method of drying a granulation continues to be the circulating hot air oven, which is heated by either steam or electricity. The important factor to consider as part of scale-up of an oven drying operation are airflow, air temperature, and the depth of the granulation on the trays. If the granulation bed is too deep or too dense, the drying process will be inefficient, and if soluble dyes are involved, migration of the dye to the surface of the granules. Drying times at specified temperatures and airflow rates must be established for each product, and for each particular oven load. 23 August 2012 KLE College of Pharmacy, Nipani.

Drying Fluidized bed dryers are an attractive alternative to the circulating hot air ovens. The important factor considered as part of scale up fluidized bed dryer are optimum loads, rate of airflow, inlet air temperature and humidity. 23 August 2012 KLE College of Pharmacy, Nipani.

Reduction of Particle size
Compression factors that may be affected by the particle size distribution are flowability, compressibility, uniformity of tablet weight, content uniformity, tablet hardness, and tablet color uniformity. First step in this process is to determine the particle size distribution of granulation using a series of “stacked” sieves of decreasing mesh openings. Particle size reduction of the dried granulation of production size batches can be carried out by passing all the material through an oscillating granulator, a hammer mill, a mechanical sieving device, or in some cases, a screening device. 23 August 2012 KLE College of Pharmacy, Nipani.

Oscillating type granulator Hammer mill 23 August 2012 KLE College of Pharmacy, Nipani.

As part of the scale-up of a milling or sieving operation, the lubricants and glidants, which in the laboratory are usually added directly to the final blend, are usually added to the dried granulation during the sizing operation. This is done because some of these additives, especially magnesium stearate, tend to agglomerate when added in large quantities to the granulation in a blender. 23 August 2012 KLE College of Pharmacy, Nipani.

Blending Type of blending equipment often differs from that using in laboratory. In any blending operation, both segregation and mixing occur simultaneously are a function of particle size, shape, hardness, and density, and of the dynamics of the mixing action. Particle abrasion is more likely to occur when high-shear mixers with spiral screws or blades are used. When a low dose active ingredient is to be blended it may be sandwiched between two portions of directly compressible excipients to avoid loss to the surface of the blender. 23 August 2012 KLE College of Pharmacy, Nipani.

Equipments used for mixing Sigma blade mixer. Planetary mixer. Twin shell blender. High shear mixer 23 August 2012 KLE College of Pharmacy, Nipani.

Slugging (Dry Granulation)
A dry powder blend that cannot be directly compressed because of poor flow or compression properties. This is done on a tablet press designed for slugging, which operates at pressures of about 15 tons, compared with a normal tablet press, which operates at pressure of 4 tons or less. Slugs range in diameter from 1 inch, for the more easily slugged material, to ¾ inch in diameter for materials that are more difficult to compress and require more pressure per unit area to yield satisfactory compacts. If an excessive amount of fine powder is generated during the milling operation the material must be screened & fines recycled through the slugging operation. 23 August 2012 KLE College of Pharmacy, Nipani.

Dry Compaction Granulation by dry compaction can also be achieved by passing powders between two rollers that compact the material at pressure of up to 10 tons per linear inch. Materials of very low density require roller compaction to achieve a bulk density sufficient to allow encapsulation or compression. One of the best examples of this process is the densification of aluminum hydroxide. Pilot plant personnel should determine whether the final drug blend or the active ingredient could be more efficiently processed in this manner than by conventional processing in order to produce a granulation with the required tabletting or encapsulation properties. 23 August 2012 KLE College of Pharmacy, Nipani.

Dry Compaction 23 August 2012 KLE College of Pharmacy, Nipani.

Compression The ultimate test of a tablet formulation and granulation process is whether the granulation can be compressed on a high-speed tablet press. During compression, the tablet press performs the following functions: Filling of empty die cavity with granulation. Precompression of granulation (optional). Compression of granules. Ejection of the tablet from the die cavity and take-off of compressed tablet. 23 August 2012 KLE College of Pharmacy, Nipani.

Compression When evaluating the compression characteristics of a particular formulation, prolonged trial runs at press speeds equal to that to be used in normal production should be tried. Only then are potential problems such as sticking to the punch surface, tablet hardness, capping, and weight variation detected. High-speed tablet compression depends on the ability of the press to interact with granulation. Following are the parameters to be considered while choosing speed of press. Granulation feed rate. Delivery system should not change the particle size distribution. System should not cause segregation of coarse and fine particles, nor it should induce static charges. 23 August 2012 KLE College of Pharmacy, Nipani.

