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`Inspection Guides > Lyophilization of Parenteral (7/93)
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`U.S. Food and Drug Administration
`Protecting and Promoting Your Health
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`Lyophilization of Parenteral (7/93)
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`GUIDE TO INSPECTIONS OF LYOPHILIZATION OF PARENTERALS
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`Note: This document is reference material for investigators and other FDA personnel. The
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`document does not bind FDA, and does no confer any rights, privileges, benefits, or
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`immunities for or on any person(s).
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`INTRODUCTION
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`Lyophilization or freeze drying is a process in which water is removed from a product after it is
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`frozen and placed under a vacuum, allowing the ice to change directly from solid to vapor without
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`passing through a liquid phase. The process consists of three separate, unique, and
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`interdependent processes; freezing, primary drying (sublimation), and secondary drying
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`(desorption).
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`The advantages of lyophilization include:
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`Ease of processing a liquid, which simplifies aseptic handling
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`Enhanced stability of a dry powder
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`Removal of water without excessive heating of the product
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`Enhanced product stability in a dry state
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`Rapid and easy dissolution of reconstituted product
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`Disadvantages of lyophilization include:
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`Increased handling and processing time
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`Need for sterile diluent upon reconstitution
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`Cost and complexity of equipment
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`The lyophilization process generally includes the following steps:
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`- Dissolving the drug and excipients in a suitable solvent, generally water for injection (WFI).
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`- Sterilizing the bulk solution by passing it through a 0.22 micron bacteria-retentive filter.
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`- Filling into individual sterile containers and partially stoppering the containers under aseptic
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`conditions.
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`- Transporting the partially stoppered containers to the lyophilizer and loading into the chamber
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`under aseptic conditions.
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`- Freezing the solution by placing the partially stoppered containers on cooled shelves in a
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`freeze-drying chamber or pre-freezing in another chamber.
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`- Applying a vacuum to the chamber and heating the shelves in order to evaporate the water from
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`the frozen state.
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`- Complete stoppering of the vials usually by hydraulic or screw rod stoppering mechanisms
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`installed in the lyophilizers.
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`There are many new parenteral products, including anti-infectives, biotechnology derived products,
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`and in-vitro diagnostics which are manufactured as lyophilized products. Additionally, inspections
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`have disclosed potency, sterility and stability problems associated with the manufacture and
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`control of lyophilized products. In order to provide guidance and information to investigators, some
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`industry procedures and deficiencies associated with lyophilized products are identified in this
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`Inspection Guide.
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`It is recognized that there is complex technology associated with the manufacture and control of a
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`lyophilized pharmaceutical dosage form. Some of the important aspects of these operations
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`include: the formulation of solutions; filling of vials and validation of the filling operation; sterilization
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`and engineering aspects of the lyophilizer; scale-up and validation of the lyophilization cycle; and
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`testing of the end product. This discussion will address some of the problems associated with the
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`manufacture and control of a lyophilized dosage form.
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`PRODUCT TYPEIFORMULATION
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`Products are manufactured in the lyophilized form due to their instability when in solution. Many of
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`the antibiotics, such as some of the semi-synthetic penicillins, cephalosporins, and also some of
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`the salts of erythromycin, doxycycline and chloramphenicol are made by the lyophilization process.
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`Because they are antibiotics, low bioburden of these formulations would be expected at the time of
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`batching. However, some of the other dosage forms that are lyophilized, such as hydrocortisone
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`sodium succinate, methylprednisolone sodium succinate and many of the biotechnology derived
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`products, have no antibacterial effect when in solution.
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`For these types of products, bioburden should be minimal and the bioburden should be determined
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`prior to sterilization of these bulk solutions prior to filling. Obviously, the batching or compounding
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`of these bulk solutions should be controlled in order to prevent any potential increase in
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`microbiological levels that may occur up to the time that the bulk solutions are filtered (sterilized).
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`The concern with any microbiological level is the possible increase in endotoxins that may develop.
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`Good practice for the compounding of lyophilized products would also include batching in a
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`controlled environment and in sealed tanks, particularly if the solution is to be held for any length of
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`time prior to sterilization.
