Primary Functions
There is a twofold mission of the chemical development group inside a pharmaceutical company. Their first function is to develop a process to manufacture the compound or biological initially for clinical trials and, at a later stage, for the manufacturing group. There is a series of necessary steps to scale a synthesis from laboratory quantity to production quantity, and each of these may require significant time and resources to complete. Biologicals are made via totally different methods that may involve fermentation, cell synthesis, extraction from natural products or plants, or other methods. The process developed for synthesis or biological production should be safe, reproducible, cost effective, and environmentally sound.
The second function of the chemical/biological group is to provide chemical compound (i.e., drug substance) of appropriate purity and quality for both clinical and preclinical trials. Synthesis of drug product for preclinical trials is primarily used for toxicology tests.
Basic Dilemma
These two functions of a chemical development group create a basic dilemma. If a chemical group spends most of its time and resources improving the process of synthesizing the active compound or working on scaleup methods, then they may not be providing adequate supplies of the drug for clinical and toxicological testing. When they spend most of their efforts developing a process, the compound may be terminated, and all of the process development and scaleup work will have been for naught. If the group eschews the process development and, instead, devotes itself to providing compound, then the need for more and more compound (
Table 107.4) will outstrip the group’s ability to provide it on schedule. The group may not have researched the scaleup adequately so that they cannot simply convert to a larger scale synthesis. Furthermore, the new process is likely to produce compound with a new impurity profile, which may lead to regulatory (toxicology) questions. Thus, the chemical group risks being the rate-limiting factor in the drug’s development.
The best solution to this dilemma is to spend most of the group’s efforts on providing compound early in the project’s life
and to spend more time on process development as the compound enters Phase 3. Of course, the strategy chosen must depend to some degree on regulatory and business pressures. Regulatory authorities are tending to request more process development and validation of the process at an earlier stage of development.
Issues Relating to Scaleup of the Chemical Synthesis
One goal of chemical development is to minimize the number of separate chemical steps required in a drug’s synthesis. Advantages of fewer chemical reactions are both practical and economical. This goal may be addressed by (a) exploring alternative synthetic routes early in the development process, (b) purchasing raw materials that are closer to the final synthetic step or that allow the chemists to reach the final step more easily, or (c) contracting the manufacture of dangerous, toxic, or highly specialized steps to other companies.
It is rarely possible to go directly from a laboratory scale of synthesizing milligrams or grams to a manufacturing scale where hundreds of kilograms or even metric tons of a chemical may be required. Scaleup often requires chemists and chemical engineers who were not involved in the original laboratory syntheses. Large glassware containers are used to make greater amounts of a drug. Still larger nonglassware reactors are used at the pilot plant scale. This is a stage between laboratory scale and manufacturing scale. Monitoring and testing systems must be developed to evaluate the performance and ruggedness of the various chemical stages. This must be done during the chemical operations and after each step in the synthesis to assure that quality, purity, and yield are maintained. One objective of this process is to fully automate these operations. The number of separate scaleup stages a drug goes through should be minimized.
The number of separate scaleup stages necessary in a pilot plant depends on the drug and problems encountered. One of the many reasons why problems arise is that numerous aspects of scaleup cannot be directly extrapolated from one size of a chemical vessel to a larger size. For example, (a) the temperature gradients may vary more in a larger vessel, (b) there are mechanical differences in stirring (e.g., shear forces), (c) a loss of visual observation occurs because the metal reactors used are opaque, (d) the changing surface-to-volume ratio that occurs is critical to heat transfer, and (e) the mechanical handling operations generally take longer on a larger scale. All of these factors may contribute to the variable performance of the process. These factors and others can markedly affect the chemical reaction and results obtained. The general quantities used for various functions are summarized in
Table 107.5.
Process Development
The chemical development staff must balance priorities and available resources to successfully complete process development and provide project support work. Chemical development specialists modify or develop new synthetic routes for ultimate use in production. Their goal may be to improve bulk drug yields or purity, decrease costs, or eliminate manufacturing hazards and toxic byproducts. At the same time, an adequate supply of drug substance must be generated to continue the various development activities (e.g., toxicology, clinical trials) on the project. Resource issues typically involve shortages in (a) personnel assigned to the work, (b) available starting materials, (c) available equipment, or (d) time to explore fully new chemical technologies. This is sometimes the central dilemma in a compound’s development.
Safety of the Process
Safety is a critically important factor to consider in improving the process of synthesis and scaleup. Some of the primary factors to consider in this regard are as follows:
Temperature changes occur more slowly in large-scale reactions.
Thermodynamics must ascertain whether the reaction is safe and will not “run away” (i.e., autocatalysis).