Compression The die feed system must be able to fill the die cavities adequately in the short period of time that the die is passing under the feed frame. The smaller the tablet , the more difficult it is to get a uniform fill a high press speeds. For high-speed machines, induced die feed systems is necessary. These are available with a variety of feed paddles and with variable speed capabilities. So that optimum feed for every granulation can be obtained. 23 August 2012 KLE College of Pharmacy, Nipani.

Compression After the die cavities are filled ,the excess is removed by the feed frame to the center of the die table. Compression of the granulation usually occurs as a single event as the heads of the punches pass over the lower and under the upper pressure rollers. This cause the punches to the penetrate the die to a preset depth, compacting the granulation to the thickness of the gap set between the punches. The rapidity and die wall time in between this press event occurs is determined by the speed at which the press is rotating and by the size of compression rollers. Larger the compressions roller, the more gradually compression force is applied and released. Slowing down the press speed or using larger compression rollers can often reduce capping in a formulation. 23 August 2012 KLE College of Pharmacy, Nipani.

Compression The final event is ejection of compressed tablets from die cavity. During compression, the granulation is compacted to form tablet, bonds within compressible material must be formed which results in sticking. High level of lubricant or over blending can result in a soft tablet, decrease in wettability of the powder and an extension of the dissolution time. Binding to die walls can also be overcome by designing the die to be to inch wider at the upper portion than at the center in order to relieve pressure during ejection. 23 August 2012 KLE College of Pharmacy, Nipani.

Compression DIFFERENT PUNCHES &DIES 23 August 2012
KLE College of Pharmacy, Nipani.

Compression MULTI ROTARY MACHINE HIGH SPEED ROTARY MACHINE 23 August 2012 KLE College of Pharmacy, Nipani.

Compression DOUBLE ROTARY MACHINE UPPER PUNCH AND LOWER PUNCH 23 August 2012 KLE College of Pharmacy, Nipani.

Compression SINGLE ROTARY MACHINE 23 August 2012 KLE College of Pharmacy, Nipani.

Tablet Coating Sugar coating is carried out in conventional coating pans, has undergone many changes because of new developments in coating technology and changes in safety and environmental regulations. The conventional sugar coating pan has given way to perforated pans or fluidized-bed coating columns. The development of new polymeric materials has resulted in a change from aqueous sugar coating and more recently, to aqueous film coating. The tablets must be sufficiently hard to withstand the tumbling to which they are subjected in either the coating pan or the coating column. 23 August 2012 KLE College of Pharmacy, Nipani.

Compression Some tablet core materials are naturally hydrophobic, and in these cases, film coating with an aqueous system may require special formulation of the tablet core and/or the coating solution. A film coating solution may have been found to work well with a particular tablet in small lab coating pan but may be totally unacceptable on a production scale. This is because of increased pressure & abrasion to which tablets are subjected when batch size is large & different in temperature and humidity to which tablets are exposed while coating and drying process. 23 August 2012 KLE College of Pharmacy, Nipani.

Pilot Plant scale-up techniques for Capsule
Capsules are solid dosage forms in which the drug substance is enclosed in either a hard or soft soluble container or shell of a suitable form of gelatin. Steps in capsule production Mixing of ingredient Granulation and lubrication Making of capsules Filling of capsules Uniformity testing Packing and labeling 23 August 2012 KLE College of Pharmacy, Nipani.

Pilot Plant scale-up techniques for Capsule
The manufacturing process for capsulated products often same to that tablets. Both tablets & capsules are produced from ingredients that may be either dry blended or wet granulated to produce a dry powder or granule mix with uniformly dispersed active ingredients. To produce capsules on high speed equipment ,the powder blend must have the uniform particle size distribution, bulk density & compressibility required to promote good flow properties & result in the formation of compact of the right size and sufficient cohesiveness to be filled in to capsule shells. 23 August 2012 KLE College of Pharmacy, Nipani.

Manufacture of Hard Gelatin Capsules
Shell composition : Gelatin : Prepared by the hydrolysis of collagen. Gelatin in its chemical and physical properties, depending upon the source of the collagen and extraction. There are two basic types of gelatin: Type – A and Type – B. The two types can be differentiated by their isoelectric points (7.0 – 9.0 for type A and 4.8 – 5.0 for type B) and by their viscosity and film forming characteristics. 23 August 2012 KLE College of Pharmacy, Nipani.