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`In some cases, manufacturers have performed bioburden testing on bulk solutions after
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`prefiltration and prior to final filtration. While the testing of such solutions may be meaningful in
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`determining the bioburden for sterilization, it does not provide any information regarding the
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`potential formation or presence of endotoxins. While the testing of 0.1 ml samples by LAL methods
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`of bulk solution for endotoxins is of value, testing of at least 100 ml size samples prior to
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`prefiltration, particularly for the presence of gram negative organisms, would be of greater value in
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`evaluating the process. For example, the presence of Pseudomonas sp. in the bioburden of a bulk
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`solution has been identified as an objectionable condition.
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`FILLING
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`The filling of vials that are to be lyophilized has some problems that are somewhat unique. The
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`stopper is placed on top of the vial and is ultimately seated in the lyophilizer. As a result the
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`contents of the vial are subject to contamination until they are actually sealed.
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`Validation of filling operations should include media fills and the sampling of critical surfaces and
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`air during active filling (dynamic conditions).
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`Because of the active involvement of people in filling and aseptic manipulations, an environmental
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`program should also include an evaluation of microbiological levels on people working in aseptic
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`processing areas. One method of evaluation of the training of operators working in aseptic
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`processing facilities includes the surface monitoring of gloves and/or gowns on a daily basis.
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`Manufacturers are actively sampling the surfaces of personnel working in aseptic processing
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`areas. A reference which provides for this type of monitoring is the USP XXII discussion of the
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`Interpretation of Sterility Test Results. It states under the heading of "|nterpretation of Quality
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`Control Tests" that review consideration should be paid to environmental control data,
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`including...microbial monitoring, records of operators, gowns, gloves, and garbing practices. In
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`those situations in which manufacturers have failed to perform some type of personnel monitoring,
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`or monitoring has shown unacceptable levels of contamination, regulatory situations have resulted.
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`Typically, vials to be lyophilized are partially stoppered by machine. However, some filling lines
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`have been noted which utilize an operator to place each stopper on top of the vial by hand. At this
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`time, it would seem that it would be difficult for a manufacturer to justify a hand-stoppering
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`operation, even if sterile forceps are employed, in any type of operation other than filling a clinical
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`batch or very small number of units. Significant regulatory situations have resulted when some
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`manufacturers have hand-stoppered vials. Again, the concern is the immediate avenue of
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`contamination offered by the operator. It is well recognized that people are the major source of
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`contamination in an aseptic processing filling operation. The longer a person works in an aseptic
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`operation, the more microorganisms will be shed and the greater the probability of contamination.
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`Once filled and partially stoppered, vials are transported and loaded into the lyophilizer. The
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`transfer and handling, such as loading of the lyophilizer, should take place under primary barriers,
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`such as the laminar flow hoods under which the vials were filled. Validation of this handling should
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`also include the use media fills.
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`Regarding the filling of sterile media, there are some manufacturers who carry out a partial
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`lyophilization cycle and freeze the media. While this could seem to greater mimic the process, the
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`freezing of media could reduce microbial levels of some contaminants. Since the purpose of the
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`media fill is to evaluate and justify the aseptic capabilities of the process, the people and the
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`system, the possible reduction of microbiological levels after aseptic manipulation by freezing
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`would not be warranted. The purpose of a media fill is not to determine the lethality of freezing and
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`its effect on any microbial contaminants that might be present.
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`In an effort to identify the particular sections of filling and aseptic manipulation that might introduce
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`contamination, several manufacturers have resorted to expanded media fills. That is, they have
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`filled approximately 9000 vials during a media fill and segmented the fill into three stages. One
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`stage has included filling of 3000 vials and stoppering on line; another stage included filling 3000
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`vials, transportation to the lyophilizer and then stoppering; a third stage included the filling of 3000
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`vials, loading in the lyophilizer, and exposure to a portion of the nitrogen fiush and then stoppering.
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`Since lyophilizer sterilization and sterilization of the nitrogen system used to backfill require
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`separate validation, media fills should primarily validate the filling, transportation and loading
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`aseptic operations.
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`The question of the number of units needed for media fills when the capacity of the process is less
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`than 3000 units is frequently asked, particularly for clinical products. Again, the purpose of the
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`media fill is to assure that product can be aseptically processed without contamination under
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`operating conditions. It would seem, therefore, that the maximum number of units of media filled be
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`equivalent to the maximum batch size if it is less than 3000 units.
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`After filling, dosage units are transported to the Iyophilizer by metal trays. Usually, the bottom of
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`the trays are removed after the dosage units are loaded into the Iyophilizer. Thus, the dosage units
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`lie directly on the Iyophilizer shelf. There have been some situations in which manufacturers have
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`loaded the dosage units on metal trays which were not removed. Unfortunately, at one
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`manufacturer, the trays warped which caused a moisture problem in some dosage units in a batch.