Increasing the temperature of a reaction by 10°C may double its rate of reaction. This may cause unwanted byproducts, reduce yield, influence product uniformity, and affect equipment functioning.
Heat must be removed from the reacting ingredients rapidly at precisely the right time to stop the process at the desired juncture.
Reproducibility of the Process
The underlying principle in scaleup is that a reaction at one size of a vessel may behave differently at a larger scale. As an example, consider the following. A six-inch-diameter stirrer in a small flask has its tip moving at 4.5 feet per second. The propeller-driven agitator in a 200-gallon reactor with a diameter of 30 inches has its tip moving at 13 feet per second. The tip could beat the crystals of the reaction into small particles and change the product’s uniformity, yield, purity, shape, density, and consistency.
Cost Effectiveness of the Process
The cost of synthesizing a compound is based on (a) material costs, (b) labor costs, (c) overhead costs, and (d) yield. Overhead refers, in part, to the specific equipment used and how long it is used, as well as to other plant operations.
Some routes of synthesis are more cost effective than others. The major factors include the costs of starting materials, number of steps involved, batch processing parameters, and cost of environmental cleanup. If starting materials are impure or unavailable, it may be necessary to synthesize them or to find other suppliers.
Environmental Cleanup of the Process
Waste materials are recycled if possible and cost effective. More regulations are being passed that require companies to control emissions of reactors, evaluate all waste streams, and perform environmental assessments. Incinerators sometimes have scrubbers in them to clear materials burned. If possible, expensive and volatile solvents are recovered.
Table 107.6 lists the sections of an environmental impact analysis that must be included in a New Drug Application (
NDA). Costs for environmental cleanup are rising rapidly.
Synopsis of the Process
Modern chemical reactors are like giant thermos containers (i.e., metal containers, usually stainless steel, around a glass-lined interior). Fluids flow between these two layers to heat or cool the contents. Heat is generally applied with steam, and cooling is done by refrigerated glycol or running water.
After a chemical reaction is complete, it is often necessary to separate two immiscible layers where the less dense phase is on top of the denser phase. In a glass flask, it is easy to see the two layers and to separate them, whereas that is impossible in a stainless steel reactor. This problem is solved by removing the lower (i.e., heavier) fluid through a small glass opening through a spout until the other colored fluid is observed at the interface. If the two fluids are both uncolored or the same color, then a nonreactive dye could be added to color one of the phases and thereby facilitate the separation.
The product is then isolated from solution with a solvent remover. The solvent can be evaporated away to crystallize the product from solution or spray dried to yield a crystalline product. The solid material is then isolated by filtration, centrifugation, or recrystallization and then washed a number of times, milled, and dried. A vacuum oven may be used with material on drying trays, or a tumble dryer may be used.
Development of Optically Pure Drugs
The issues and debate surrounding chirality (i.e., molecules with one or more asymmetric centers) and the development of optically pure drugs have become more intense in recent years. In the past, companies developed optically pure drugs (i.e., single enantiomers) when it was clear to them that racemates (i.e., a compound with an equal proportion of enantiomers) were less safe or less potent. New biotechnology methods have made the isolation and scaleup of optically pure enantiomers more practical. Some companies have exploited these technologies by patenting isomers of well-known drugs that were not patented by the originator. After a couple of examples of this occurrence, companies rapidly learned the necessity of patenting each of the enantiomers as well as the racemate of all of their new compounds.
The Food and Drug Administration (
FDA) issued the “Policy Statement for the Development of New Stereoisomeric Drugs” in 1992 (
FDA 1992). The document discusses three categories of compounds: (a) those where both enantiomers have similar desirable actions (e.g., ibuprofen), (b) those where one enantiomer is active and the other is inactive (e.g., propranolol), and (c) those where the enantiomers have different activities (e.g., sotalol). The policy statement advocates clinical evaluation of both enantiomers even if only one is chosen to be developed or if the racemate is developed. The major point is that a company must examine the issue scientifically during the early development period and reach a rational conclusion before Phase 2 trials are completed.
This policy is reasonable in that it does not consider all clinical drugs as a single group and also because it encourages development choices of enantiomers to be based on good science and logic. It rejects the claims of some scientists that all new drugs should be single enantiomers.
A single enantiomer should be developed if it is easy to synthesize and if it has improved clinical activities than the racemate. Other reasons to develop a single enantiomer are ease of development to obtain absorption, metabolism, excretion, or physiological advantages. Racemates should be developed if there is a rapid interconversion of enantiomers, if individual enantiomers are difficult to synthesize, or if the separate enantiomers have similar activity and safety profiles.