Combination of pork skin and bone gelatin are often used to optimize shell characteristics. The physicochemical properties of gelatin of most interest to shell manufactures are the bloom strength and viscosity. Colorants : Various soluble synthetic dyes (“coal tar dyes”) and insoluble pigments are used. Not only play a role in identifying the product, but also may play a role in improving patient compliance. E.g., white, analgesia; lavender, hallucinogenic effects; orange or yellow, stimulants and antidepressants. 23 August 2012 KLE College of Pharmacy, Nipani.

Opaquing agents : Titanium dioxide may be included to render the shell opaque. Opaque capsules may be employed to provide protection against light or to conceal the contents. Preservatives : When preservatives are employed, parabens are often selected. 23 August 2012 KLE College of Pharmacy, Nipani.

Shell manufacture : 23 August 2012 KLE College of Pharmacy, Nipani.

Dipping : Pairs of the stainless steel pins are dipped into the dipping solution to simultaneously form the caps and bodies. The pins are at ambient temperature; whereas the dipping solution is maintained at a temperature of about 500C in a heated, jacketed dipping pan. The length of time to cast the film has been reported to be about 12 sec. Rotation : After dipping, pins are elevated and rotated 2-1/2 times until they are facing upward. This rotation helps to distribute the gelatin over the pins uniformly and to avoid the formation of a bead at the capsule ends. 23 August 2012 KLE College of Pharmacy, Nipani.

Drying : The racks of gelatin coated pins then pass into a series of four drying oven. Drying is mainly done by dehumidification. A temperature elevation of only a less degrees is permissible to prevent film melting. Under drying will leave the films too sticky for subsequent operation. Stripping : A series of bronze jaws strip the cap and body portions of the capsules from the pins. 23 August 2012 KLE College of Pharmacy, Nipani.

Trimming : The stripped cap and body portions are delivered to collects in which they are firmly held. As the collects rotate, knives are brought against the shells to trim them to the required length. Joining : The cap and body portions are aligned concentrically in channels and the two portions are slowly pushed together. 23 August 2012 KLE College of Pharmacy, Nipani.

Sorting : The moisture content of the capsules as they are from the machine will be in the range of 15 – 18% w/w. During sorting, the capsules passing on a lighted moving conveyor are examined visually by inspectors. Defects are generally classified according to their nature and potential to cause problems in use. Printing : In general, capsules are printed before filling. Generally, printing is done on offset rotary presses having throughput capabilities as high as three-quarter million capsules per hour. 23 August 2012 KLE College of Pharmacy, Nipani.

Sizes and shapes : For human use, empty gelatin capsules are manufactured in eight sizes, ranging from 000 to 5. Capsule capacities in table: Size Volume Fill weight(g) at 0.8 g/cm3 powder density 000 1.37 1.096 00 0.95 0.760 0.68 0.544 1 0.50 0.400 2 0.37 0.296 3 0.30 0.240 4 0.21 0.168 5 0.15 0.104 23 August 2012 KLE College of Pharmacy, Nipani.

The largest size normally acceptable to patient is a No: 0. Three larger size are available for veterinary use: 10, 11, and 12 having capacities of about 30, 15, and 7.5 g, respectively. The standard shape of capsules is traditional, symmetrical bullet shape. Some manufactures have employed distinctive shapes. e.g. Lilly’s pulvule tapers to a bluntly pointed end. Smith Kline Beacham’s spansule capsules taper at both the cap and body ends. 23 August 2012 KLE College of Pharmacy, Nipani.

Sealing : Capsules are sealed and somewhat reshaped in the Etaseal process. This thermal welding process forms an indented ring around the waist of the capsule where the cap overlaps the body. Storage : Finished capsules normally contain an equilibrium moisture content of 13-16%. To maintain a relative humidity of 40-60% when handling and storing capsules. 23 August 2012 KLE College of Pharmacy, Nipani.

Filling of hard gelatin capsules
Equipment used in capsule filling operations involves one often of two types of filling systems. Zanasi or Martelli encapsulator: Forms slugs in a dosatar which is a hollow tube with a plunger to eject capsule plug. Hofliger-Karg machine: Formation of compacts in a die plate using tamping pins to form a compact. 23 August 2012 KLE College of Pharmacy, Nipani.

ZANASI AUTOMATIC CAPSULE FILLING MACHINE HOFLIGER KARG AUTOMATIC CAPSULE FILLING MACHINE 23 August 2012 KLE College of Pharmacy, Nipani.