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`In the transport of vials to the Iyophilizer, since they are not sealed, there is concern for the
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`potential for contamination. During inspections and in the review of new facilities, the failure to
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`provide laminar flow coverage or a primary barrier for the transport and loading areas of a
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`Iyophilizer has been regarded as an objectionable condition. One manufacturer as a means of
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`correction developed a laminar fiow cart to transport the vials from the filling line to the Iyophilizer.
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`Other manufacturers building new facilities have located the filling line close to the Iyophilizer and
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`have provided a primary barrier extending from the filling line to the Iyophilizer.
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`In order to correct this type of problem, another manufacturer installed a vertical laminar flow hood
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`between the filling line and Iyophilizer. Initially, high velocities with inadequate return caused a
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`contamination problem in a media fill. It was speculated that new air currents resulted in rebound
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`contamination off the floor. Fortunately, media fills and smoke studies provided enough meaningful
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`information that the problem could be corrected prior to the manufacture of product. Typically, the
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`lyophilization process includes the stoppering of vials in the chamber.
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`Another major concern with the filling operation is assurance of fill volumes. Obviously, a low fill
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`would represent a subpotency in the vial. Unlike a powder or liquid fill, a low fill would not be
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`readily apparent after lyophilization particularly for a biopharmaceutical drug product where the
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`active ingredient may be only a milligram. Because of the clinical significance, sub-potency in a vial
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`potentially can be a very serious situation.
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`For example, in the inspection of a lyophilization filling operation, it was noted that the firm was
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`having a filling problem. The gate on the filling line was not coordinated with the filling syringes,
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`and splashing and partial filling was occurring. It was also observed that some of the partially filled
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`vials were loaded into the Iyophilizer. This resulted in rejection of the batch.
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`On occasion, it has been seen that production operators monitoring fill volumes record these fill
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`volumes only after adjustments are made. Therefore, good practice and a good quality assurance
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`program would include the frequent monitoring of the volume of fill, such as every 15 minutes.
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`Good practice would also include provisions for the isolation of particular sections of filling
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`operations when low or high fills are encountered.
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`There are some atypical filling operations which have not been discussed. For example, there have
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`also been some situations in which lyophilization is performed on trays of solution rather than in
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`vials. Based on the current technology available, it would seem that for a sterile product, it would
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`be difficult to justify this procedure.
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`The dual chamber vial also presents additional requirements for aseptic manipulations. Media fills
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`should include the filling of media in both chambers. Also, the diluent in these vials should contain
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`a preservative. (Without a preservative, the filling of diluent would be analogous to the filling of
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`media. In such cases, a 0% level of contamination would be expected.)
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`LYOPHILIZATION CYCLE AND CONTROLS
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`After sterilization of the lyophilizer and aseptic loading, the initial step is freezing the solution. In
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`some cycles, the shelves are at the temperature needed for freezing, while for other cycles, the
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`product is loaded and then the shelves are taken to the freezing temperature necessary for product
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`freeze. In those cycles in which the shelves are precooled prior to loading, there is concern for any
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`ice formation on shelves prior to loading. Ice on shelves prior to loading can cause partial or
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`complete stoppering of vials prior to lyophilization of the product. A recent field complaint of a
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`product in solution and not lyophilized was attributed to preliminary stoppering of a few vials prior
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`to exposure to the lyophilization cycle. Unfortunately, the firm's 100% vial inspection failed to
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`identify the defective vial.
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`Typically, the product is frozen at a temperature well below the eutectic point.
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`The scale-up and change of lyophilization cycles, including the freezing procedures, have
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`presented some problems. Studies have shown the rate and manner of freezing may affect the
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`quality of the lyophilized product. For example, slow freezing leads to the formation of larger ice
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`crystals. This results in relatively large voids, which aid in the escape of water vapor during
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`sublimation. On the other hand, slow freezing can increase concentration shifts of components.
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`Also, the rate and manner of freezing has been shown to have an affect on the physical form
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`(polymorph) of the drug substance.