Filling of hard gelatin capsules
In this both system, the scale-up process involve bulk density, powder flow, compressibility, and lubricant distribution. Overly lubricated granules are responsible for delaying capsule disintegration and dissolution. 23 August 2012 KLE College of Pharmacy, Nipani.

OSAKA MODEL R-180 SEMI AUTOMATIC CAPSULE FILLING MACHINE

Manufacture of Soft Gelatin Capsules
Composition of the shell: Similar to hard gelatin shells, the basic component of soft gelatin shell is gelatin; however, the shell has been plasticized. The ratio of dry plasticizer to dry gelatin determines the “hardness” of the shell and can vary from for very hard shell to for very soft shell. Up to 5% sugar may be included to give a “chewable” quality to the shell. The residual shell moisture content of finished capsules will be in the range of 6-10%. 23 August 2012 KLE College of Pharmacy, Nipani.

Formulation : Formulation for soft gelatin capsules involves liquid, rather than powder technology. Materials are generally formulated to produce the smallest possible capsule consistent with maximum stability, therapeutic effectiveness and manufacture efficiency. The liquids are limited to those that do not have an adverse effect on gelatin walls. The pH of the liquid can be between 2.5 and 7.5. Emulsion can not be filled because water will be released that will affect the shell. 23 August 2012 KLE College of Pharmacy, Nipani.

The types of vehicles used in soft gelatin capsules fall in to two main groups: Water immiscible, volatile or more likely more volatile liquids such as vegetable oils, mineral oils, medium-chain triglycerides and acetylated glycerides. Water miscible, nonvolatile liquids such as low molecular weight PEG have come in to use more recently because of their ability to mix with water readily and accelerate dissolution of dissolved or suspended drugs. All liquids used for filling must flow by gravity at a temperature of 350c or less. The sealing temperature of gelatin films is C. 23 August 2012 KLE College of Pharmacy, Nipani.

Manufacture process : Plate process : The process involved Placing the upper half of a plasticized gelatin sheet over a die plate containing numerous die pockets, Application of vacuum to draw the sheet in to the die pockets, Filling the pockets with liquor or paste, Folding the lower half of gelatin sheet back over the filled pockets, and Inserting the “ sandwich” under a die press where the capsules are formed and cut out. 23 August 2012 KLE College of Pharmacy, Nipani.

Rotary die press: In this process, the die cavities are machined in to the outer surface of the two rollers. The die pockets on the left hand roller form the left side of the capsule and the die pockets on the right hand roller form the right side of the capsule. Two plasticized gelatin ribbons are continuously and simultaneously fed with the liquid or paste fill between the rollers of the rotary die mechanism. As the die rolls rotate, the convergence of the matching die pockets seals and cuts out the filled capsules. 23 August 2012 KLE College of Pharmacy, Nipani.

Accogel process: In general, this is another rotary process involving A measuring roll, A die roll, and A sealing roll. As the measuring roll and die rolls rotate, the measured doses are transferred to the gelatin-linked pockets of the die roll. The continued rotation of the filled die converges with the rotating sealing roll where a second gelatin sheet is applied to form the other half of the capsule. Pressure developed between the die roll and sealing roll seals and cuts out the capsules. 23 August 2012 KLE College of Pharmacy, Nipani.

Bubble method: The Globex Mark II capsulator produces truly seamless, one-piece soft gelatin capsules by a “bubble method”. 23 August 2012 KLE College of Pharmacy, Nipani.

A concentric tube dispenser simultaneously discharges the molten gelatin from the outer annulus and the liquid content from the tube. By means of a pulsating pump mechanism, the liquids are discharged from the concentric tube orifice into a chilled-oil column as droplets that consists of a liquid medicament core within a molten gelatin envelop. The droplets assume a spherical shape under surface tension forces and the gelatin congeals on cooling. The finished capsules must be degreased and dried. 23 August 2012 KLE College of Pharmacy, Nipani.

Soft/Liquid-filled hard gelatin capsules
Important reason: the standard for liquid filled capsules was inability to prevent leakage from hard gelatin capsules. As banding and of self-locking hard gelatin capsules, together with the development of high-resting state viscosity fills, has now made liquid/semisolid-filled hard gelatin capsules. As with soft gelatin capsules, any materials filled into hard capsules must not dissolve, alter or otherwise adversely affect the integrity of the shell. Generally, the fill material must be pumpable. 23 August 2012 KLE College of Pharmacy, Nipani.