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`It is desirable after freezing and during primary drying to hold the drying temperature (in the
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`product) at least 4-50 below the eutectic point. Obviously, the manufacturer should know the
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`eutectic point and have the necessary instrumentation to assure the uniformity of product
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`temperatures. The lyophilizer should also have the necessary instrumentation to control and record
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`the key process parameters. These include: shelf temperature, product temperature, condenser
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`temperature, chamber pressure and condenser pressure. The manufacturing directions should
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`provide for time, temperature and pressure limits necessary for a Iyophilization cycle for a product.
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`The monitoring of product temperature is particularly important for those cycles for which there are
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`atypical operating procedures, such as power failures or equipment breakdown.
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`Electromechanical control of a Iyophilization cycle has utilized cam-type recorder-controllers.
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`However, newer units provide for microcomputer control of the freeze drying process. A very basic
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`requirement for a computer controlled process is a flow chart or logic. Typically, operator
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`involvement in a computer controlled Iyophilization cycle primarily occurs at the beginning. It
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`consists of loading the chamber, inserting temperature probes in product vials, and entering cycle
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`parameters such as shelf temperature for freezing, product freeze temperature, freezing soak time,
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`primary drying shelf temperature and cabinet pressure, product temperature for establishment of fill
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`vacuum, secondary drying shelf temperature, and secondary drying time.
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`In some cases, manufacturers have had to continuously make adjustments in cycles as they were
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`being run. In these situations, the Iyophilization process was found to be non-validated.
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`Validation of the software program of a lyophilizer follows the same criteria as that for other
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`processes. Basic concerns include software development, modifications and security. The Guide to
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`Inspection of Computerized Systems in Drug Processing contains a discussion on potential
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`problem areas relating to computer systems. A Guide to the Inspection of Software Development
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`Activities is a reference that provides a more detailed review of software requirements.
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`Leakage into a lyophilizer may originate from various sources. As in any vacuum chamber, leakage
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`can occur from the atmosphere into the vessel itself. Other sources are media employed within the
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`system to perform the lyophilizing task. These would be the thermal fluid circulated through the
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`shelves for product heating and cooling, the refrigerant employed inside the vapor condenser
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`cooling surface and oil vapors that may migrate back from the vacuum pumping system.
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`Any one, or a combination of all, can contribute to the leakage of gases and vapors into the
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`system. It is necessary to monitor the leak rate periodically to maintain the integrity of the system.
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`It is also necessary, should the leak rate exceed specified limits, to determine the actual leak site
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`for purposes of repair.
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`Thus, it would be beneficial to perform a leak test at some time after sterilization, possibly at the
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`beginning of the cycle or prior to stoppering. The time and frequency for performing the leak test
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`will vary and will depend on the data developed during the cycle validation. The pressure rise
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`found acceptable at validation should be used to determine the acceptable pressure rise during
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`production. A limit and what action is to be taken if excessive leakage is found should be
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`addressed in some type of operating document.
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`In order to minimize oil vapor migration, some Iyophilizers are designed with a tortuous path
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`between the vacuum pump and chamber. For example, one fabricator installed an oil trap in the
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`line between the vacuum pump and chamber in a Iyophilizer with an internal condenser. Leakage
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`can also be identified by sampling surfaces in the chamber after lyophilization for contaminants.
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`One could conclude that if contamination is found on a chamber surface after lyophilization, then
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`dosage units in the chamber could also be contaminated. It is a good practice as part of the
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`validation of cleaning of the lyophilization chamber to sample the surfaces both before and after
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`cleaning.
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`Because of the lengthy cycle runs and strain on machinery, it is not unusual to see equipment
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`malfunction or fail during a lyophilization cycle. There should be provisions in place for the
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`corrective action to be taken when these atypical situations occur. In addition to documentation of
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`the malfunction, there should be an evaluation of the possible effects on the product (e.g., partial or
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`complete meltback. Refer to subsequent discussion). Merely testing samples after the
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`lyophilization cycle is concluded may be insufficient to justify the release of the remaining units. For
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`example, the leakage of chamber shelf fluid into the chamber or a break in sterility would be cause
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`for rejection of the batch.
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`The review of Preventive Maintenance Logs, as well as Quality Assurance Alert Notices,
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`Discrepancy Reports, and Investigation Reports will help to identify problem batches when there
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`are equipment malfunctions or power failures. It is recommended that these records be reviewed
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`early in the inspection.