Soft/Liquid-filled hard gelatin capsules
Three formulation strategies based on having a high resting viscosity after filling have been described. Thixotropic formulations, Thermal-setting formulations, Mixed thermal-Thixotropic systems. The more lipophilic contents, the slower the release rate. Thus, by selecting excipients with varying HLB balance, varying release rate may be achieved. 23 August 2012 KLE College of Pharmacy, Nipani.

AUTO MATIC CAPSULE ARRANGEMNT CAPSULE POLISHING MACHINE 23 August 2012 KLE College of Pharmacy, Nipani.

Scale-up for Parenterals

Injectables The majority of the parenteral solutions are solutions requiring a variety of tankage, piping and ancillary euipment for liquid mixing, filteration, transfer and related activities. The majority of the equipments are composed of 300 series austenitic stainless steel, with tantalum or glass lined vessels employed for preparation of formulations sensitive to iron and other metal ions. The vessels can be equipped with external jackets for heating and/or cooling and various types of agitators, depending upon the mixing requirements of the individual formulation. 23 August 2012 KLE College of Pharmacy, Nipani.

Working area of a parenteral pilot plant
Incoming goods are stored in special areas for Quarantine, Released and Rejected status. A cold room is available for storage of temperature-sensitive products. Entrance into the warehouse and production areas is restricted to authorized personnel. Sampling and weighing of the raw material is performed in a dedicated sampling area and a central weighing suite, respectively. The route for final products is separated from the incoming goods; storage of final products is done in designated areas in the warehouse while they are awaiting shipment. Several clothing and cleaning procedures in the controlled transport zone and production area ensure full quality compliance. In addition, a technical area is located in between the production zone and the area for formulation development. Here, the water for injection equipment is located, as well as the technical installation of the lyophilizer. 23 August 2012 KLE College of Pharmacy, Nipani.

Lay-out of the pilot-plant

Facility Design To provide the control of microbial, pyrogen and particles controls over the production environment are essential. Warehousing: All samples should be aseptically taken, which mandates unidirectional airflow and full operator gowning. These measures reduce the potential for contamination ingress into materials that are yet to receive any processing at any site. 23 August 2012 KLE College of Pharmacy, Nipani.

Facility Design Preparation Area: The materials utilized for the production of the sterile products move toward the preparation area through a series of progressively cleaner environments. 23 August 2012 KLE College of Pharmacy, Nipani.

Preparation Area First the materials are passed through class 100,000 i.e. grade D environment for presterilization. Transfer of materials are carried out in air-locks to avoid cross contamination The preparation areas are supplied with HEPA filters. There should be more than 20 air changes per hour The preparation place is Class 100 area. 23 August 2012 KLE College of Pharmacy, Nipani.

Production area 23 August 2012 KLE College of Pharmacy, Nipani.

Production area Compounding area: The manufacture of parenterals is carried out in class 10,000 (Grade C) controlled environments in which class 100 unidirectional flow hoods are utilized to provide greater environmental control during material addition. These areas are designed to minimize the microbial, pyrogen, and particulate contamination to the formulation prior to sterilization. 23 August 2012 KLE College of Pharmacy, Nipani.

Production area Aseptic filling rooms: The filling of the formulations is performed in an Class 100 environment. Capping and Crimp sealing areas: The air supply in the capping line should be of Class 100 Corridors: They serve to interconnect the various rooms. Fill rooms, air locks and gowning rooms are assessed from the corridor. Aseptic storage rooms. Air-locks and pass-throughs: Air locks serve as a transition points between one environment and another. They are fitted with the UltraViolet lights, spray systems, or other devices that may be effectively utilized for decontamination of materials. 23 August 2012 KLE College of Pharmacy, Nipani.

Formulation aspects Solvent: The most widely used solvent used for parenteral production is water for injection. WFI is prepared by by distillation or reverse osmosis. Sterile water for injection is used as a vehicle for reconstitution of sterile solid products before administration and is terminally sterilized by autoclaving . Solubilizers: They are used to enhance and maintain the aqueous solubility of poorly water-soluble drugs. 23 August 2012 KLE College of Pharmacy, Nipani.

Formulation aspects Solubilizing agents used in sterile products include: 1. co-solvents: glycerine, ethanol, sorbitol, etc. 2. Surface active agents: polysorbate 80, polysorbate 20, lecithin. 3. Complexing agents: cyclodextrins etc They act by reducing the dielectric constant properties of the solvent system, thereby reducing the electrical, conductance capabilities of the solvent and thus increase the solubility. Antimicrobial preservative agents: 23 August 2012 KLE College of Pharmacy, Nipani.

Formulation aspects Buffers: They are used to maintain the pH level of a solution in the range that provides either maximum stability of the drug against hydrolytic degradation or maximum or optimal solubility of the drug in solution. Antioxidants: Antioxidants function by reacting prefentially with molecular oxygen and minimizing or terminating the free the free radical auto-oxidation reaction. Examples phenol ( %), m-cresol ( %) etc. 23 August 2012 KLE College of Pharmacy, Nipani.

Instrumentation Mixer Homogenizer Filteration assembly Filling machinery 23 August 2012 KLE College of Pharmacy, Nipani.

Mixer/Homogenizer 23 August 2012 KLE College of Pharmacy, Nipani.

Filtration assembly 23 August 2012 KLE College of Pharmacy, Nipani.

Bottling/Filling machinery

Sterilization and Depyrogenation
Steam sterilization Dry-heat sterilization and depyrogenation Gas and vapour sterilization Radiation sterilization Sterilization by filteration 23 August 2012 KLE College of Pharmacy, Nipani.

Aseptic processing control and evaluation
In-process Testing: End-product Testing: Process simulations: Quality Assurance Particulate matter Pyrogen test Stability test 23 August 2012 KLE College of Pharmacy, Nipani.

Particulate matter detector

Liquid orals The physical form of a drug product that is pourable displays Newtonian or pseudoplastic flow behaviour and conforms to it’s container at room temperature. Liquid dosage forms may be dispersed systems or solutions. In dispersed systems there are two or more phases, where one phase is distributed in another. A solution refers two or more substances mixed homogeneously. 23 August 2012 KLE College of Pharmacy, Nipani.

Steps of liquid manufacturing process
Planning of material requirements: Liquid preparation: Filling and Packing: Quality assurance: 23 August 2012 KLE College of Pharmacy, Nipani.

Critical aspects of liquid manufacturing
Physical Plant: Heating, ventilation and air controlling system: The effect of long processing times at suboptimal temperatures should be considered in terms of consequences on the physical or chemical stability of ingredients as well as product. 23 August 2012 KLE College of Pharmacy, Nipani.

Formulation aspects of oral liquids
Suspensions: Purpose Agent Facilitating the connection between API and vehicle -wetting agents Salt formation ingredients Protecting the API - Buffering-systems, polymers, antioxidants Maintaining the suspension appearance Colorings, suspending agent, flocculating agent. Masking the unpleasant taste/smell Sweeteners, flavorings 23 August 2012 KLE College of Pharmacy, Nipani.

Emulsions: Purpose Agent Particle Size Solid particles, Droplet particles Protecting the API Buffering-systems, antioxidants, polymers Maintaining the appearance Colorings, Emulsifying agents, Penetration enhancers, gelling agents Taste/smell masking Sweetners, flavorings 23 August 2012 KLE College of Pharmacy, Nipani.

Solutions: Protecting the API Buffers, antioxidants, preservatives Maintaining the appearance Colorings, stabilizers, cosolvents, antimicrobial preservatives Taste/smell masking Sweetners, flavorings. 23 August 2012 KLE College of Pharmacy, Nipani.

Layout of the pilot plant

Equipments Mixer Homogenizer Filteration assembly Bottling assembly 23 August 2012 KLE College of Pharmacy, Nipani.

Filtration assembly 23 August 2012 KLE College of Pharmacy, Nipani.

General flow chart Raw Materials Measured and weighed Mixing Distilled water Filling Packing Finished products storage Quality Assurance 23 August 2012 KLE College of Pharmacy, Nipani.

Quality assurance Dissolution of drugs in solution Potency of drugs in suspension Temperature uniformity in emulsions Microbiological control Product uniformity Final volume Stability 23 August 2012 KLE College of Pharmacy, Nipani.

References Lachman L. The Theory and practice of industrial pharmacy. 3rd Edition. Varghese publication house. 23 August 2012 KLE College of Pharmacy, Nipani.

E-mail : nanjwadebk@gmail.com
Thank You Cell No: 23 August 2012 KLE College of Pharmacy, Nipani.

PILOT PLANT SCALE UP TECHNIQUES

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