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`CYCLE VALIDATION
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`Many manufacturers file (in applications) their normal lyophilization cycles and validate the
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`lyophilization process based on these cycles. Unfortunately, such data would be of little value to
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`substantiate shorter or abnormal cycles. In some cases, manufacturers are unaware of the eutectic
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`point. It would be difficult for a manufacturer to evaluate partial or abnormal cycles without knowing
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`the eutectic point and the cycle parameters needed to facilitate primary drying.
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`Scale-up for the Iyophilized product requires a knowledge of the many variables that may have an
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`effect on the product. Some of the variables would include freezing rate and temperature ramping
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`rate. As with the scale-up of other drug products, there should be a development report that
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`discusses the process and logic for the cycle. Probably more so than any other product, scale-up
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`of the lyophilization cycle is very difficult.
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`There are some manufacturers that market multiple strengths, vial sizes and have different batch
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`sizes. It is conceivable and probable that each will have its own cycle parameters. A manufacturer
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`that has one cycle for multiple strengths of the same product probably has done a poor job of
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`developing the cycle and probably has not adequately validated their process. Investigators should
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`review the reports and data that support the filed Iyophilization cycle.
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`LYOPHILIZER STERILIZATIONIDESIGN
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`The sterilization of the lyophilizer is one of the more frequently encountered problems noted during
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`inspections. Some of the older lyophilizers cannot tolerate steam under pressure, and sterilization
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`is marginal at best. These lyophilizers can only have their inside surfaces wiped with a chemical
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`agent that may be a sterilant but usually has been found to be a sanitizing agent. Unfortunately,
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`piping such as that for the administration of inert gas (usually nitrogen) and sterile air for backfill or
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`vacuum break is often inaccessible to such surface "sterilization" or treatment. It would seem very
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`difficult for a manufacturer to be able to demonstrate satisfactory validation of sterilization of a
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`lyophilizer by chemical "treatment".
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`Another method of sterilization that has been practiced is the use of gaseous ethylene oxide. As
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`with any ethylene oxide treatment, humidification is necessary. Providing a method for introducing
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`the sterile moisture with uniformity has been found to be difficult.
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`A manufacturer has been observed employing Water For Injection as a final wash or rinse of the
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`lyophilizer. While the chamber was wet, it was then ethylene oxide gas sterilized. As discussed
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`above, this may be satisfactory for the chamber but inadequate for associated plumbing.
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`Another problem associated with ethylene oxide is the residue. One manufacturer had a common
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`ethylene oxide/nitrogen supply line to a number of lyophilizers connected in parallel to the system.
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`Thus, there could be some ethylene oxide in the nitrogen supply line during the backfilling step.
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`Obviously, this type of system is objectionable.
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`A generally recognized acceptable method of sterilizing the lyophilizer is through the use of moist
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`steam under pressure. Sterilization procedures should parallel that of an autoclave, and a typical
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`system should include two independent temperature sensing systems. One would be used to
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`control and record temperatures of the cycle as with sterilizers, and the other would be in the cold
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`spot of the chamber. As with autoclaves, lyophilizers should have drains with atmospheric breaks
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`to prevent back siphonage.
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`As discussed, there should also be provisions for sterilizing the inert gas or air and the supply
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`lines. Some manufacturers have chosen to locate the sterilizing filters in a port of the chamber. The
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`port is steam sterilized when the chamber is sterilized, and then the sterilizing filter, previously
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`sterilized, is aseptically connected to the chamber. Some manufacturers have chosen to sterilize
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`the filter and downstream piping to the chamber in place. Typical sterilization-in-place of filters may
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`require steaming of both to obtain sufficient temperatures. In this type of system, there should be
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`provisions for removing and/or draining condensate. The failure to sterilize nitrogen and air filters
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`and the piping downstream leading into the chamber has been identified as a problem on a
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`number of inspections.
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`Since these filters are used to sterilize inert gas and/or air, there should be some assurance of
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`their integrity. Some inspections have disclosed a lack of integrity testing of the inert gas and/or air
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`filter. The question is frequently asked how often should the vent filter be tested for integrity? As
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`with many decisions made by manufacturers, there is a level of risk associated with the operation,
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`process or system, which only the manufacturer can decide. If the sterilizing filter is found to pass
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`the integrity test after several uses or batches, then one could claim its integrity for the previous
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`batches. However, if it is only tested after several batches have been processed and if found to fail
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`the integrity test, then one could question the sterility of all of the previous batches processed. In
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`an effort to minimize this risk, some manufacturers have resorted to redundant filtration.
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`For most cycles, stoppering occurs within the lyophilizer. Typically, the lyophilizer has some type of
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`rod or rods (ram) which enter the immediate chamber at the time of stoppering. Once the rod
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`enters the chamber, there is the potential for contamination of the chamber. However, since the
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`vials are stoppered, there is no avenue for contamination of the vials in the chamber which are now
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`stoppered. Generally, lyophilizers should be sterilized after each cycle because of the potential for
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`contamination of the shelf support rods. Additionally, the physical act of removing vials and
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`cleaning the chamber can increase levels of contamination.
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`In some of the larger units, the shelves are collapsed after sterilization to facilitate loading.
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`Obviously, the portions of the ram entering the chamber to collapse the shelves enters from a non-
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`sterile area. Attempts to minimize contamination have included wiping the ram with a sanitizing
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`agent prior to loading. Control aspects have included testing the ram for microbiological
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`contamination, testing it for residues of hydraulic fluid, and testing the fluid for its bacteriostatic
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`effectiveness. One lyophilizer fabricator has proposed developing a flexible "skirt" to cover the ram.
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`In addition to microbiological concerns with hydraulic fluid, there is also the concern with product
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`contamination.
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`During steam sterilization of the chamber, there should be space between shelves that permit
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`passage of free flowing steam. Some manufacturers have placed "spacers" between shelves to
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`prevent their total collapse. Others have resorted to a two phase sterilization of the chamber. The
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`initial phase provides for sterilization of the shelves when they are separated. The second phase
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`provides for sterilization of the chamber and piston with the shelves collapsed.
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`http://www.fda.gov/IC EC I/Inspections/lnspecfi onGuides/ucm074909.htm
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`10/23
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`FRESENIUS KABI 1026-0010
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`10/16/2015
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`Inspection Guides > Lyophilization of Parenteral (7/93)
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`Typically, biological indicators are used in lyophilizers to validate the steam sterilization cycle. One
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`manufacturer of a Biopharmaceutical product was found to have a positive biological indicator after
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`sterilization at 1210C for 45 minutes. During the chamber sterilization, trays used to transport vials
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`from the filling line to the chamber were also sterilized. The trays were sterilized in an inverted
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`position on shelves in the chamber. It is believed that the positive biological indicator is the result of
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`poor steam penetration under these trays.
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`The sterilization of condensers is also a major issue that warrants discussion. Most of the newer
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`units provide for the capability of sterilization of the condenser along with the chamber, even if the
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`condenser is external to the chamber. This provides a greater assurance of sterility, particularly in
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`those situations in which there is some equipment malfunction and the vacuum in the chamber is
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`deeper than in the condenser.
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`Malfunctions that can occur, which would indicate that sterilization of the condenser is warranted,
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`include vacuum pump breakdown, refrigeration system failures and the potential for contamination
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`by the large valve between the condenser and chamber. This is particularly true for those units that
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`have separate vacuum pumps for both the condenser and chamber. When there are problems with
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`the systems in the lyophilizer, contamination could migrate from the condenser back to the
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`chamber. It is recognized that the condenser is not able to be sterilized in many of the older units,
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`and this represents a major problem, particularly in those cycles in which there is some equipment
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`and/or operator failure.
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`As referenced above, leakage during a lyophilization cycle can occur, and the door seal or gasket
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`presents an avenue of entry for contaminants. For example, in an inspection, it was noted that
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`during steam sterilization of a lyophilizer, steam was leaking from the unit. If steam could leak from
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`a unit during sterilization, air could possibly enter the chamber during lyophilization.
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`Some of the newer lyophilizers have double doors - one for loading and the other for unloading.
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`The typical single door lyophilizer opens in the clean area only, and contamination between loads
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`would be minimal. This clean area, previously discussed, represents a critical processing area for a
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`product made by aseptic processing. In most units, only the piston raising/lowering shelves is the
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`source of contamination. For a double door system unloading the lyophilizer in a non-sterile
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`environment, other problems may occur. The non-sterile environment presents a direct avenue of
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`contamination of the chamber when unloading, and door controls similar to double door sterilizers
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`should be in place.
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`Obviously, the lyophilizer chamber is to be sterilized between batches because of the direct means
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`of contamination. A problem which may be significant is that of leakage through the door seal. For
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`the single door unit, leakage prior to stoppering around the door seal is not a major problem from a
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`http://www.fd